ПАРОТУРБИННАЯ УСТАНОВКА

Изобретение относится к паротурбинной установке с множеством расположенных на общем валу турбины ступеней давления. В паротурбинной установке (1) с множеством расположенных на общем валу турбины (6) ступеней давления (4а, 4b) для особенно компактной конструкции согласно изобретению конденсатор (10) расположен в аксиальном направлении вала турбины (6) на стороне оттока, а подогреватель питательной воды (14) выполнен модульным. Подогреватель питательной воды (14) при этом содержит множество теплообменных модулей (20, 22), обогреваемых паром отбора (АN, АH) из одной или каждой ступени давления (4а, 4b) и расположенных в общем корпусе (24), которые включены на стороне питательной воды последовательно, а на стороне пара отбора параллельно. Общая для теплообменных модулей (20, 22) сборная шина (38) для конденсированного пара отбора (АK) расположена в корпусе (24). Изобретение позволяет повысить компактность паротурбинной установки и упростить ее монтаж. 3 з.п. ф-лы, 1 ил.

ЛУННАЯ СИЛОВАЯ УСТАНОВКА

Полезная модель относится к космической технике и предназначена для производства электроэнергии на Луне или ином небесном теле лунного типа. Технической задачей является упрощение конструкции, повышение надежности и эффективности. Установка содержит котел 1, закрепленный на камере 2. Камера установлена на опоре 3, размещенной в заглублении 8 в лунном грунте в зоне вечной мерзлоты. Камера 2 разделена на две секции. Турбина 7 размещена в верхней секции камеры, которая соединена с выходом котла. Секция 6 камеры, являющаяся конденсатором, соединена через конденсатный насос со входом котла 1. Электрогенератор 9 связан с турбиной 7. При нагревании котла солнечной радиацией жидкость в котле превращается в пар, который вращает турбогенератор. Отработанный пар конденсируется в холодной секции 6 (холод обеспечивает вечная мерзлота) и перекачивается обратно в котел, который оборудован следящим за солнцем приводом. 1 осн. п-т формулы, 2 илл.

ПАРОГАЗОВАЯ ЭНЕРГЕТИЧЕСКАЯ УСТАНОВКА

Установка предназначена для использования в теплоэнергетике, в частности на электрических станциях с теплофикационными установками. Установка содержит высокоманевренную газотурбинную установку, выполненную на базе двухконтурного газотурбинного двигателя с переменной степенью двухконтурности, с промежуточным охлаждением воздуха при сжатии и с промежуточным подогревом газа при расширении. Наличие значительного числа регулируемых элементов (входных направляющих аппаратов компрессоров низкого и высокого давления; сопловых аппаратов турбин) согласно изобретению обеспечивает маневренность и экономичную работу в трех режимах: базовом, в режиме снятия пиковых нагрузок и в режиме частичной нагрузки. 1 ил.

ИМПУЛЬСНАЯ ЭНЕРГЕТИЧЕСКАЯ УСТАНОВКА ЧЕКУНКОВА

Импульсная установка может быть использована для преобразования тепловой энергии в механическую в различных отраслях: теплоэнергетике, энергомашиностроении и т.д. Установка содержит испаритель, конденсатор, двигатель и контуры, подводящие и отводящие рабочее тело. Крутильный элемент двигателя - ротор имеет круглое сплошное сечение, а по его наружному периметру равномерно выполнены прямоугольные пазы, подводящий и отводящий контуры подключены к двигателю посредством отверстий подвода и отвода рабочего тела, выполненных в корпусе по касательным к его наружному периметру с возможностью совмещения с пазами ротора. Причем на выходе из испарителя и на входе в него, сообщенных с подводящим и отводящим рабочее тело контурами соответственно, установлены дроссели, причем дроссель подводящего контура имеет больший диаметр, чем дроссель отводящего контура. 1 з.п.ф-лы. 3 ил.

ТУРБОУСТАНОВКА

Изобретение относится к области теплоэнергетики и может быть использовано в паротурбинных установках с двухпоточным цилиндром низкого давления (ЦНД). Турбоустановка содержит двухпоточный двухкорпусный цилиндр низкого давления с двумя выходными патрубками, камерами отбора пара из его внутреннего и внешнего корпусов соответственно во второй по ходу конденсата подогреватель низкого давления и в первый по ходу конденсата подогреватель низкого давления, конденсатор с двумя переходными патрубками, каждый из которых соединен с соответствующим выходным патрубком цилиндра низкого давления. Камера отбора пара в первый подогреватель низкого давления размещена между внешним и наружным корпусами и выполнена общей для обеих проточных частей цилиндра низкого давления. Камеры выполнены с коаксиальными патрубками отбора пара, размещенными между выходными патрубками цилиндра низкого давления. При этом патрубок отбора пара на второй подогреватель проходит внутри патрубка отбора пара на первый подогреватель ...

БЛОК ЦИЛИНДРА НИЗКОГО ДАВЛЕНИЯ С КОНДЕНСАТОРОМ

Использование: в паротурбинных установках и в блоке цилиндра низкого давления (ЦНД) с конденсатором. Сущность изобретения: корпус ЦНД выполнен с подвижной крышкой, соединенной с этим корпусом через другой компенсатор и с конденсатором через распорные стержни, передающие на этот конденсатор вертикальную составляющую нагрузки от избыточного атмосферного давления, действующего на ЦНД. Такое выполнение позволяет уменьшить деформационные нагрузки на корпус ЦНД при относительно простом исполнении. 1 з.п. ф-лы, 1 ил.

ПАРОТУРБИННАЯ УСТАНОВКА

Изобретение относится к энергомашиностроению и предназначено для использования в качестве стационарной или транспортной силовой установки. Пар, образующийся в котле, поступает не только в паровую турбину, но и в сквозную резонансную трубу, которая благодаря теплу, выделяющемуся в результате имеющих место в ней автоматических колебаний газового столба, используется в качестве дополнительного нагревательного элемента котла. В качестве дополнительного или же основного нагревательного элемента котла может также использоваться камера сгорания прерывистого действия, конструкция которой в отличие от камеры сгорания непрерывного действия, включает в себя сквозную резонансную трубу и вследствие этого значительно эффективнее способствует парообразованию. С целью дальнейшего увеличения эффективности паротурбинной установки на выходе из сквозной резонансной трубы и/или сквозной резонансной трубы камеры сгорания прерывистого действия может быть установлено по турбоприводу того или иного агрегата силовой ...

ДВИГАТЕЛЬ ВНУТРЕННЕГО СГОРАНИЯ

Изобретение относится к области двигателестроения, конкретно к поршневым дизельным двигателям. Устройство содержит поршневой дизельный двигатель с жидкостным охлаждением, свободную газовую турбину, установленную на общем валу с воздушным компрессором или с другим потребителем механической энергии, и соединенную с поршневым двигателем газовой связью, изохорную теплонасосную центрифугу с полым внутрилопаточным замкнутым ротором, заполненным инертными газами, с охватывающим его кольцевым парогенератором, паровую турбину и высокоскоростной обратимый стартовый электропривод с выключающейся электромагнитной муфтой. Технико-экономический эффект состоит в значительном повышении эффективной мощности и снижении расхода топлива.

СПОСОБ ПОВЫШЕНИЯ ЭКОНОМИЧНОСТИ ТУРБОКОМПРЕССОРНЫХ ДВИГАТЕЛЕЙ, УСТРОЙСТВО ТУРБОКОМПРЕССОРНОГО ТИПА

Изобретение относится к области теплового двигателестроения, теплоэнергетики и холодильной техники. Способ состоит в том, что сжатый компрессором воздух перед поступлением в камеру сгорания нагревают с помощью центробежного теплового насоса с полым ротором, заполненным смесью тяжелых инертных газов и гелия. Устройство содержит компрессор, турбину, общий вал, конус обтекателя и центробежный тепловой насос. Ротор теплового насоса выполнен в барабане компрессора, а конус обтекателя связан с диском турбины и снабжен спиральным радиальным и осевым каналами испарительной системы теплопередачи, соединенными с артериальной системой вала и осевой полостью теплового насоса.

Теплосиловая установка

Паровая установка

Способ охлаждения комбинированных турбин

Wärmekraftmaschine

Wärmekraftmaschine mit drei über jeweils zwei Arbeitsflüssigkeitsverbindungsleitungen (91a, 91b; 92a, 92b; 93a, 93b) ringförmig miteinander verbundenen Arbeitsbehältereinheiten (10, 20, 30), wobei jede Arbeitsbehältereinheit (10, 20, 30) einen Hochruckbehälter (12, 22, 32), einen Niederdruckbehälter (11, 21, 31) und eine mit dem Niederdruckbehälter (11, 21, 31) verbundene oder in diesem angeordnete Turbine aufweist, und wobei der Niederdruckbehälter (11, 21, 31) und der Hochdruckbehälter (12, 22, 32) einer Arbeitsbehältereinheit (10, 20, 30) über eine Dampfaustauschleitung (15, 25, 35) und über eine Arbeitsflüssigkeitsaustauschleitung (16, 26, 36) miteinander verbindbar sind, wenigstens einem Dampferzeuger (40), wobei jeder Hochdruckbehälter (12, 22, 32) mit wenigstens einem Dampferzeuger (40) verbindbar ist, und wenigstens einem Kondensator (42, 46), wobei jeder Niederdruckbehälter (11, 21, 31) über wenigstens eine Dampfleitung (61, 71; 62, 72; 63, 73) mit wenigstens einem Kondensator ...

Verbindungssystem für einen Kondensator und eine Dampfturbine und Verfahren zur Montage desselben

Es ist ein Verbindungssystem zur Kopplung einer Dampfturbine mit einem Kondensator geschaffen. Das Verbindungssystem enthält einen hundeknochenförmigen Verbinder, eine erste Klemme und eine zweite Klemme. Der hundeknochenförmige Verbinder enthält ein erstes Ende, ein zweites Ende, das dem ersten Ende in Bezug auf die dritte Richtung gegenüberliegt, und einen sich dazwischen erstreckenden Körper. Die erste Klemme enthält einen ersten Abschnitt, einen mit dem ersten Abschnitt gekoppelten zweiten Abschnitt und einen dazwischen definierten ersten Rückhaltehohlraum. Der erste Rückhaltehohlraum ist eingerichtet, um mit einer/einem von der Dampfturbine und dem Kondensator derart gekoppelt zu sein, dass der erste Abschnitt in Bezug auf den zweiten Abschnitt entlang der dritten Richtung bewegbar ist. Die zweite Klemme ist eingerichtet, um mit der/dem anderen von der Dampfturbine und dem Kondensator gekoppelt zu sein, und enthält einen dritten Abschnitt, einen vierten Abschnitt, der mit dem dritten ...

Hochtemperatur-Dampfturbinen-Kraftwerk

A mounting block for a turbo-alternator

... 1,113,483. Surface condensers. SOCIETE EUROPEENE D'EQUIPEMENT "EUREQUIP". 28 May, 1965 [28 May, 1964], No. 22895/65. Heading F4S. A turbo-alternator is mounted on a supporting block which incorporates a condenser for low pressure steam from the turbine, the block comprising a metal or plastics lined chamber formed from a series of pre-stressed or poststressed or reinforced concrete parallel frames 17 interconnected by cross members 15, the chamber having an open top and having the sides closed by partitions 18 and the ends closed by tube plates 13 between which extend straight or undulating condensing tubes 23, 24, additionally supported by intermediate plates 36, 37. The top of the chamber is sealed by means of a fluid tight joint 27 to the exhaust of the low pressure stage 25 of the turbine. The cooling water is supplied to and withdrawn from the condenser through integral concrete pipes 19, 22 opening into water boxes 12 having doors 31, the water passing through the tubes either in ...

Improvements in and relating to turbo-generators

... 415,986. Cooling dynamos. BRITISH THOMSON - HOUSTON CO., Ltd., Crown House, Aldwych, London. April 27, 1934, No. 12768. Convention date, April 28, 1933. [Class 35.] A steam turbine 12 and a generator 10 are vertically arranged and connected by a coupling 9 which is released upon the turbine being lifted. A condenser 15 surrounds, or partly surrounds the generator, and forms part of the support for the turbine casing. Cooling water flows between headers 17, 18 and cooled fluid from the turbine is drained away through an outlet 22. Centrifugal blowers 23, 24, supply cooling air for the generator jacket 25. An additional water jacket separates jacket 25 from the condenser.

Improvements in or relating to Steam Turbines.

... 105,933. Baumann, K. Feb. 4, 1916. Axial-flow type; casings; exhaust, disposing of; mounting and supporting.-R e l a t e s mainly to improved constructions of turbine exhaust casings for axial-flow turbines, said casings conducting the exhaust steam from the last row or rows of moving blades to the exhaust outlet or condenser, and the invention is particularly applicable to multiple exhaust turbines of the kind described in Specification 14053/15. In an ordinary axial-flow turbine, Figs. 1 and 2, the whole of the exhaust steam leaving the moving blades 8, according to the invention, is deflected outwards into a substantially radial direction by the casing wall 10 and then conducted by guide walls 11 in a number of segmental portions outwardly away from the turbine axis in a direction substantially transverse thereto. The exhaust outlet 6 is long and narrow, thus distributing the steam over the whole length of the condenser 7, which may be supported directly from the outlet 6, no expansion ...

Improvements in Radial Flow Steam Turbines.

... 110,786. Baumann, K. Oct. 28, 1916, Addition to 105,933. Radial-flow (bladed) type; exhaust, disposing of; mounting and supporting. -The exhaust casing described in the parent Specification is modified for use with radial-flow turbines, for example with the Ljungstr÷m type of turbine, by omitting the guides for deflecting the steam leaving the turbine outwardly into a radial direction of flow. The exhaust casing 7 has a number of internal guide walls 8 conducting segmental portions of steam leaving the blade ring 3 to the outlet 11, and is supported together with the condenser 14 on feet 12, 13.

Improvements in and relating to methods of and means for supporting turbines, turbine driven sets and the like

... 159,354. British Thomson - Houston Co., Ltd., (General Electric Co.). Dec. 8, 1919. Mounting and supporting.-A turbine or tur. bine-driven set is supported by a rigid mounting on a condenser and is provided with one or more additional supports between the turbine and condenser, these supports being rigid in a transverse direction, but may yield in an axial direction to allow for expansion due to heating. A turbine or turbine-driven set 5 is mounted rigidly on a condenser 8 by bolting its exhaust conduit 7 to the inlet conduit 9 of the condenser. Plates 15 also support the turbine on the condenser, and they are rigid transversely, but may yield axially.

Improvements in Steam Turbine Plants.

... 109,251. Soc. Anon. des Ateliers de Constructions Mecaniques Escher, Wyss, et Cie. Aug. 25, 1916, [Convention date]. Surface condensers.-The annular casing 1 of a surface condenser, receiving exhaust steam direct from the last runner wheel of a turbine 16. has covers 2, 3 for the water chambers and inlet and outlet pipes 4, 5 for the water, and is divided in a horizontal plane into upper and lower halves connected by pipes 6, 7.

Improvements in steam turbine-generator condensing plants

... 758,262. Power generating systems; turbines. STONE & WEBSTER ENGINEERING CORPORATION. Jan. 5,1954 [Jan. 6, 1953], No. 315/54. Classes 110(3) and 122(3) A power plant comprises an electric generator 2 axially aligned with and driven by a steam turbine 1 exhausting to a two-pass surface condenser arranged between the turbo-generator floor 3e and the condenser floor 3d of the, preferably concrete, supporting structure 3 and comprising two separate sections 7, 8 spaced apart side by side transversely to the turbo-generator axis 2a, a part of the structure such as buttresses 5 extending through the space between the sections 7, 8 to act as a support for the turbo-generator. A cross beam 6 extends between the buttresses 5 and provides support for the bearing 61 between the turbine and the generator. The condenser section 7 is aranged directly below the turbine exhaust unit 10 and the other section 8 below the generator and the sections are carried on supports 12, those suporting the ...

Improvements relating to elastic fluid turbines and condensing apparatus therefor

... 294,252. Metropolitan-Vickers Electrical Co., Ltd., (Assignees of Hodgkinson, F.). July 21, 1927, [Convention date]. Axial-flow type; casings.-A housing structure constituting a combined turbine casing and condenser shell is formed with a removable upper part consisting of a turbine casing portion and a condenser shell portion. The high pressure blading is enclosed by casing members 13, 14, and the low pressure blading by members 16, 17, which also provide the exhaust chamber and form portions of the shells of the condensers. In the arrangement shown, two nests of condenser tubes 23 are provided in connected shells 18. The shells are preferably built in sections as shown, with a removable cap 33, but the upper part may be formed in one piece. Vibration of the upper water boxes 29 is prevented by screws 34 and struts 36, Fig. 5, or by thin flexible diaphragms 46, Fig. 4, secured to the upper tube plate 43.

Improvements in or relating to steam turbine installations

... 1,116,261. Steam turbines. ASSOCIATED ELECTRICAL INDUSTRIES Ltd. March 28, 1966 [April 2, 1965], No. 14192/65. Heading F1T. A steam turbine installation comprises an L. P. unit 1 containing three double-flow L.P. turbine cylinders flanked by banks of condenser tubes, and a sub-frame 3 supporting an H . P. turbine cylinder 7, a first I. P. turbine cylinder 9 and a second I. P. turbine cylinder 11. Inlet and outlet pipes 21, 31 for the H. P. cylinder and inlet pipes 41 for the first I. P. cylinder are connected to the cylinders at bolted flanges 23A, 31A and 43A or, preferably, welded joints, these connections being located beyond the sides of the sub-frame 3 so that the sub-frame complete with bearing pedestals 13, 15, 17, 19 and at least the second I. P. cylinder 11 can be lowered into position after the pipes and their associated valves 23, 43 have been erected.

Improvements in and relating to elastic fluid turbines

... 238,222. British Thomson-Houston Co., Ltd., (Assigrees of Warren, (T. B., and Wirt, H. L.). Aug. 11, 1924, [Convention date]. Addition to 238,221. Exhaust, facilitating. - In a turbine as described in the parent Specification having the condenser 12 located to one side of the turbine shaft 6, one of the exhaust passages 14 is formed as therein claimed, and the remainder 15, 16 extend first in the general direction of flow of the elastic fluid and then turn abruptly towards the condenser, guide blades 19 being provided at the turn. The length of each abruptly turning passage is approximately equal to twice the diameter of the last stage wheel. The radial height of the admission end of the annular expanding passage 13 is equal to the length of the buckets 5, and the length of the passage 13 is at least twice the length of the buckets 5. The major part of the conversion of velocity into pressure takes place before the direction of flow is changed, and the construction affords easy access to ...

OPTIMIZED INTEGRATED SYSTEM FOR SOLAR-BIOMASS HYBRID ELECTRICITY GENERATION

Solar energy and external source steam complementary power generation apparatus

SOLAR ENERGY AND EXTERNAL SOURCE STEAM COMPLEMENTARY POWER GENERATION APPARATUS

SOLAR ENERGY GENERATION METHOD AND SYSTEM USING BIOMASS BOILER AS AUXILIARY HEAT SOURCE

Solar energy and external source steam complementary power generation apparatus

OPTIMIZED INTEGRATED SYSTEM FOR SOLAR-BIOMASS HYBRID ELECTRICITY GENERATION

Solar energy generation method and system using biomass boiler as auxiliary heat source

Solar energy generation method and system using biomass boiler as auxiliary heat source

Solar energy generation method and system using biomass boiler as auxiliary heat source

OPTIMIZED INTEGRATED SYSTEM FOR SOLAR-BIOMASS HYBRID ELECTRICITY GENERATION

Solar energy and external source steam complementary power generation apparatus

SPRINGILY SUPPORTED RECUPERATOR FOR A MICRO TURBINE SYSTEM

STEAM PLANT

CONDENSER FROM CONCRETE FOR A TURBINE WITH AXIAL WITHDRAWAL AND TURBINE WITH SUCH A CONDENSER

Mechanism for sealing one a low-pressure steam turbine of evaporate-laterally subordinate area

Low pressure turbine with two independent condensing systems

A low-pressure turbine and a steam power plant with a low-pressure turbine (1) is suggested that is connected to an additional condensing system (25), thus allowing to maintain the electric output at a high level, even if the main condensing system (17) has a reduced capacity due to cooling water restrictions.

Solar energy and external source steam complementary power generation apparatus

A solar energy and external source steam complementary power generation apparatus comprising a solar steam generation device, an external source steam regulator (15), a turboset (2) and a generator (1). A steam output end of the solar steam generation device is connected to a high-pressure steam inlet (3) of the turboset (2) through a first regulating valve (15); a steam output end of the external source steam regulator (15) is connected to the high-pressure steam inlet (3) of the turboset (2) through a second regulating valve (20) and a second switching valve (19). A low-pressure steam outlet (4) of the turboset (2) is connected to a circulating water input end of the solar steam generation device through a condenser (5), a deaerator (6), a water feed pump (7) and a first switching valve (16) in turn. An output end of the water feed pump (7) is connected to an external source steam water return bypass (11) through a fourth switching valve (23).

SUPPORTING DEVICE

The present invention relates to a supporting device for a condensation steam turbine. The turbine parts which are exposed to vacuum tension are attached to a foundation carrier. The foundation carrier is also integrated into a spring supported foundation. The foundation carrier may be connected to a substructure through a separate support. Alternately, a supporting structure may be used to support the foundation carrier and the spring supported foundation. A condenser itself may be constructed as a support.

TURBINE-CONDENSER SUPPORT SYSTEM

TURBINE EXHAUST ARRANGEMENT FOR IMPROVED EFFICIENCY

Steam exhaust outlets of a low pressure steam turbine are fitted with a divider plate to separate exhaust steam into isolated flow paths in fluid communication with a condenser. Separation of the flow paths is maintained through the condenser so that heat rate is improved by lower average back pressure and higher temperature condensate exiting the condenser. In a double flow turbine, a further divider plate separates steam from one exhaust outlet from that of the other exhaust outlet thereby creating four steam flow paths to the condenser.

TURBINE EXHAUST ARRANGEMENT FOR IMPROVED EFFICIENCY

... 56,307 Steam exhaust outlets of a low pressure steam turbine are fitted with a divider plate to separate exhaust steam into isolated flow paths in fluid communication with a condenser. Separation of the flow paths is maintained through the condenser so that heat rate is improved by lower average back pressure and higher temperature condensate exiting the condenser. In a double flow turbine, a further divider plate separates steam from one exhaust outlet from that of the other exhaust outlet thereby creating four steam flow paths to the condenser.

Horizontalachsige Dampfturbine mit achsialer Dampfeinströmung in den unmittelbar angebauten Oberflächenkondensator.

Turbogruppe, welche von zwei liegenden Kondensatoren getragen wird.

Aus Dampfturbine, Kondensator und angetriebener Maschine bestehende Turbogruppe.

Doppelendige Kondensations-Dampfturbine mit einander entgegengesetzten Dampfströmungen.

Abdampfverbindung zwischen Dampfturbine und mittelbar durch Fundament abgestütztem Kondensator.

Dampfturbinenanlage mit drei Austrittsstutzen.

Entlastete Dehnungsausgleichsvorrichtung.

Dampfturbinenanlage mit zwei gleichachsig angeordneten, doppelflutigen Niederdruckturbinen.

Turboaggregat für Dampf.

Dampfturbinenanlage

Fondement pour groupe turbo-alternateur

DAMPFTURBINENANLAGE.

Dampfturbinenanlage

Begrenzungswand für Abdampfräume von Dampfturbinen

Turbosatz

Dampfturbinenanlage

Dispositif moteur rotatif

Oberflächenkondensator

Abdampfverbindung zwischen Dampfturbine und Kondensator

Kondensationseinrichtung an einer Dampfturbine

Dampfturbinenanlage in mehrgehäusiger Bauart

FLEXIBLE CONNECTION OF A CONDENSER WITH A TURBINE.

Integral Steam Power Plant.

Die hier beschriebene Erfindung betrifft eine integrale Dampfkraftanlage zur Umwandlung von thermischer in mechanische Energie. Sie besteht aus einem Stator (2), der in sich im Wesentlichen eine Wärmezufuhrkammer (3), eine Verdampfungskammer (4) sowie eine Kondensationskammer (10) umfasst. Der Stator umgibt einen Rotor (9), wesentlich bestehend aus einer Rotorwelle (12), auf welcher ein Turbinenlaufrad (13) und ein Multifunktionslaufrad (25) sowohl zur Zu- und Abfuhr des Kühlmittels (21) wie auch zum Antrieb der Fördereinheit (6) für das Arbeitsmedium (5) angeordnet sind. Die hier beschriebene Erfindung zeichnet sich dadurch aus, dass sie allein mittels Zufuhr von thermischer Energie durch die Wärmezufuhrkammer selbstanlaufend ist und während des Betriebs die Kühlung des Kondensators sowie den Antrieb der Fördereinheit für das Arbeitsmedium ohne Inanspruchnahme weiterer externer Energiequellen eigenständig leistet.

Steam power plant i.e. steam turbine system, for conversion of thermal energy into mechanical energy, has rotor comprising rotor shaft, turbine wheel and multi-function running wheel and completely surrounding stator

The plant (1) has a rotor (9) comprises a rotor shaft (12), a turbine wheel (13) and a multi-function running wheel (25) and rotatable around a rotational axis, where the plant comprises a heat input chamber (3), a connecting device (26), a guide device (7), a flash chamber (8), a condensation chamber (10) and a coolant supply chamber (11). A vaporization chamber (4) partially vaporizes a working medium (5). The rotor completely surrounds a stator (2). The heat input chamber surrounds the vaporization chamber. A wall (15) separates the input chamber from the vaporization chamber.

Verfahren und Anlage zur Erzeugung von elektrischer Energie und Wasserstoff aus RESH.

Nach diesem Verfahren werden Wasserstoff H 2 und Sauerstoff O 2 durch Nutzung der Abwärme aus einer Pyrolyseanlage, in welcher kohlenstoffhaltige Reststoffe (RESH) thermisch aufgearbeitet werden, hergestellt. Die erzeugte Wärme wird zum Heizen eines Brenners eines Dampfkessels (2) genutzt. Der Druckdampf wird über eine Turbine (4) entspannt, die einen Generator (6) antreibt. Die elektrische Energie wird zum Betrieb und Aufrechterhaltung der Wasser-Elektrolyse eingesetzt und dafür auf die geeignete Spannung herunter transformiert und dann gleichgerichtet, wonach die Spannung an einen Alkalielektrolyse-Stapel angelegt wird. Die entstehenden Gase Wasserstoff H 2 und Sauerstoff O 2 werden aufgefangen und der Wasserstoff wird vorzugsweise in Metallhydrid-Speichern eingelagert, für eine bedarfsweise Nutzung. Ein Teil des erzeugten Wasserstoffs H 2 wird zur Aufrechterhaltung der Pyrolyse des RESH eingesetzt und kann das sonst dafür nötige Erdgas ersetzen.

METHOD OF PREPARING HEAT CARRIER FOR A DOUBLE-TUBE HEATING SYSTEM AND A HIGH-CAPACITY BOILER-HOUSE THEREFOR

Cogeneration turbine for heating and supplying heat

Distributed energy supply system for electric heating heat storage heat energy power generation

Steam power generation device

Super-gravity and thermal power circulation device and method

Low-medium temperature heat energy recovery power generation device

Electric hydrogen CO-production system and method

Thermodynamic system capable of being switched between operation mode of driving two steam turbines through one boiler and operation mode of driving one steam turbine through one boiler

Compared with prior art,

Concentrative heat supply system for recovering condensation heat of indirect air-cooled unit of power plant

Coal mine gas comprehensive utilization system

Reheat cycle system

Joint fragmentary heating system that exerts oneself of three steam extraction 200MW unit middle and low voltage jars

Nuclear power station heating power combined cycle system

Gas - steam combined cycle generation waste heat utilization system

The utility model relates to a gas - steam combined cycle generation waste heat utilization system, its structural feature lies in: set up surperficial formula heat exchanger at the air input of gas turbine power generation unit, be equipped with hot water heat exchanger at exhaust -heat boiler's afterbody, exhaust -heat boiler's gas input end is connected to the flue gas output of gas turbine power generation unit, and turbo generator set's steam input is connected to exhaust -heat boiler's steam output, exhaust -heat boiler's feedwater input is connected to turbo generator set's comdenstion water output, hot water heat exchanger's high temperature hot water output end connects the high temperature hot water input of lithium bromide absorbed refrigeration machine, and the low temperature hot water output end of lithium bromide absorbed refrigeration machine connects hot water heat exchanger's low temperature hot water input, forms gas - steam combined cycle generation waste heat utilization ...

Utilize cement kiln low temperature waste heat to heat turbo generator set condensate system

Steam-organic Rankine cascade power cycle generating system and method

The invention discloses a steam-organic Rankine cascade power cycle generating system and a method for realizing cascade use of heat energy. In the method, a steam Rankine cycle is effectively cascaded with an organic Rankine cycle, the heat of exhaust gas from a previous grade steam Rankine cycle steam turbine is not directly removed by using cooling water but is used for heating a liquid working medium with a low boiling point in a next organic Rankine bottom cycle to produce working medium steam with a low boiling point and high pressure so as to perform expansion-driven power generation by using an organic turbine (expander). The system belongs to the technical field of industrial energy conservation. The process of the method comprises the following steps of: (1) performing steam Rankine top cycle power generation; (2) directly taking the exhaust gas of the steam Rankine top cycle as a driving heat source for the organic Rankine bottom cycle; and (3) transferring heat to the working ...

Waste heat recovery device for steam stripping device and steam stripping device with same

Living beings incineration boiler and parallelly connected power generation system of coal fired boiler

System is utilized to living beings coupling coal -fired unit's high efficiency

Steam accumulator for waste heat recovery in iron and steel enterprises

Operation-controllable double-unit backheating system

Thermal storage peak regulation system and method for stratosphere based on high-voltage heating loop

Heat supply method of cogeneration unit and heat supply system

Low temperature exhaust heat storage system with combined heat and power generation

Coal-fired electricity generation-CO2 capture-heat supply integrating system and method

A thermal power unit and the air turbine coupled power generation system

HYBRID SOLAR POWER PLANT

A solar power plant includes a first solar reflective system configured to heat a first heat transfer fluid to a temperature within a first temperature range and at least a second solar reflective system coupled to the first solar reflective system, the second solar reflective system having a second heat transfer fluid configured to be heated to a temperature within the first temperature range by the first heat transfer fluid, the second solar reflective system configured to heat the second heat transfer fluid to a temperature within a second temperature range. The solar power plant may also include a power generation system coupled to the first solar reflective system and the second solar reflective system and configured to generate electricity by receiving heat from the first heat transfer fluid and the second heat transfer fluid. 1. A solar power plant comprising:a first solar reflective system configured to heat a first heat transfer fluid to a temperature within a first temperature range;at least a second solar reflective system coupled to the first solar reflective system, the second solar reflective system having a second heat transfer fluid configured to be heated to a temperature within the first temperature range by the first heat transfer fluid, the second solar reflective system configured to heat the second heat transfer fluid to a temperature within a second temperature range; anda power generation system coupled to the first solar reflective system and the second solar reflective system and configured to generate electricity by receiving heat from the second first heat transfer fluid and the second heat transfer fluid.2. The solar power plant of claim 1 , wherein the power generation system comprises:a steam generator configured to generate a first steam with heat from the first heat transfer fluid;a superheater configured to generate a second steam from the first steam with heat from the second heat transfer fluid; andwherein the second steam has ...

DIRECT CONTACT CONDENSER FOR STEAM TURBINE

A steam turbine direct contact condenser prevents cooling water sprayed from spray nozzles from reaching turbine blades of an axial-flow turbine, while introducing turbine exhaust gases exhausted by a steam turbine in the horizontal direction to cool such gases. The condenser includes an exhaust gas inlet part that introduces the turbine exhaust gases containing steam of the steam turbine and non-condensable gases in the horizontal direction, a steam cooling chamber that sprays cooling water to the introduced turbine exhaust gases to cool them, and a water storage disposed at the bottom of the steam cooling chamber that stores condensed water cooled from the steam and the cooling water. The steam cooling chamber includes a first cooling water spraying mechanism and a second cooling water spraying mechanism. 1. A direct contact condenser for a steam turbine , the direct contact condenser comprising:an exhaust gas inlet part configured to introduce a turbine exhaust gas containing steam and a non-condensable gas of the steam turbine in a horizontal direction;a steam cooling chamber configured to spray cooling water at the turbine exhaust gas introduced through the exhaust gas inlet part to cool the turbine exhaust gas; anda water storage which is disposed at a bottom of the steam cooling chamber and which stores condensed water generated by cooling the steam and the cooling water, a first cooling water spraying mechanism which is disposed adjacent the exhaust gas inlet part and which sprays the cooling water within a range restricted from a side of the condenser to a downstream direction of the turbine exhaust gas; and', 'a second cooling water spraying mechanism which is disposed at a downstream side of the first cooling water spraying mechanism and which sprays the cooling water to the turbine exhaust gas in all directions., 'the steam cooling chamber comprising2. The steam turbine direct contact condenser according to claim 1 , wherein the first cooling water ...

METHOD FOR CONTROLLING A SHORT-TERM INCREASE IN POWER OF A STEAM TURBINE

A method is provided for controlling a short-term increase in power in a steam turbine including a fossil-fired steam generator having a flow path through which a flow medium flows. The method involves tapping off the flow medium from the flow path in a pressure stage and injecting it into the flow path on the flow-medium side upstream of a super heater heating surface of the respective pressure stage. A first characteristic value is used as a controlled variable for the amount of injected flow medium. The first characteristic value is characteristic of the deviation between the outlet temperature of a final super heater heating surface of the respective pressure stage on the flow medium side and a predetermined nominal temperature value. The nominal temperature value is reduced and, for the duration of the reduction in the nominal temperature value, the characteristic value is temporarily increased over-proportionately to the deviation. 18-. (canceled)9. A method for controlling a short-term increase in power in a steam turbine comprising a fossil-fired steam generator arranged upstream having a plurality of economizer , evaporator and super heater heating surfaces , which form a flow path and through which a flow medium flows , the method comprising:tapping off the flow medium from the flow path in a pressure stage and injecting it into the flow path on the flow-medium side upstream of a super heater heating surface of the respective pressure stage, wherein a first characteristic value is used as a controlled variable for the amount of injected flow medium, the first characteristic value being characteristic of the deviation between the outlet temperature of the final super heater heating surface of the respective pressure stage on the flow medium side and a predetermined nominal temperature value,wherein, in order to achieve a short-term increase in power of the steam turbine, the nominal temperature value is reduced and, for the duration of the reduction in the ...

FEEDWATER HEATING HYBRID POWER GENERATION

The technology combines a secondarily-fueled boiler with a primary-fueled Rankine steam cycle combustion system in a hybrid process. Outputs from a secondarily-fueled combustion system are fed into the feedwater heater(s), deaerators, feedwater heating lines, and/or reheat lines of a primary-fueled Rankine system. The integrated steam flow eliminates or reduces one or more extractions from the steam turbine generator, thereby allowing it to generate more electrical power using the same Rankine system input energy or generate equivalent electrical power using energy inputs from multiple fuel sources. The technology can be utilized in any type and/or configuration of secondary fuel or secondarily-fueled combustion technology and/or can utilize any type of primary-fueled steam source. 1. A method for generating electrical power comprising:processing, via a first boiler system, a first energy source to produce a first steam flow;processing the first steam flow through a steam turbine to produce electricity;taking one or more extractions from one or more low pressure (LP) sections and/or one or more intermediate pressure (IP) sections of the steam turbine to heat a feedwater flow in one or more feedwater heaters/deaerators;processing, via at least one additional boiler system, at least one additional fuel source to produce at least one additional steam flow, wherein the at least one additional boiler system continuously produces the at least one additional steam flow during operation of the first boiler system;routing at least part of the at least one additional steam flow to at least one of the one or more feedwater heaters/deaerators to further heat the feedwater flow, wherein the feedwater flow in the one or more feedwater heaters/deaerators is heated only by the at least one additional steam flow and the one or more extractions from the one or more LP sections and/or the one or more IP sections; androuting at least part of the feedwater flow from the one or more ...

Heat Engine Shuttle Pump System and Method

A heat engine including a novel method for transferring working fluid from the low pressure side of the cycle back to the high pressure side. The invention includes one or more transfer tanks connecting the condenser to the boiler. Each transfer tank is connected to the condenser by a fill line and connected to the boiler by a dump line. Gravity and/or small transfer pumps are used to transfer the working fluid horn the low pressure side, through the transfer tank or tanks, and then to the high pressure side. 1. A method of transferring working fluid within a heat engine from a condenser to an evaporator , comprising:a. providing a condenser having an internal condenser pressure, said condenser containing working fluid in a liquid form;b. providing an evaporator having an internal evaporator pressure;c. providing a first transfer tank;d. providing a first fill line leading from said evaporator to said first transfer tank;e. providing a first dump line leading from said first transfer tank to said evaporator;f. providing a first flow control valve in said first fill line;g. providing a second flow control valve in said first dump line;h. providing a first vent line leading from said first transfer tank to said condenser;i. providing a second vent line leading from said first transfer tank to said evaporator;j. providing a first vent control valve in said first vent line;k. providing a second vent control valve in said second vent line;l. opening said first flow control valve, closing said second flow control valve, opening said first vent control valve, and closing said second vent control valve;m. whereby said liquid working fluid in said condenser flows through said first fill line into said first transfer tank and any gaseous working fluid contained within said first transfer tank is vented through said first vent line back to said condenser;n. closing said first flow control valve, opening said second flow control valve, closing said first vent control valve, and ...

Thermal Energy Conversion Plant

A thermal energy conversion plant, wherein a pressurized liquefied working fluid gasifies in an evaporator unit located at the lower level of a closed-loop thermodynamic circuit, ascends through a widening ascending conduit to a condenser unit located at the upper level of said thermodynamic circuit, condenses and falls because gravity powering a power extraction apparatus, before entering back into the evaporator, and restarting the cycle. A much lighter pressuring gas could be optionally included in the widening ascending conduit. 1. A thermal energy conversion plant , comprising a closed-loop thermodynamic circuit and a closed-loop thermal circuit ,the thermodynamic circuit comprising:a pressurized working fluid in the thermodynamic circuit;at least one evaporator unit located at the lowest level of the closed-loop thermodynamic circuit;at least one widening ascending conduit in fluid communication with the evaporator and connected to the evaporator unit, the widening ascending conduit having an initial diameter smaller than the final diameter;at least one condenser unit in fluid communication with the widening ascending conduit and connected to the upper level of the widening ascending conduit;at least one descending conduit that is in fluid communication with the condenser and evaporator units, and connects the condenser unit with the evaporator unit, the descending conduit closing the closed-loop thermodynamic circuit; andat least one power extraction apparatus in fluid communication with the descending conduit and connected to the descending conduit;wherein:the thermodynamic circuit is configured such that the working fluid gasifies in the evaporator unit, then the gasified working fluid egresses from the evaporator unit entering into the widening ascending conduit, ascending up to the condenser unit; in the condenser unit, the gasified working fluid liquefies; then the liquefied working fluid egresses from the condenser unit, falling because of gravity, ...

SYSTEM AND PROCESS FOR ELECTRICITY GENERATION USING STEAM PRODUCTION BY HYDROGEN COMBUSTION

The invention relates to a system and process for electricity generation using steam production by hydrogen combustion, and more particularly to a Rankine Cycle system and process for the generation of electricity using a primary pure hydrogen fuel source for the generation of steam in the boiler system. The Rankine Cycle system and process may also use one or more secondary fuel sources in combination with the primary hydrogen fuel source to supplement the primary pure hydrogen fuel if necessary. Additionally, the inventive system and process can use a flame temperature reducing fluid for lowering bulk flame temperature of a burner in the boiler system to increase equipment life and decrease equipment failure. The inventive Rankine Cycle system and process reduce emissions of carbon dioxide, nitrogen oxides, and other greenhouse gases into the atmosphere, and reduce bulk flame temperatures to increase equipment life and decrease equipment failure. 1100118112114128126100. A system for electricity generation using hydrogen combustion , said system comprising a Rankine Cycle fluid recirculation loop () , a condenser () , a steam turbine () engaged with a generator () to generate the electricity , and a feed water pump () for circulating water () through the Rankine Cycle fluid recirculation loop () , the system further comprising:{'b': 104', '136', '138, 'a source of an oxidizer (, , );'}{'b': 2', '102, 'a source of primary pure hydrogen (H) fuel (); and'}{'b': '106', 'claim-text': [{'b': 146', '104', '136', '138, 'an oxidizer inlet () downstream from the source of oxidizer (, , ),'}, {'b': 148', '102, 'a primary fuel inlet () downstream from the source of primary pure hydrogen fuel (),'}, {'b': 108', '102', '104', '136', '138', '108', '102', '104', '136', '138', '110, 'at least one burner () configured to combust the primary pure hydrogen fuel () with the oxidizer (, , ) to produce flame and combustion products, and the burner () further configured to combust the ...

THERMAL POWER PLANT WITH HEAT RECOVERY

In an energy conversion method and a thermal power plant for converting heat into mechanical or electric energy using a working medium, a vapor state in the working medium is generated at a first pressure in a steam generator. The vaporized working medium is expanded to a lower second pressure in a steam expanding device. An energy obtained by the expansion process is discharged. The expansion of the steam state is carried out using a saturation line of the working medium. The working medium is thereby separated into a non-condensed portion and a condensed portion in a separating device. The non-condensed portion is then compressed into a compressed non-condensed portion in a compressor. The compressed non-condensed portion is cooled and condensed into a compressed condensed portion. The compressed condensed portion and the initially condensed portion are then heated, and both portions are returned to the steam generator together. 1. Thermal power plant for converting energy by means of a working medium , which has:{'b': '25', 'a steam generator () for vaporizing the working medium at a first pressure,'}a steam expanding device for expanding the working medium present in the vapor state to a lower, second pressure,{'b': '36', 'a condenser (), which cools and liquefies the working medium let out of the steam expanding device, and'}{'b': '37', 'a condensate pump (), characterized in that'}the steam expanding device is designed in such a way that a working medium expanded by the steam expanding device has a condensed portion and a non-condensed portion,{'b': 51', '5, 'a separation device for separation of the condensed portion and the non-condensed portion and a compressor () for compression () of the non-condensed portion of the working medium are provided,'}{'b': '36', 'whereby the non-condensed portion of the expanded working medium condenses at least partially through the condensed portion in the condenser ().'}24444514454. Thermal power plant according to claim 1 ...

ORGANIC RANKINE BINARY CYCLE POWER GENERATION SYSTEM

An organic rankine binary cycle power generation system includes: a superheater heating a working fluid by exchanging heat with discharged heat; a turbine receiving the working fluid from the superheater and generating mechanical energy; a power generator connected to a power shaft of the turbine and generating power; a condenser keeping gas-state and liquid-state working fluids having passed through the turbine; a pump pumping the liquid-state working fluid in the condenser; a buffer tank disposed in a working fluid line between the pump and the superheater and keeping the gas-state and liquid-state working fluids; a compressor connected to the power shaft of the turbine, connected to the condenser and the buffer tank through diverging lines, respectively; and an expansion valve disposed in a bypass line connecting the buffer tank and the condenser and forcibly evaporating the working fluid moved by a pressure difference between the buffer tank and the condenser. 1. An organic rankine binary cycle power generation system comprising:a superheater heating a working fluid by exchanging heat with discharged heat;a turbine receiving the working fluid from the superheater and generating mechanical energy;a power generator connected to a power shaft of the turbine and generating power;a condenser keeping gas-state and liquid-state working fluids having passed through the turbine;a pump pumping the liquid-state working fluid in the condenser;a buffer tank disposed in a working fluid line between the pump and the superheater and keeping the gas-state and liquid-state working fluids;a compressor connected to the power shaft of the turbine, connected to the condenser and the buffer tank through diverging lines, respectively, and taking the working fluid inside from the condenser, compressing and heating the working fluid, and sending the working fluid to the buffer tank by using power from the turbine; andan expansion valve disposed in a bypass line connecting the buffer tank ...

HEAT TRANSFER ELEMENTS FOR ROTARY HEAT EXCHANGERS

A rotary heat exchanger for preheating air using waste heat comprises a plurality of heat transfer elements movable between first and second openings in a housing to exchange heat between heated exhaust gases and a stream of fresh air. At least one heat transfer element comprises a first plate having a plurality of elongate notches formed therein at spaced intervals and oriented at a first angle relative to the flow direction. The plate further comprises a plurality of elongate undulations formed therein at spaced intervals and oriented a second angle relative to the flow direction, wherein the first angle is different than the second angle. A first height of each of said plurality of elongate notches is larger than a second height of each of said plurality of elongate undulations. The heat transfer elements may be stacked in a container for installation in the rotary heat exchanger. 1. A heat transfer element for a rotary heat exchanger having a flow direction , said heat transfer element comprising:a plate having a plurality of elongate notches formed therein at spaced intervals, said elongate notches each being oriented at a first angle relative to the flow direction and having a first height relative to a surface of said plate;said plate further having a plurality of elongate undulations formed therein at spaced intervals, said elongate undulations each being oriented at a second angle relative to the flow direction and having a second height relative to a surface of said plate;wherein said first height of each of said plurality of elongate notches is larger than said second height of each of said plurality of elongate undulations; andwherein said first angle is different than said second angle.2. A heat transfer element as set forth in claim 1 , wherein said first angle is in the range of 5° to 45° relative to the flow direction.3. A heat transfer element as set forth in claim 1 , wherein said first angle is 20° relative to the flow direction.4. A heat transfer ...

HEAT TRANSFER ELEMENTS FOR ROTARY HEAT EXCHANGERS

A rotary heat exchanger for preheating air using waste heat comprises a plurality of heat transfer elements movable between first and second openings in a housing to exchange heat between heated exhaust gases and a stream of fresh air. At least one heat transfer element comprises a first plate having a plurality of elongate notches formed therein at spaced intervals and oriented at a first angle relative to the flow direction. The plate further comprises a plurality of turbulators formed in the spaced intervals between the plurality of elongate notches, the plurality of turbulators being arranged in a two-dimensional pattern. The heat transfer elements may be stacked in a container for installation in the rotary heat exchanger. 120.-. (canceled)21. A heat transfer element for a rotary heat exchanger having a flow direction , the heat transfer element comprising:a plate having a plurality of elongate notches formed therein at spaced intervals, the elongate notches each being oriented at a first angle relative to the flow direction; anda plurality of turbulators formed in the spaced intervals between the plurality of elongate notches, the plurality of turbulators being arranged in a two-dimensional pattern.22. A heat transfer element as set forth in claim 21 , wherein the two-dimensional pattern includes rows and columns of turbulators.23. A heat transfer element as set forth in claim 21 , wherein the plurality of turbulators includes a plurality of hemi-spherical dimples.24. A heat transfer element as set forth in claim 21 , wherein the plurality of turbulators includes a plurality of diamond-shaped protrusions.25. A heat transfer element as set forth in claim 21 , wherein each of the plurality of elongate notches has a first height and each of the plurality of turbulators has a second height claim 21 , and wherein the first height is greater than the second height.26. A heat transfer element as set forth in claim 21 , wherein a spacing between adjacent turbulators ...

Apparatus And Method Of Energy Recovery For Use In A Power Generating System

This invention relates to a method of condensing and energy recovery within a thermal power plant using the Venturi effect and gas stored under hydrostatic pressure and to an energy storage system using the method in a hydrogen and oxygen combusting turbine, where the hydrogen and oxygen gasses are produced by water electrolysis and hydrostatically pressurised and stored. 1. A method of energy recovery for a thermal power plant , said method comprising the following steps:(a) a first working fluid delivering energy to a main power generating turbine then passes through a heat exchanger means in a Venturi condenser whereupon at least some of the remaining energy is extracted, and at least some of the first working fluid condenses to a liquid state;(b) a second working fluid enters one or more Venturi tubes in a Venturi condenser at elevated pressure, the second working fluid cooling and decreasing in pressure as it passes through the Venturi tubes the second working fluid absorbing thermal energy from the first working fluid in a heat exchanger means in the Venturi condenser;(c) the reduced volume of the first working fluid causing a decreased pressure downstream of the main power generating turbine so increasing flow of the first working fluid through the main power generating turbine;(d) the second working fluid after absorbing thermal energy in the heat exchanger means passing through a second power generating turbine where energy is extracted.2. A method according to where the second working fluid which is ducted through the Venturi tube condenser during periods of higher electricity demand to provide condensing and energy recovery claim 1 , has been compressed using off peak or lower demand energy to compress it for storage under hydrostatic pressure for release on demand.3. A method of energy recovery as claimed in in which hydrogen and oxygen gasses are produced by a method of water electrolysis claim 1 , the gasses are stored under hydrostatic pressure claim ...

HYBRID POWER GENERATION SYSTEM AND METHOD USING SUPERCRITICAL CO2 CYCLE

A hybrid power generation system using a supercritical COcycle includes a steam power generation unit including a plurality of turbines driven with steam heated using heat generated by a boiler to produce electric power, and a supercritical COpower generation unit including an S—COheater for heating a supercritical COfluid, a turbine driven by the supercritical COfluid, a precooler for lowering a temperature of the supercritical COfluid passing through the turbine, and a main compressor for pressurizing the supercritical COfluid, so as to produce electric power. The steam power generation unit and the supercritical COpower generation unit share the boiler. The hybrid power generation system may improve both the power generation efficiencies of the steam cycle and the supercritical COcycle by interconnecting the steam cycle and the supercritical COcycle. 1. A hybrid power generation system using a supercritical COcycle , comprising:a steam power generation unit comprising a plurality of turbines driven with steam heated by a boiler to produce electric power; and{'sub': 2', '2', '2', '2', '2', '2, 'a supercritical COpower generation unit comprising an S—COheater for heating a supercritical COfluid, a turbine driven by the supercritical COfluid, a precooler for lowering a temperature of the supercritical COfluid passing through the turbine, and a main compressor for pressurizing the supercritical COfluid, so as to produce electric power,'}{'sub': '2', 'wherein the steam power generation unit and the supercritical COpower generation unit share the boiler.'}2. The hybrid power generation system according to claim 1 , wherein the steam power generation unit further comprises a plurality of feed water heaters for reheating the steam driving the turbines claim 1 , a plurality of outside air injectors for supplying outside air to the boiler claim 1 , a gas air heater (GAH) for recovering waste heat from combustion gas discharged after burning by the boiler claim 1 , and an ...

Supercritical co2 power generating system for preventing cold-end corrosion

A supercritical CO 2 power generating system prevents cold-end corrosion capable of improving reliability against cold-end corrosion by including a recirculation pump. Part of the working fluid heated in the low-temperature-side external heat exchanger using the recirculation pump is mixed with the low-temperature working fluid at the rear end of the pump, to heat the working fluid above the temperature of the dewpoint of the waste heat gas. The heated working fluid is then supplied to the external heat exchanger. By reducing the cold-end corrosion phenomenon of the low-temperature-side external heat exchanger, the life of the external heat exchanger can be increased and the reliability of the external heat exchanger and the supercritical CO 2 power generating system can be improved.

BIOMASS PYROLYSIS APPARATUS, AND POWER GENERATION SYSTEM

Provided is a biomass pyrolysis apparatus comprising: a combustion furnace that produces a heat quantity by causing a stable property fuel to combust; a pyrolysis gasification furnace that produces a torrefied material, and a pyrolysis gas by pyrolyzing woody biomass by a heat quantity produced by the combustion furnace; and a pyrolysis gas introduction passage that introduces the pyrolysis gas from the pyrolysis gasification furnace into a boiler, into which the torrefied material is introduced. 1. A biomass pyrolysis apparatus comprising:a combustion furnace that produces a heat quantity by causing a stable property fuel to combust;a pyrolysis gasification furnace that produces a torrefied material and a pyrolysis gas by pyrolyzing woody biomass by a heat quantity produced by the combustion furnace; anda pyrolysis gas introduction passage that introduces the pyrolysis gas from the pyrolysis gasification furnace into a boiler, into which the torrefied material is introduced.2. The biomass pyrolysis apparatus according to claim 1 , wherein the pyrolysis gasification furnace is an indirect heating type pyrolysis gasification furnace that indirectly heats the woody biomass by a heating gas.3. The biomass pyrolysis apparatus according to further comprising a control device that controls a temperature of the pyrolysis gasification furnace claim 1 , whereinthe control device controls a temperature of the pyrolysis gasification furnace so that the current value of a pulverizer that pulverizes a torrefied material produced by the pyrolysis gasification furnace is generally in a constant range.4. A power generation system comprising: the biomass pyrolysis apparatus according to ;a boiler in which the torrefied material is introduced and by which the torrefied material is combusted;a steam turbine in which steam produced by the boiler is introduced; anda power generator driven by the steam turbine. The present application is a National Phase of International Application No. ...

PASSIVE LOW TEMPERATURE HEAT SOURCES ORGANIC WORKING FLUID POWER GENERATION METHOD

The present invention relates to a passive type low-temperature heat sources organic working fluid power generation method. The organic working fluid absorbs heat and evaporates in the first evaporator and the second in turn evaporator. When the pressure of organic working fluid reaches the set pressure, the self-operated pressure regulator valve at the outlet of the evaporator opens triggered by operating pressure. The organic working fluid vapor flows into the turbine and pushes the turbine to rotate with a high speed, driving the generator to provide output power. The low-temperature low-pressure exhaust gas flows into the condenser and condenses into liquid working fluid. Through the first and second evaporator in turn providing working steam, the turbine can maintain continuous work and provide output power. Compared with the prior technology, the present invention has reliable performance, relying on the evaporation of the working fluid in a closed space to achieve increased pressure. 1. A method of the passive type low-temperature heat sources organic working fluid generation method comprises the steps of:(1) when the organic working fluid within the first evaporator absorbs heat and evaporates, the temperature and the pressure of first evaporator increases until the organic working fluid pressure reaches the set pressure. The first self-operated pressure regulator valve at the outlet of the first evaporator opens triggered by working pressure, the organic working fluid vapor flows into the turbine and pushes the turbine to rotate with a high speed, driving the generator to provide output power. The low-temperature low-pressure exhaust gas flows into the condenser and condenses into liquid working fluid;(2) The condensed organic working fluid flows into the reservoir. As the organic working fluid of the first evaporator consuming, the evaporator pressure drops to the set value of self-operated pressure regulator valve, and the first self-operated pressure ...

Vortex Tube Supplying Superheated Vapor for Turbine Power Generation

The vortex tube when properly used within a Rankine cycle can produce phenomenal results. This invention functionally describes the preferred vortex tube used to produce superheated vapor from a compressed heated liquid without summoning the additional heat required for latent-heat to effect vaporization. The vortex tube provides superheated vapor to a turbine for generating electricity burning 50% less fossil fuel, also releasing 50% less carbon emissions to the environment. The vortex tube extends the efficient Rankine Cycle temperature range well below 150° F. with the proper refrigerant choice. The physical size and function of the hearing equipment is reduced. The invention delivers new thermal efficiencies for both the Rankine Cycle and the Organic Rankine Cycle. 1. A process of making a superheated vapor from a compressed liquid comprising the steps:entering at least one inlet tangentially a compressed liquid stream into the internal diameter and near perpendicular of a cylindrical inlet chamber, said compressed liquid stream transverses at least one inlet, reducing the liquid temperature and pressure,creating a second duel-phase fluid stream having fluid expanding and straight line acceleration; said second duel-phase fluid stream following the inlet chamber internal diameter forcing a duel-phase fluid rotation developing a fluid vortex and vital angular momentum, also straight line forward and angular acceleration, initiating both a fluid temperature and pressure reduction, said second duel-phase fluid stream at least partially converting its pressure energy into the accelerating rotating fluid kinetic energy,forming a condensate precipitating out of said accelerating rotating fluid,emitting condensation heat,forming and migrating condensate inward due to a loss of angular momentum and inward toward a lower pressure developing near the vortex center,sweeping away residual liquid water and condensate by a passing swirling center counterflow vortex in close ...

Method to integrate regenerative rankine cycle into combined cycle applications

A system is disclosed that incorporates a regenerative Rankine cycle integrated with a conventional combined cycle. An added duct firing array, typically located after the combustion turbine exhaust and before the conventionally designed Heat Recovery Steam Generator (HRSG), is used to boost enthalpy of said exhaust. An added heating element downstream of the firing array provides sufficient heating for sensible heating, evaporation and superheating of feedwater that has been previously heated by feedwater heaters as part of a regenerative Rankine cycle. In practice, the condensate stream from the condenser is bifurcated such that a dedicated feedwater flow is directed to feedwater heaters. After further heating in the added heating element, the superheated steam, at the same pressure and temperature as the main steam, is now mixed with the main steam prior to turbine entry. The condensate is directed to the HRSG to be heated in conventional fashion. 1. A method for generating electric power that incorporates the use of a regenerative Rankine cycle with a combined cycle , the method comprising the steps of:Bifurcating the condensate from a condenser into two or more separate condensate feed streams whereby the condensate in at least one condensate feed stream is pressurized to feedwater and sent directly to a heat recovery steam generator and the condensate in at least one condensate feed stream is pressurized to feedwater and sent to at least one separately fired heating element first being preheated by a one or more feedwater heaters utilizing extraction steam from an extraction turbine;generating steam in at least one separately fired heating element and transferring the steam to an extraction steam turbine having one or more extraction ports;converting the steam into electricity through the use of an extraction steam turbine and generator and extracting some of the steam for heating feedwater.2. The method of claim 1 , wherein additional heat enthalpy is ...

CLOSED-CYCLE PLANT

A closed cycle plant for converting thermal power to mechanical or electrical power including: a closed circuit inside which a working fluid circulates according to a predetermined circulation direction, a volumetric expander configured to receive at the inlet the working fluid in a gaseous state. The volumetric expander includes: a jacket having an inlet and an outlet for enabling the introduction and discharge the working fluid; an active element housed in said jacket and suitable for defining, in cooperation with said jacket, a variable volume expansion chamber; a main shaft; a valve active that opens and closes the inlet and outlet, and a generator connected to the main shaft. The valve includes a regulation device configured to vary the duration of the introduction condition, or the maximum through cross-section of the inlet. 118-. (canceled)19. A closed cycle plant for converting thermal power into electric power comprising:a closed circuit, inside which at least one working fluid according to a predetermined circulation direction circulates, (i) at least one jacket having at least one inlet and one outlet respectively suitable for introducing and discharging the working fluid,', '(ii) an active element housed in said jacket and suitable for defining, in cooperation with said jacket, a variable volume expansion chamber,', '(iii) a main shaft associated to the active element and configured to rotatively move around an axis,', '(iv) at least one valve, active on the inlet and outlet of the jacket, and configured to selectively open and close said inlet and said outlet to allow at least one condition of introducing, one condition of expanding and one condition of discharging the working fluid from said expansion chamber,, 'at least one volumetric expander configured to receive at the inlet the working fluid at the gaseous state, said volumetric expander comprisingat least one electric energy generator connected to the main shaft, (i) the duration of the ...

METHOD FOR IMPROVING THERMAL-CYCLE YIELD IN NUCLEAR POWER PLANTS

The present invention relates to a method for increasing the efficiency of electric power generation in pressurized water nuclear power plants, comprising steps of superheating a main steam and reheating the reheated steam by means of an auxiliary circuit, where the streams for the superheating and the reheating work in parallel. 1. Method for increasing the efficiency of electric power generation in pressurized water nuclear power plants , comprising the following steps:a. the saturated or slightly wet steam originating from the steam generator (SG) is superheated before entering a steam turbine (ST) with several bodies;b. the steam reheated with steam from a high pressure (HP) turbine extraction, is again reheated using live-steam from the reactor;c. the steam reheated in the preceding step is again reheated, exchanging heat with a thermal fluid at a higher temperature;d. the reheated steam of step c is expanded in the low (LP) body of the steam turbine;e. the expanded steam of step d is condensed and the condensed water is recirculated to the steam generators after heating with water steam originating from turbine extractionscharacterized in that the superheating in a and the reheating in c are performed by means of an auxiliary thermal fluid circuit with the streams for the superheating and the reheating working in parallel.2. Method according to claim 1 , characterized in that in steps a and c the exchange with the thermal fluid is performed by means of pressurized water and at a higher temperature claim 1 , where the water originates from a second auxiliary circuit which diverts part of the water from the reactor to an exchanger.3. Method according to claim 1 , characterized in that the energy source or sources used for the superheating and the reheating of steps a and c is/are external to the power plant.4. Method according to any of claim 3 , where the energy source or sources is/are a renewable source. The present invention relates to a method for being ...

GEOTHERMAL ENERGY DEVICE

The technical outcome of the proposed geothermal energy device is to increase its efficiency (CE), to simplify and cheapen the construction. 1. A geothermal energy device comprises downward and upward pipes placed in a borehole , unilaterally closed only from the ground surface that are filled with a fluid thermal agent and connected to each other with a heat exchanger in the depth of the borehole , at this , the downward pipe is equipped with at least one , or several sequential mechanical non-return valves , and on the downward pipe on the ground surface there is also installed a down pushing pump for the thermal agent and it's steam condensate , and the end of the upward pipe on the ground surface is connected with a steam turbine , which in its turn , is connected to the said pump by means of a pipeline and a steam condenser for condensation and delivery to the pump of exhaust steam passed through the turbine , characterized by that the ending of the upward pipe is connected with the turbine by means of an impulse accelerator consisting of a controlled valve provided to convert the thermal agent from liquid to gaseous phase , a control device which manages the valve open-close duration and frequency in order to oscillate steam of the thermal agent at a resonant frequency , and a turbine-directed nozzle that accelerates steam of the thermal agent that is sprayed through the valve.2. The geothermal energy device of claim 1 , characterized by the said nozzle performed as a “Laval nozzle”;3. The geothermal energy device of claim 1 , characterized by the impulse accelerator valve at the end of the upward pipe claim 1 , performed in the form of electromagnetic or electro-mechanical controllable valve;4. The geothermal energy device of claim 1 , characterized by the turbine at the end of the upward pipe designed as a condensation type steam turbine;5. The geothermal energy device of claim 1 , characterized by a substance with a low evaporation temperature used as the ...

SYSTEM AND METHOD FOR PROVIDING SUPERCRITICAL STEAM

A system for providing supercritical steam including a first boiler that generates steam via combusting a first fuel, and a second boiler fluidly connected to the first boiler via a conduit which heats the generated steam to supercritical steam temperatures via combusting a second fuel. A first temperature of the conduit may be below a critical corrosion temperature and a second temperature of the conduit is greater than or equal to the critical corrosion temperature. A combined carbon emission rate of the first boiler and the second boiler may be less than a combined carbon emission rate of generating and heating the steam to supercritical steam temperatures using boilers that only combust the first fuel. The first boiler may be fluidly connected to a heat exchanger that heats the generated steam to a supercritical steam temperature via a flue gas produced by a gas turbine. 1. A system for providing supercritical steam comprising:a first boiler that generates steam via combusting a first fuel; anda heat exchanger fluidly connected to the first boiler via a conduit such that the generated steam flows from the first boiler to the heat exchanger;wherein the heat exchanger is disposed in a second boiler operative to heat the generated steam to a supercritical steam temperature via combustion of a second fuel that is different from the first fuel.2. The system of claim 1 , wherein the first fuel is at least one of a heavy oil residue claim 1 , a heavy fuel oil claim 1 , and a solid fuel.3. The system of claim 1 , wherein the second fuel is a gas or a combination of a gas blended with at least one of a liquid fuel or a solid fuel.4. The system of claim 1 , wherein the first boiler and the second boiler are each fluidly connected to a common air source.5. The system of claim 1 , wherein combustion of the second fuel by the second boiler produces a flue gas claim 1 , and the second boiler is further fluidly connected to the first boiler such that the flue gas flows from ...

PLANT CONTROL APPARATUS, PLANT CONTROL METHOD AND POWER PLANT

In one embodiment, a plant control apparatus controls a power plant, which includes a gas turbine, a generator driven by the gas turbine, an exhaust heat recovering boiler to generate first steam using heat of exhaust gas from the gas turbine, a steam turbine driven by the first steam, and a clutch to connect a first shaft connected to the gas turbine and generator with a second shaft connected to the steam turbine. The apparatus includes a starting module to start the gas turbine and generator while holding the steam turbine in a stop state, when the clutch is in a released state. The apparatus further includes a warming module to warm the steam turbine by supplying second steam from equipment different from the boiler to the steam turbine in parallel with the starting of the gas turbine and generator, when the clutch is in a released state. 1. A plant control apparatus configured to control a power plant , the plant comprising:a gas turbine;a generator configured to be driven by the gas turbine;an exhaust heat recovering boiler configured to generate first steam by using heat of exhaust gas from the gas turbine;a steam turbine configured to be driven by the first steam; anda clutch configured to connect a first shaft that is connected to the gas turbine and to the generator with a second shaft that is connected to the steam turbine,the apparatus comprising:a starting module configured to start the gas turbine and the generator while holding the steam turbine in a stop state, when the clutch is in a released state; anda warming module configured to warm the steam turbine by supplying second steam from equipment that is different from the exhaust heat recovering boiler to the steam turbine in parallel with the starting of the gas turbine and the generator, when the clutch is in a released state.2. The apparatus of claim 1 , whereinthe warming module ends the warming of the steam turbine based on a metal temperature of the steam turbine, andthe starting module begins ...

ULTRA EFFICIENT TURBO-COMPRESSION COOLING

A turbo-compression cooling system includes a power cycle and a cooling cycle coupled one to the other. The power cycle implements a waste heat waste heat exchanger configured to evaporate a first working fluid and a turbine configured to receive the evaporated working fluid. The turbine is configured to rotate as the first working fluid expands to a lower pressure. A condenser condenses the first working fluid to a saturated liquid and a pump pumps the saturated liquid to the waste heat waste heat exchanger. The cooling cycle implements a compressor increasing the pressure of a second working fluid, a condenser condensing the second working fluid to a saturated liquid upon exiting the compressor, an expansion valve expanding the second working fluid to a lower pressure, and an evaporator rejecting heat from a circulating fluid to the second working fluid, thereby cooling the circulating fluid. 1. A system for turbo-compression cooling comprising: a first working fluid;', 'a waste heat exchanger configured to heat the first working fluid to a superheated vapor;', 'a turbine receiving the superheated vapor working fluid, the turbine having a plurality of vanes disposed around a central shaft and configured to rotate about the central shaft, the plurality of vanes configured to rotate as the working fluid expanding to a lower pressure; and', 'a condenser condensing the working fluid to a subcooled liquid;, 'a power cycle comprising a second working fluid;', 'a compressor configured to increase the pressure of the second working fluid;', 'a cooler configured to cool the second working fluid after exiting the compressor;', 'an expansion valve wherein the second working fluid expands to a lower pressure;', 'an evaporator rejecting heat from a circulating fluid to the second working fluid, thereby cooling the circulating fluid;, 'a cooling cycle comprisingwherein the turbine and compressor are coupled one to the other, thereby coupling the power cycle and the cooling ...

COOLING DEVICE FOR HIGH TEMPERATURE PIPE

In a cooling device for a high temperature pipe, a high temperature pipe is efficiently cooled, and cooling performance is improved. A cooling device () for a high temperature pipe that cools a surface to be cooled () of a pipe () as a high temperature pipe includes: a cooling medium supply header () that is disposed so as not to shield heat dissipation by radiation from the surface to be cooled () to the periphery, and allows a cooling medium to flow out toward the surface to be cooled (); and a cooling medium supply device () that supplies the cooling medium to the cooling medium supply header (). 1. A cooling device for a high temperature pipe installed on a periphery of a surface to be cooled of a high temperature pipe , the cooling device for a high temperature pipe comprising:a cooling medium supply header that is disposed at such a position as not to shield heat dissipation by radiation from the surface to be cooled to the periphery, and allows a cooling medium to flow out toward the surface to be cooled; anda cooling medium supply device that supplies the cooling medium to the cooling medium supply header.2. The cooling device for a high temperature pipe according to claim 1 , whereinthe surface to be cooled is an exposed surface of the high temperature pipe exposed from an uncovered part of a heat insulating material that covers the high temperature pipe, and the cooling medium supply header is disposed outside the surface to be cooled.3. The cooling device for a high temperature pipe according to claim 2 , whereinthe cooling medium supply header is supported on an outer surface of the heat insulating material.4. The cooling device for a high temperature pipe according to claim 2 , whereinthe cooling medium supply header is supported on the high temperature pipe and an outer surface of the heat insulating material by a support member.5. The cooling device for a high temperature pipe according to claim 1 , further comprising:a cooling medium outflow nozzle ...

BOILER WITH INTEGRATED AIR COMPRESSOR

An integrated power generation system is provided. The system includes an heat source that produces a first gas flow to power a turbine operatively coupled to a compressor. The first gas flow can also heat a feedwater flow passing through a boiler. The compressor can produce a second gas flow that may be divided in two portions, the first portion flowing back to the heat source and the second portion flowing to an end user. Also, the second portion may be routed through an air cooler to dissipate heat to the feedwater flow to cool the second portion as well as preheat the feedwater flow prior to entering the boiler. The first portion can also exchange heat with the first gas flow exiting the boiler prior to the first portion entering the heat source. The boiler operation and the compressor operation are operable independently or concurrently. 1. An integrated power generation system comprising:a heat source producing a first gas flow;an expander in flow communication with the first gas flow from the heat source;a boiler in flow communication with the first gas flow from the expander;a feedwater flow in flow communication with the boiler;a compressor operatively coupled to the expander, the compressor producing a second gas flow divisible into a first portion and a second portion, the first portion in flow communication with the heat source and the second portion in flow communication with a point of use.2. The system of claim 1 , further comprising a first heat exchanger in flow communication with the feedwater flow and the second portion of the second gas flow claim 1 , the first heat exchanger exchanging heat between the second portion of the second gas flow and the feedwater flow.3. The system of claim 1 , further comprising a second heat exchanger in flow communication with the first gas flow and the first portion of the second gas flow claim 1 , the second heat exchanger exchanging heat between the first gas flow and the first portion of the second gas flow.4. ...

MULTI-SHAFT COMBINED CYCLE PLANT, AND CONTROL DEVICE AND OPERATION METHOD THEREOF

In an operation method of a multi-shaft combined cycle plant, a low-load mode in which an output of the multi-shaft combined cycle plant is adjusted by adjustment of only an output of a gas turbine and a high-load mode in which the output of the multi-shaft combined cycle plant is adjustable by adjustment of the output of the gas turbine and adjustment of an output of a steam turbine are switched according to a demanded load. In the low-load mode, steam at a standby flow rate at which the steam turbine is capable of maintaining a predetermined initial load is supplied to the steam turbine, and the initial load is applied to the steam turbine. 1. An operation method of a multi-shaft combined cycle plant including a gas turbine , an exhaust heat recovery boiler that generates steam using an exhaust gas from the gas turbine , and a steam turbine that is driven by the steam generated by the exhaust heat recovery boiler , in which a gas turbine rotor of the gas turbine and a steam turbine rotor of the steam turbine are not mechanically connected to each other , the method comprising:switching, according to a demanded load, between a low-load mode in which an output of the multi-shaft combined cycle plant is adjusted by adjustment of only an output of the gas turbine and a high-load mode in which the output of the multi-shaft combined cycle plant is adjustable by adjustment of the output of the gas turbine and adjustment of an output of the steam turbine; andsupplying steam at a standby flow rate at which the steam turbine is capable of maintaining a predetermined initial load to the steam turbine, and applying the initial load to the steam turbine even in the low-load mode.2. The operation method of a multi-shaft combined cycle plant according to claim 1 ,wherein when the demanded load becomes low in the high-load mode and the high-load mode is switched to the low-load mode, the steam at the standby flow rate is supplied to the steam turbine.3. The operation method of a ...

SYSTEM AND METHOD FOR DECOUPLING STEAM PRODUCTION DEPENDENCY FROM GAS TURBINE LOAD LEVEL

A system for decoupling steam production dependency from gas turbine load includes a gas turbine having an inlet system, a compressor, a combustor and a turbine. The combustor includes a plurality of axially staged fuel injectors positioned downstream from a plurality of primary fuel nozzles and a center fuel nozzle. The gas turbine further includes at least one bleed air extraction port that is in fluid communication with at least one of the compressor, a compressor discharge casing or the combustor. The system also includes a diluent injection system that is in fluid communication with the combustor and an exhaust section that is disposed downstream from the turbine. The exhaust section includes an oxidation catalyst system and a heat recovery steam generator. 1. A system for decoupling steam production dependency from gas turbine load , comprising:a gas turbine having an inlet system, a compressor, a combustor and a turbine, the combustor comprising a plurality of axially staged fuel injectors positioned downstream from a plurality of primary fuel nozzles and a center fuel nozzle, the gas turbine further comprising at least one bleed air extraction port, wherein the bleed air extraction port is in fluid communication with at least one of the compressor, a compressor discharge casing or the combustor;a diluent injection system in fluid communication with the combustor; andan exhaust section disposed downstream from the turbine, the exhaust section comprising an oxidation catalyst system and a heat recovery steam generator, wherein the oxidation catalyst system and the heat recovery steam generator receive an exhaust gas from an outlet of the turbine.2. The system as in claim 1 , wherein the at least one bleed air extraction port is fluidly coupled to the compressor and to an inlet section of the gas turbine via a bleed air inlet port.3. The system as in claim 1 , wherein the at least one bleed air extraction port is fluidly coupled to the compressor and to the ...

SYSTEM TO AGGREGATE WORKING FLUID FOR HEAT RECOVERY STEAM GENERATORS

A system for aggregating a working fluid includes a fluid delivery line defining a fluid connection to at least one downstream process component; a plurality of collection lines each fluidically connected to a plurality of header lines by a respective set of header links; and a connecting junction fluidically connecting each of the plurality of collection lines to the fluid delivery line, the connecting junction including: at least one tee member oriented substantially perpendicularly with respect to the fluid delivery line, the at least one tee member connected to the fluid delivery line, and a plurality of branch fluid lines each fluidically coupling a respective one of the plurality of collection lines to the at least one tee member. 1. A system for aggregating a working fluid , the system comprising:a fluid delivery line defining a fluid connection to at least one downstream process component;a plurality of collection lines each fluidically connected to a plurality of header lines by a respective set of header links; and at least one tee member oriented substantially perpendicularly with respect to the fluid delivery line, the at least one tee member connected to the fluid delivery line, and', 'a plurality of branch fluid lines each fluidically coupling a respective one of the plurality of collection lines to the at least one tee member., 'a connecting junction fluidically connecting each of the plurality of collection lines to the fluid delivery line, the connecting junction including2. The system of claim 1 , wherein the at least one tee member includes a plurality of tee members claim 1 , and wherein the plurality of branch fluid lines fluidically couples each of the plurality of header lines to each of the plurality of tee members.3. The system of claim 1 , wherein the plurality of branch fluid lines includes:a first branch fluid path coupled to a first collection line of the plurality of collection lines and coupled to a first tee member of the at least one ...

PLANT CONTROL APPARATUS AND COMBINED CYCLE POWER PLANT

In one embodiment, a combined cycle power plant includes first and second superheaters to generate first and second main steams, first and second reheaters to heat first and second discharge steams to generate first and second reheat steams, and a steam turbine to be supplied with the merged first and second reheat steams. The plant further includes a first valve to adjust a flow rate of the first discharge or reheat steam, and a second valve to adjust a flow rate of the second discharge or reheat steam. A plant control apparatus includes a determination module to determine a target opening degree of the second valve by using flow rates of the first and second main steams, and a controller to compare the determined target opening degree with a valve opening degree of the second valve and to control the second valve based on a comparison result. 1. A plant control apparatus configured to control a combined cycle power plant comprising:a first superheater configured to recover heat of exhaust gas of a first gas turbine to generate first main steam;a second superheater configured to recover heat of exhaust gas of a second gas turbine to generate second main steam;a first steam turbine configured to be supplied with the first main steam and the second main steam;a first reheater configured to heat first discharge steam obtained by dividing discharge steam of the first steam turbine to generate first reheat steam;a second reheater configured to heat second discharge steam obtained by dividing the discharge steam of the first steam turbine to generate second reheat steam;a second steam turbine configured to be supplied with the first reheat steam and the second reheat steam after the first reheat steam and the second reheat steam are merged;a first valve configured to adjust a flow rate of the first discharge steam supplied to the first reheater or the first reheat stream discharged from the first reheater; anda second valve configured to adjust a flow rate of the second ...

Zero Emissions Power Generation Boiler

This is a zero emissions power generation boiler that can be used to drive a wide range of steam turbines, from 20 MW up to 1200 MW, creating dry steam pressure ranging from 1000 psi up to 4500 psi. It creates steam by burning liquid hydrogen with liquid oxygen, completely eliminating the emission of greenhouse gases, lethal poisons, and every form of pollutant. It employs high-pressure cryogenic fuel pumps, a water cooling system, an electronic sparking system, a double-wall cylindrical boiler with a hemispherical top, and a control system that employs electronic sensors, actuators, signal conditions, microprocessors, digital interfaces, and mechanical back-up systems. It can be used in new power plants or as a replacement for current boilers in existing power plants. It has the option of working as part of a combined cycle system and can employ steam reheat systems. 1. First claim: This zero [harmful] emissions power plant boiler is a unique design that can produce enough steam to run turbines ranging from 20 MW to 1200 MW , at pressures of 1000-4500 psi , by means of burning liquid hydrogen and liquid oxygen , completely eliminating the emission of greenhouse gases , lethal poisons , and all known pollutants , in a system comprising:cryogenic fuel tankshigh-pressure cryogenic fuel pumpsrings of centrally-located burnersan electronic sparking system.2. Second claim: The boiler is a unique , double-walled cylindrical design with a hemispherical top capable of handling the high stresses involved , in which steam pressure is created in the central cavity , rather than in a system of piping along the sides , and is comprised of:an outer wallan inner walla steam header at the top.3. Third claim: The boiler is cooled by a system of water pumps that send heated water at high pressure to rings of nozzles located between the burners and the walls , sending the water up into the central cavity where it becomes steam while cooling the walls and top of the boiler , in a ...

Passive low temperature heat sources organic working fluid power generation method

The present invention relates to a passive low temperature heat energy organic working fluid power generation method and system, Comprising: organic working fluid in a first evaporator and a second evaporator are heated to evaporate; when a pressure of the organic working fluid reaches a setting pressure, a self-operating pressure control valve at an outlet of the evaporator is triggered opening by a working pressure, and steam of the organic working fluid flows into a turbine, pushes the turbine to work, and drives a generator to output electric energy; after work is completed, the steam flows into a condenser to be condensed, and working steam is output in turn through the first evaporator and the second evaporator, and thus the turbine is driven continuously to work and output electric energy. Compared with the prior technology, the present invention has reliable performance, and is operated by heating and evaporating of the working fluid in a closed space to achieve increased pressure.

EXTERNAL REACTOR VESSEL COOLING AND ELECTRIC POWER GENERATION SYSTEM

An external reactor vessel cooling and electric power generation system according to the present invention includes an external reactor vessel cooling section formed to enclose at least part of a reactor vessel with small-scale facilities so as to cool heat discharged from the reactor vessel, a power production section including a small turbine and a small generator to generate electric energy using a fluid that receives heat from the external reactor vessel cooling section, a condensation heat exchange section to perform a heat exchange of the fluid discharged after operating the small turbine, and condense the fluid to generate condensed water, and a condensed water storage section to collect therein the condensed water generated in the condensation heat exchange section, wherein the fluid is phase-changed into gas by the heat received from the reactor vessel. The external reactor vessel cooling and electric power generation system according to the present invention can continuously operate even during an accident as well as during a normal operation to cool the reactor vessel and produce emergency power, thereby enhancing system reliability. The external reactor vessel cooling and electric power generation system according to the present invention can easily apply safety class or seismic design using small-scale facilities, and its reliability can be improved owing to applying the safety class or seismic design. 1. An external reactor vessel cooling and electric power generation system , comprising:a reactor vessel;an external reactor vessel cooling section formed to enclose at least part of the reactor vessel so as to cool heat discharged from the reactor vessel;a power production section including a small turbine and a small generator to generate electric energy using a fluid that receives heat from the external reactor vessel cooling section;a condensation heat exchange section to perform a heat exchange of the fluid discharged after operating the small ...

SOLAR AND RENEWABLE/WASTE ENERGY POWERED TURBINE WITH TWO STAGE HEATING AND GRAPHITE BODY HEAT EXCHANGER

A turbine driven from renewable or waste energy sources has a working fluid in a two stage heating process using a first heating apparatus using a renewable or waste energy source and a second heating apparatus comprising a graphite body containing an embedded heat exchanger heated by concentrated solar energy where the graphite body releases stored heat to heat the working fluid to provide a continuous stream of the working fluid heated to a working temperature for input to the turbine. A relationship exists between an outer surface area of the embedded heat exchanger tube and a mass of graphite in the graphite body whereby there is from 0.60 mto 20 mof outer surface area of embedded heat exchanger tube per tonne of graphite in the graphite body. 1. A process for operating a turbine driven from renewable or waste energy sources wherein a working fluid which drives the turbine is passed around a working fluid circuit and heated in a two stage heating process using a first heating apparatus using a renewable or waste energy source and a second heating apparatus comprising a graphite body heated by concentrated solar energy the graphite body containing an embedded heat exchanger comprising at least one heat exchanger tube embedded in and in contact with the graphite body , the process , comprising:heating the working fluid using the renewable or waste source to generate a stream of working fluid heated to an intermediate temperature;heating the graphite body using the concentrated solar energy to store heat within the graphite body;delivering the stream of heated working fluid into the heat exchanger which is embedded in the graphite body whereby the graphite body releases stored heat to heat the working fluid to provide a continuous stream of the working fluid heated to a working temperature for input to the turbine; and{'sup': 2', '2, 'wherein, a relationship exists between an outer surface area of the embedded heat exchanger tube and a mass of graphite in the ...

DEVICE FOR POWER GENERATION ACCORDING TO A RANKINE CYCLE

A device for power generation according to a Rankine cycle, in particular according to an organic Rankine cycle (ORC), comprises a turbine (), for expanding a vapour of a working fluid, and at least one heat exchanger (), through which the expanded vapour has to flow. The turbine () and the heat exchanger(s) () are contained in a vapour tight container (). The turbine () is a radial-outward-flow type turbine having a shaft that is led in a sealed manner out of said container (), an axial vapour inlet port arranged opposite the shaft and located inside the container (), and a stator exhaust ring with stator exhaust blades defining peripheral vapour exhaust openings for discharging the expanded vapour directly into the vapour tight container (), in which the expanded vapour flows through the heat exchanger(s) (). 1. A device for power generation according to a Rankine cycle , in particular according to an organic Rankine cycle (ORC) , comprising:{'b': '16', 'a turbine () for expanding a vapour of a working fluid; and'}{'b': 18', '20', '22, 'at least one heat exchanger (, , ) through which the expanded vapour has to flow; and'}{'b': 10', '16', '18', '20', '22, 'a vapour tight container () containing said turbine () and said at least one heat exchanger (, , ),'}{'b': 16', '66', '10', '10', '18', '20', '22, 'wherein said turbine () has a shaft () that is led in a sealed manner out of said container () and discharges the expanded vapour directly into said vapour tight container (), in which the expanded vapour flows through said at least one heat exchanger (, , );'}characterized in that{'b': '16', 'said turbine () is a radial-outward-flow type turbine having{'b': 82', '10, 'an axial vapour inlet port () arranged opposite said shaft and located inside the container (); and'}{'b': 56', '58', '10, 'sub': 4', '4, 'a stator exhaust ring () with stator exhaust blades () defining peripheral vapour exhaust openings for discharging the expanded vapour directly into said vapour ...

TURBINE SHAFT BEARING AND TURBINE APPARATUS

The present invention provides a turbine shaft bearing apparatus, comprising two axially spaced, inlet side and outlet side bearings for providing support to a turbine shaft to which are connected a plurality of turbine wheels such that the turbine shaft, the two spaced bearings, and the plurality of turbine wheels are all coaxial, wherein the outlet side bearing is protected from overheating by motive fluid expanded by one or more of the plurality of turbine wheels or stages by a solid bearing housing which surrounds the outlet side bearing which is supported and provided with a conduit through which a lubricating medium for lubricating said outlet side bearing is supplied from a port external to said turbine. The present invention is also directed to a single turbine module, comprising a plurality of axially spaced turbine wheels, each of which constitutes one expansion stage of said turbine module, being connected to a common turbine shaft and coaxial therewith; an inlet through which motive fluid vapor is introduced to a first stage of said turbine wheels; a structured bleeding exit opening formed in an outer turbine casing of the turbine module; and a passage defined between two of the turbine wheels and in fluid communication with the bleeding exit opening, wherein expanded motive fluid vapor is extracted through said structured bleeding exit opening and is supplied to a heat exchange component, for heating the motive fluid condensate. 1. Turbine shaft bearing apparatus , comprising two axially spaced , inlet side and outlet side bearings for providing support to a turbine shaft to which are connected a plurality of turbine wheels such that said turbine shaft , said two spaced bearings , and said plurality of turbine wheels are all coaxial , wherein said outlet side bearing is protected from overheating by motive fluid expanded by one or more of said plurality of turbine wheels or stages by a solid bearing housing which surrounds said outlet side bearing which ...

Solar-aided coal-fired flexible power generation system and operation method thereof

A solar-aided coal-fired flexible power generation system and an operating method thereof are provided. The system includes a coal-fired thermal power generation system and a high-temperature heat storage system coupled with solar thermal power generation; wherein a heat storage medium heater is arranged in the boiler flue; the flow rates of heat storage medium entering the solar heat collection device and the heat storage medium heater are adjusted by the regulating valve and the pump, eliminating irradiation fluctuation influences and maintaining stable power; a heat storage medium tank is used for peak shaving to reduce steam turbine output under stable boiler combustion; the flow and temperature of the feedwater entering the heat storage medium and feedwater heat exchanger are adjusted to realize rapid load cycling. The present invention can realize solar and coal-fired generation coupling, reduce coal consumption, and greatly improve the flexibility and economy. 1. A solar-aided coal-fired flexible power generation system , comprising: a coal-fired thermal power generation system and a high-temperature heat storage system coupled with solar thermal power generation; wherein:{'b': 1', '2', '3', '4', '5', '6', '7', '8', '9', '10', '1', '1', '2', '1', '9', '2', '3', '1', '3', '9', '3', '7', '3', '6', '3', '4', '4', '6', '5', '6', '7, 'the coal-fired thermal power generation system comprises a boiler (), a steam turbine high pressure cylinder (), a steam turbine middle and low pressure cylinder (), a condenser (), a condensate pump (), a low pressure heater (), a deaerator (), a feedwater pump () and a high pressure heater and regulating valve group () which are connected in sequence; wherein a heat storage medium heater () is also arranged in a flue of the boiler (); a superheated steam outlet of the boiler () is connected with an inlet of the steam turbine high pressure cylinder (); a feedwater inlet of the boiler () is connected with a feedwater outlet of the ...

Hybrid power generation equipment

Disclosed is a hybrid power generation facility. The hybrid power generation facility includes a gas turbine including a compressor configured to compress air introduced from an outside, a combustor configured to mix the compressed air with fuel and to combust the air and fuel mixture, and a turbine configured to produce power with first combustion gas discharged from the combustor, a boiler configured to burn a mixture of the first combustion gas and air, a first water heat exchanger configured to pass second combustion gas discharged from the boiler and to heat water through heat exchange to between the water and the second combustion gas, a water supply device configured to supply water to the first water heat exchanger, a steam turbine through which steam generated in the boiler passes, and a fuel heat exchanger configured to pass fuel supplied to the combustor and to pass a portion of water that is returned to the water supply device from the first water heat exchanger and has a higher temperature than the water supplied to the first water heat exchanger.

Power Generation System And Method With Partially Recuperated Flow Path

The present disclosure relates to a power generation system and related methods that use supercritical fluids, whereby a portion of the supercritical fluid is recuperated. 1a supercritical fluid cycle including a supercritical fluid compressor configured to receive and compress a supercritical fluid, a supercritical fluid turbine configured to receive and expand the supercritical fluid, and a recuperating heat exchanger configured to receive discharge streams from the supercritical fluid compressor and the supercritical fluid turbine;an air breathing cycle configured to heat air flowing along the air breathing cycle; anda plurality of heat exchangers arranged so that supercritical fluid from the supercritical fluid cycle and air from the an air breathing cycle passes therethrough but does not intermix, wherein a first heat exchanger of the plurality of heat exchangers is arranged to feed into an inlet of the supercritical fluid turbine, and a second heat exchanger of the plurality of heat exchangers is arranged to feed into an inlet of the supercritical fluid compressor, wherein the first heat exchanger has a first heat capacity rate and the second heat exchanger has a second heat capacity rate that is substantially different than the first heat capacity rate;. A system configured to generate power, comprising:1) split the supercritical fluid discharged from the supercritical fluid compressor into first and second discharge streams of compressed supercritical fluid, such that a) the first discharge stream of compressed supercritical fluid flows through the recuperating heat exchanger, and b) the second discharge stream of compressed supercritical fluid flows through the first heat exchanger of the plurality of heat exchangers, and2) split the supercritical fluid discharged from the supercritical fluid turbine into a first and second discharge streams of expanded supercritical fluid such that a) the first discharge stream of expanded supercritical fluid flows through ...

WASTEWATER PROCESSING SYSTEMS FOR POWER PLANT FLUE GAS DESULFURIZATION WATER AND OTHER INDUSTRIAL WASTEWATERS

Methods, systems, and/or apparatuses for treating wastewater produced at a thermoelectric power plant, other industrial plants, and/or other industrial sources are disclosed. The wastewater is directed through a wastewater concentrator including a direct contact adiabatic concentration system. A stream of hot feed gases is directed through the wastewater concentrator. The wastewater concentrator mixes the hot feed gases directly with the wastewater and evaporates water vapor from the wastewater. The wastewater concentrator separates the water vapor from remaining concentrated wastewater. A contained air-water interface liquid evaporator may be arranged to pre-process the wastewater before being treated by the wastewater concentrator. 1. A wastewater treatment system for a thermoelectric power plant , the system comprising:a wastewater concentrator implementing a direct contact adiabatic wastewater concentrator system, the wastewater concentrator comprising a direct contact evaporative section and a gas-liquid separator;a stream of wastewater generated in a thermoelectric power plant operatively connected to the wastewater concentrator to supply the wastewater to the direct contact evaporative section; anda stream of hot feed gases operatively connected to the wastewater concentrator to supply feed gases to the direct contact evaporative section simultaneously as the stream of wastewater;wherein the direct contact evaporative section mixes the hot feed gases directly with the wastewater and evaporates water from the wastewater to form water vapor and concentrated wastewater, andwherein the gas-liquid separator separates the water vapor from the concentrated wastewater and exhausts discharge gases from the gas-liquid separator, including the water vapor and some or all of the feed gases.2. The wastewater treatment system of claim 1 , wherein the stream of wastewater comprises at least one of flue gas desulfurization purge water claim 1 , cooling tower purge water ...

SUPPLY ASSEMBLY FOR A TURBINE OF A SOLAR THERMODYNAMIC SYSTEM AND SOLAR THERMODYNAMIC SYSTEM COMPRISING SAID ASSEMBLY

Supply assembly for a turbine of a solar thermodynamic system provided with plural multiple parabolic mirrors for heating a first thermal carrier fluid contained in a tank to a first temperature, comprising a column structure provided at the upper part with an exit. The column structure comprises: a lower portion provided with two inlets connected to the tank to be supplied with the first thermal carrier fluid, the lower portion comprising first and second heat exchangers supplied with a second thermal carrier fluid respectively to an overheated temperature and re-overheating temperature; an upper portion fluidically connected with the lower portion, the upper portion comprising a boiler to bring the second fluid from a pre-heating temperature to a boiling temperature, and a cylindrical body arranged on the boiler; a pre-heating and supplying structure for heating the second thermal carrier fluid to the pre-heating temperature and supply it to the column structure. 1. Supply assembly for a turbine of a solar thermodynamic system of the type provided with a plurality of parabolic mirrors arranged for converting solar energy into thermal energy for heating a first thermal carrier fluid contained in a tank to a first temperature , comprising:a column structure provided at the upper part with an exit for bleeding saturated dry steam:a lower portion provided with two inlets connected to said tank such as to be supplied with said first thermal carrier fluid heated by said mirrors, said lower portion comprising a first heat exchanger and a second heat exchanger arranged for being supplied with a second thermal carrier fluid at an overheating temperature and re-overheating temperature, respectively;an upper portion fluidically connected to said lower portion and arranged above it so that said first thermal carrier fluid can pass from said lower portion to said upper portion, said upper portion comprising a boiler arranged for bringing said second fluid at a boiling ...

HYBRID POWER GENERATION SYSTEM

Disclosed herein is a hybrid power generation system. The hybrid power generation system may enhance efficiency of production of electricity and heating heat by integrating power generation using supercritical carbon dioxide (CO) and cogeneration. 1. A hybrid power generation system including a power generation system that uses supercritical carbon dioxide as a working fluid to produce electrical energy and a cogeneration system that burns fuel to produce thermal energy and electrical energy , comprising:at least one pump operable to circulate the working fluid;at least one recuperator coupled to the pump and operable to heat the working fluid having passed through the pump;at least one first heat exchanger coupled to the at least one recuperator and operable to heat the working fluid having passed through the recuperator using an external heat source;a plurality of turbines coupled to the at least one first heat exchanger and operable to be driven by the working fluid heated in the at least one first heat exchanger; anda second heat exchanger operable to exchange heat between heating water of the cogeneration system and the working fluid to heat the heating water and cool the working fluid, whereinthe at least one recuperator is coupled to the turbines and operable to cool working fluid having passed through the turbines by heat exchange with the working fluid having passed through the pump in the recuperator, and the at least one recuperator is coupled to the second heat exchanger to supply the cooled working fluid to the second heat exchanger; andthe power generation system using supercritical carbon dioxide and the cogeneration system share the second heat exchanger.2. The hybrid power generation system according to claim 1 , whereinthe second heat exchanger is coupled to the pump to provide the working fluid having passed through the second heat exchanger to the pump,at least one of the recuperator and the heat exchanger and is coupled to the cogeneration ...

SYSTEM AND METHOD OF CLEANING CONDENSER FOR BINARY POWER GENERATION

A system of cleaning a condenser provided in a circulation flow passage for allowing circulation of a working medium in a binary power generation system, includes: an inlet header into which a cooling medium flows; and a heat exchanger including a plurality of branch ports into which the cooling medium flows from the inlet header. The heat exchanger is configured to perform heat exchange between the working medium and the cooling medium to condense the working medium. The cleaning system includes a switching unit configured to switch a flow of the cooling medium to a direction from the heat exchanger to the inlet header. 1. A system of cleaning a condenser for binary power generation , the condenser being provided in a circulation flow passage for allowing circulation of a working medium in a binary power generation system , whereinthe condenser comprises:an inlet header into which a cooling medium flows; anda heat exchanger including a plurality of branch ports into which the cooling medium flows from the inlet header, the heat exchanger being configured to perform heat exchange between the working medium and the cooling medium to condense the working medium, andthe cleaning system comprises a switching unit configured to switch a flow of the cooling medium to a direction from the heat exchanger to the inlet header.2. The system of cleaning the condenser for binary power generation according to claim 1 , comprising:a third pipe adapted to connect a first pipe for allowing the cooling medium to flow into the inlet header of the condenser, to a second pipe for allowing the cooling medium to flow out of the condenser; anda fourth pipe adapted to connect a second portion of the first pipe to a fourth portion of the second pipe, the second portion being located downward, in a flow direction of the cooling medium, of a first portion of the first pipe to which the third pipe is connected, the fourth portion being located downstream, in the flow direction of the cooling ...

Control method for optimizing solar-to-power efficiency of solar-aided coal-fired power system under off-design working conditions

A control method for optimizing a solar-to-power efficiency of a solar-aided coal-fired power system under off-design working conditions is provided. Through reading the relevant information of the solar collecting system, the coal-fired power generation system, the environmental conditions, and the working conditions of the solar-aided coal-fired power system, the water flow rate range able to be heated by the solar collecting unit and the solar-coal feedwater flow distribution ratio range of the solar-aided coal-fired power system are determined; through establishing the relationship between the solar-to-power efficiency and the solar-coal feedwater flow distribution ratio of the solar-aided coal-fired power system under the off-design working conditions, the solar-coal feedwater flow distribution ratio is regulated, so that a flow rate of water entering the solar collecting system to be heated is controlled, thereby maximizing the solar-to-power efficiency and improving the economy of the solar-aided coal-fired power system under the off-design working conditions. The present invention provides clear guidance to optimize the solar-aided coal-fired power system under the off-design working conditions, enable solar energy to fully play its role in the solar-aided coal-fired power system, improve the utilization rate of solar energy, facilitate the consumption of the renewable energy, and greatly increase the economy of the solar-aided coal-fired power system. 2. The control method claim 1 , as recited in claim 1 , wherein: in the step (1) claim 1 , the read relevant information of the environmental conditions comprises a current solar irradiance and an environmental temperature; the read relevant information of the solar collecting system comprises relevant information of the solar collecting unit and relevant information of a heliostat field; the read relevant information of the coal-fired power generation system comprises main steam parameters claim 1 , ...

Power Recovery System Using A Rankine Power Cycle Incorporating A Two-Phase Liquid-Vapor Expander With Electric Generator

A power recovery system using the Rankine power cycle incorporating a two-phase liquid-vapor expander with an electric generator which further consists of a heat sink, a heat source, a working fluid to transport heat and pressure energy, a feed pump and a two-phase liquid-vapor expander for the working fluid mounted together with an electric generator on one rotating shaft, a first heat exchanger to transport heat from the working fluid to the heat sink, a second heat exchanger to transport heat from the heat source to the working fluid. 1. A power recovery system for recovery of part of the required energy input during regasification of LNG using consecutive first and second Rankine power cycle sub-systems , the first and the second Rankine power cycle sub-systems of the power recovery system each comprising:a working fluid contained in a closed loop system, the closed-loop system comprising a pump two-phase liquid-vapor expander generator having (i) a feed pump, (ii) an induction generator and (iii) a two-phase liquid-vapor expander all mounted on a common, rotating axial shaft, the feed pump pumping liquid-phase working fluid to a high pressure, the pressurized liquid-phase working fluid then passing through the induction generator to become partly heated and vaporized therein, and then flowing out of the pump two-phase liquid-vapor expander generator;a first heat exchanger with a heat source, the first heat exchanger connected to the pump two-phase liquid-vapor expander generator via the closed-loop system, the heat source heating the pressurized working fluid into higher vapor content while it is passing through, the heated and pressurized two-phase working fluid then re-entering the pump two-phase liquid-vapor expander generator at the two-phase liquid-vapor expander wherein the heated and pressurized two-phase working fluid expanded and driving the rotating center shaft, and subsequently the induction generator, the expanded two-phase working fluid flowing ...

Production of mechanical/electrical energy from heat energy with and by the use of buoyancy factor on evaporation or sublimation and condensation

There are various source of heat energy. Amongst the various sources Solar energy, waste heat form garbage, waste heat from transformers, waste heat from chemical reactions, waste heat from plant and machinery, heat from geo-thermal or the vast heat energy lying in the seas and oceans are some of the major ones which are free and unused. Apart from these, we can also produce heat energy from fuels like fossil fuels, hydrogen gas, forest products etc. A lot of heat energy is being wasted and though converted to mechanical or electric energy it is not that efficient. However, using the evaporation or sublimation and condensation process brought about through difference in temperature and the use of buoyancy factor to increase the efficiency of the energy production, the heat energy can be converted to mechanical or electrical energy in excess of hundred percent. Moreover, heat energy obtained from hydrolysis of some chemicals like salts or hydroxides and their dehydration for reuse or the heat stored as latent heat on melting of salts can be utilized for huge storage of energy for some months or more and use it through this invention method. The energy lying in the water under the oceans during winter can be easily utilized for production of huge energy when there are very low (freezing) temperatures on the surface of the earth.

CONTROL SYSTEM FOR OXY FIRED POWER GENERATION AND METHOD OF OPERATING THE SAME

A method of operating an electricity production system having at least one oxy-combustion boiler unit and a turbine for electricity generation at least includes the steps of: determining a power demand for an air separation unit that supplies oxygen gas to the boiler unit and a gas processing unit that treats flows of fluid for COcapture; determining a total power demand for electricity production that includes the determined power demand for the air separation unit and the gas processing unit; and coordinating operation of the air separation unit, gas processing unit, the boiler unit, and the turbine such that power generated by the plant provides power that meets the determined total power demand and also controls steam pressure of the turbine to a pre-specified level. 1. A method of operating an electricity production system having at least one oxy-combustion boiler unit and a turbine for electricity generation , comprising:determining a power demand for an air separation unit that supplies oxygen gas to the boiler unit and a gas processing unit that treats flows of fluid for carbon dioxide capture;determining a total power demand for electricity production that includes the determined power demand for the air separation unit and the gas processing unit; andcoordinating operation of the air separation unit, the gas processing unit, the boiler unit, and the turbine such that power generated by the turbine provides power that meets the determined total power demand and also controls steam pressure of the turbine to a pre-specified level.2. The method of claim 1 , comprising:selecting a mode of control from one of a boiler following mode, a turbine following mode, and a coordinated control mode for the coordinating operation of the air separation unit, the gas processing unit, the boiler unit, and the turbine based on coordinated turbine pressure control and desired turbine power.3. The method of claim 2 , wherein the pre-specified level is a pressure set point ...

OXY FIRED POWER GENERATION SYSTEM AND METHOD OF OPERATING THE SAME

An electricity production system configured to operate in accordance with a method of operating an electricity production system that at least includes the steps of: determining an oxygen distribution between oxygen gas to be separated by an air separation unit (“ASU”) and oxygen gas stored in a storage tank of the ASU to be fed to the boiler unit, determining a carbon capture value for a gas processing unit, determining a power consumption value for the gas processing unit and the ASU, determining a total power demand value based on the power consumption value of the gas processing unit and the ASU, and on a determined electricity demand, and controlling the boiler unit, the turbine, the ASU, and the gas processing unit based on the determined total power demand along with correcting signals generated from a coordinated Model Predictive Control. 1. A method of operating an electricity production system having at least one oxy-combustion boiler unit , a turbine for electricity generation , an air separation unit and a gas processing unit comprising: determining an oxygen distribution between oxygen gas to be separated by the air separation unit and oxygen gas stored in a storage tank of the air separation unit to be fed to the boiler unit;', 'determining a carbon capture value for the gas processing unit via a scheduler;', 'determining a power consumption value for the gas processing unit and the air separation unit based on the carbon capture value and the determined oxygen distribution and determining a total power demand based on the power consumption value of the gas processing unit and the air separation unit and a determined electricity demand from one of a pre-specified electricity demand value, a grid frequency value, and an automatic dispatch system value; and', 'controlling the boiler unit, the turbine, the air separation unit, and the gas processing unit based on the determined total power demand along with correcting signals determined by a coordinated ...

METHOD FOR OPERATING A CHEMICAL PLANT

A chemical plant and operating method therefor; the chemical plant comprises a steam turbine having a shaft, a first pressure turbine stage and a second pressure turbine stage, each being arranged on the shaft and being connected in series in terms of the steam process; steam for driving the steam turbine is obtained from a reactor plant, said reactor plant producing a hydrogen-containing substance from a carbon-containing energy-carrier stream; the steam is heated in an overheating step before being supplied to the second pressure turbine stage; the steam turbine has a third pressure turbine stage which is arranged on the shaft and which is connected between the first pressure turbine stage and the second pressure turbine stage in terms of the steam process; and the steam passes through the overheating step after exiting the third pressure turbine stage. 1. A method comprising:operating a chemical plant, wherein the chemical plant comprises a steam turbine defining a shaft and first pressure turbine stage, a second pressure turbine stage, and a third pressure turbine stage connected to the shaft in series, wherein steam passing through the steam turbine successively passes through the first pressure turbine stage, the third pressure turbine stage and then the second pressure turbine stage;wherein the operating step includesobtaining steam from a reactor plant configured to produce a hydrogen-containing substance from a carbon-containing energy-carrier flow;driving the steam turbine with the steam;overheating the steam after it exits the third pressure turbine stage; and supplying said overheated steam to the second pressure turbine stage.2. The method according to claim 2 , further including the reactor plant producing methanol and/or ammonia.3. The method according to claim 16 , further including generating synthesis gas in a synthesis gas section of the reactor plant.4. The method according to claim 3 , wherein the step of generating the synthesis gas ...

Rankine-cycle power-generating apparatus

Specific operation is executable in a Rankine-cycle power-generating apparatus. In the Rankine-cycle power-generating apparatus, a) in the specific operation, the control device adjusts the degree of opening of the opening/closing device so that the direct-current electric power absorbed by the electric power absorber approaches first electric power, or b) in the specific operation, the degree of opening of the opening/closing device is increased to the predetermined intermediate degree of opening so that the direct-current electric power absorbed by the electric power absorber falls within a predetermined range.

AUTOMATED MAXIMUM SUSTAINED RATE SYSTEM AND METHOD

In the context of electric power generation facilities, a system and method that enable control of maximum sustained rate of change in output to accommodate changing load conditions and to facilitate efficient use of system resources are disclosed. In accordance with aspects of the disclosed subject matter, a ramp rate for an electric generator source may be set, operating parameters may be monitored, rates of change or discrepancies of the operating parameters over time may be computed; and output signals may then be used selectively to control certain system components. 1. A method comprising:setting a ramp rate for an electric source;monitoring operating parameters at components of the source including one or more of a boiler, a steam turbine, an electric generator, and a stack;computing rates of change or discrepancies of the operating parameters over time; andproviding output signals as a result of said monitoring and said computing selectively to control one of the boiler, the turbine, or the generator.2. The method of wherein the operating parameters include throttle pressure at the boiler claim 1 , first stage metal temperature at the turbine claim 1 , megawatt error at the generator claim 1 , and opacity at the stack.3. The method of wherein said providing output signals comprises selectively transmitting the output signals to ones of the boiler claim 2 , turbine claim 2 , generator claim 2 , and stack to control the operating parameters.4. The method of wherein said setting a ramp rate comprises utilizing the output signals selectively to vary the ramp rate based on the operating parameters.5. The method of wherein said setting a ramp rate further comprises utilizing input from a distributed control system component remote from the electric source.6. The method of wherein said setting a ramp rate further comprises utilizing input from a solar generator source having a solar unit controller in communication with the distributed control system component.7. ...

METHODS AND APPARATUS FOR POWER RECOVERY IN FLUID CATALYTIC CRACKING SYSTEMS

A co-generation process for a regenerator in an FCC system having a reactor and a regenerator includes the steps of introducing flue gas from the regenerator into a heating unit at a first location of the heating unit, and introducing an oxygen/fuel gas mixture into the heating unit at a second location of the heating unit apart from the first location, and combusting the oxygen/fuel gas mixture in the heating unit at the second location to form a hot combustion gas. The process further includes the steps of combining the hot combustion gas and the flue gas at a third location of the heating unit apart from the first location to produce heated flue gas, heating water and/or steam with the heated flue gas to produce a heated steam, and introducing the heated steam into a turbine to extract energy from the heated steam. 1. A co-generation process for a regenerator in a fluidized catalytic cracking (FCC) system having a reactor and a regenerator , the process comprising the steps of:introducing flue gas from the regenerator into a heating unit at a first location of the heating unit, and introducing an oxygen/fuel gas mixture into the heating unit at a second location of the heating unit apart from the first location;combusting the oxygen/fuel gas mixture in the heating unit at the second location to form a hot combustion gas;combining the hot combustion gas and the flue gas at a third location of the heating unit apart from the first location to produce heated flue gas;heating water and/or steam with the heated flue gas to produce a heated steam; andintroducing the heated steam into a turbine to extract energy from the heated steam.2. The process of claim 1 , wherein introducing the oxygen/fuel gas mixture comprises introducing an air/fuel gas mixture.3. The process of claim 1 , further comprising expanding the heated flue gas prior to the step of heating the water and/or the stream with the heated flue gas.4. The process of claim 1 , wherein combining the hot ...

EXHAUST HEAT RECOVERY APPARATUS, HEATING SYSTEM, STEAM BOILER, AND DEODORIZATION SYSTEM

An exhaust heat recovery apparatus includes an exhaust heat passage through which a first heat medium holding exhaust heat flows; a second heat medium passage through which the second heat medium, of which temperature is lower than that of the first heat medium, flows; a Rankine cycle which includes a pump, an evaporator, an expander, and a condenser and causes heat exchange at the evaporator between the first heat medium flowing through the exhaust heat passage and a working fluid, so that the working fluid is evaporated, the evaporated working fluid expands at the expander, and power is generated; and an exhaust heat recovery heat exchanger which causes heat exchange between the first heat medium flowing through the exhaust heat passage and the second heat medium flowing through the second heat medium passage, so that the second heat medium is heated and exhaust heat of the first heat medium is recovered. 1. An exhaust heat recovery apparatus comprising:an exhaust heat passage through which a first heat medium holding exhaust heat flows;a second heat medium passage through which a second heat medium flows, a temperature of the second heat medium being lower than that of the first heat medium;a Rankine cycle which includes a pump, an evaporator, an expander, and a condenser, and which causes heat exchange to be performed at the evaporator between the first heat medium flowing through the exhaust heat passage and a working fluid, so that the working fluid is evaporated, the evaporated working fluid expands at the expander, and power is generated; andan exhaust heat recovery heat exchanger which causes heat exchange to be performed between the first heat medium flowing through the exhaust heat passage and the second heat medium flowing through the second heat medium passage, so that the second heat medium is heated and the exhaust heat held by the first heat medium is recovered.2. The exhaust heat recovery apparatus according to claim 1 , wherein the second heat ...

System and Method for Airborne Atmospheric Water Generation

The invention is a system and method for the airborne generation of usable water from atmospheric water vapor and the generation of electric power from and for such system. 1. A system for airborne atmospheric water generation , comprising an airborne platform connected to a land-based platform , wherein the airborne platform comprises air fans to intake moist atmospheric air , a dehumidifier condenses water from vapor and drains the condensed water to the land-based platform and exhaust air fans to vent dehumidified air back into the atmosphere , and wherein the land-based platform comprises a water turbine and generator for generating power for all electrical components of the system , a collection tank for accumulating condensed water , and an external holding tank.2. The system of claim 1 , further comprising wherein the condensed water is drained to the land-based platform using a drainage tube comprising a nozzle focused on the water turbine and wherein the water turbine is an impact turbine.3. The system of claim 1 , further comprising wherein the condensed water is drained to the land-based platform using a drainage tube emptying into a turbine basin claim 1 , wherein the water turbine is a reaction turbine and fully submerged when operating.4. The system of claim 1 , further comprising wherein the collection tank comprises a water pump for moving water from the collection tank to the holding tank claim 1 , such water pump powered by electricity from the generator.5. The system of claim 1 , wherein a power line from the generator connects to an amplifier in the airborne platform claim 1 , then extends to one or more capacitors claim 1 , which capacitor(s) are each connected to one or more air fans.6. The system of claim 1 , wherein the airborne platform elevates via one or more levitation bladders containing a gas lighter than air.7. The system of claim 6 , wherein the levitation bladder(s) is one or more hot air balloons claim 6 , from which the airborne ...

STEAM POWER PLANT WITH AN ADDITIONAL FLEXIBLE SOLAR SYSTEM FOR THE FLEXIBLE INTEGRATION OF SOLAR ENERGY

A thermal power plant is described comprising a solar collector field and a heat storage to allow the use of the thermal energy collected by the solar field with a time delay for the production of electricity in the steam power plant. 1. A steam power plant comprisinga steam generator, a turbine, a condenser, a feed water container, a condensate line at least one low-pressure preheater and at least one high-pressure preheater,wherein the condensate line connects the condenser, the preheaters and the feed water container with each other, and a flexible solar system mounted parallel to the condensate line.2. The steam power plant according to claim 1 ,wherein the flexible solar system comprises a heat storage and a field of solar collectors.3. The steam power plant according to claim 2 ,wherein the solar collectors is concentrating and/or non-concentrating.4. The steam power plant according to claim 1 , wherein the flexible solar system is mounted parallel to one or more of the low pressure preheaters.5. The steam power plant according to claim 1 , wherein the flexible solar system is mounted parallel to one or more of the high pressure preheaters.6. The steam power plant according to claim 1 , wherein the flexible solar system comprises a ductwork and a plurality of valves and a plurality of pumps that flexibly allow to bypass one or more of the preheaters depending on temperature of the thermal energy delivered by the flexible solar system.7. The steam power plant according to claim 1 , wherein the flexible solar system delivers thermal energy from the solar field and the heat storage simultaneously to the condensate line.8. The steam power plant according to claim 1 ,wherein the flexible solar system delivers thermal energy from the solar field and the heat storage simultaneously to the condensate line at different temperatures to different preheaters.9. The steam power plant according to claim 1 , wherein the flexible solar system is directly connected to the ...

NUCLEAR-POWERED TURBINE ENGINE

A turbine engine comprising a compressor section and a turbine section in serial flow arrangement defining a working air flow path with a heat exchanger in fluid communication the working air flow path, and a nuclear fuel in thermal communication with the heat exchanger and a release valve in fluid communication with the working air flow path. 1. A turbine engine comprising:a compressor section, and turbine section in serial flow arrangement to define a working air flow path;a heat exchanger in fluid communication with the working air flow path;a nuclear fuel in thermal communication with the working air flow path; andan air release valve in fluid communication with the working air flow path between the compressor section and the turbine section.2. The turbine engine of wherein the nuclear is provided within the heat exchanger.3. The turbine engine of wherein the nuclear fuel is at least one of W181 or Ta182.4. The turbine engine of wherein the nuclear fuel primarily decays through alpha or beta decay.5. The turbine engine of wherein there are multiple heat exchangers where each is in thermal communication with different types of the nuclear fuel.6. The turbine engine of wherein the different types of the nuclear fuel have different half-lives.7. The turbine engine of wherein the turbine section comprises a high-pressure turbine and a low-pressure turbine claim 1 , and the air release valve comprises at least one of a high-pressure air release valve located upstream of the high-pressure turbine or a low-pressure air release valve located upstream of the low-pressure turbine.8. The turbine engine of wherein the air release valve comprises at least both the high-pressure release valve and the low-pressure release valve.9. The turbine engine of wherein the nuclear fuel is provided within the heat exchanger.10. The turbine engine of wherein the nuclear fuel is at least one of W181 or Ta182.11. The turbine engine of further comprising a combustor section in the working ...

SYSTEM AND METHOD FOR PROVIDING SUPERCRITICAL STEAM

A system for providing supercritical steam including a first boiler that generates steam via combusting a first fuel, and a second boiler fluidly connected to the first boiler via a conduit which heats the generated steam to supercritical steam temperatures via combusting a second fuel. A first temperature of the conduit may be below a critical corrosion temperature and a second temperature of the conduit is greater than or equal to the critical corrosion temperature. A combined carbon emission rate of the first boiler and the second boiler may be less than a combined carbon emission rate of generating and heating the steam to supercritical steam temperatures using boilers that only combust the first fuel. The first boiler may be fluidly connected to a heat exchanger that heats the generated steam to a supercritical steam temperature via a flue gas produced by a gas turbine. 1. A system for providing supercritical steam comprising:a first boiler that generates steam via combusting a first fuel;a second boiler fluidly connected to the first boiler via a conduit such that the generated steam flows from the first boiler to the second boiler which heats the generated steam to a supercritical steam temperature via combusting a second fuel that is different from the first fuel; andwherein a first temperature of the conduit is below a critical corrosion temperature at which contaminants produced by combusting the first fuel corrode the conduit and a second temperature of the conduit is greater than or equal to the critical corrosion temperature.2. The system of claim 1 , wherein the first fuel is at least one of a heavy oil residue claim 1 , a heavy fuel oil claim 1 , and a solid fuel.3. The system of claim 1 , wherein at least one of the first boiler and the second boiler is an air-fired boiler or an oxy-fired boiler.4. The system of claim 1 , wherein the second fuel is a gas or a combination of a gas blended with at least one of a liquid fuel or a solid fuel.5. The ...

FUEL HEATING SYSTEM USING STEAM AND WATER IN SINGLE FUEL HEAT EXCHANGER

A fuel heating system for a gas turbine system is provided. The system includes a boiler for generating steam, a HRSG independent of the boiler, and a single fuel heat exchanger structured to operate using steam or water as the heating medium. A control valve system selectively delivers the heating medium to the second passage of the single fuel heat exchanger as one of: the steam from the boiler and the hot feedwater from the HRSG. 1. A fuel heating system for a gas turbine system , the fuel heating system comprising:a boiler for generating steam;a heat recovery steam generator (HRSG) independent of the boiler;a single fuel heat exchanger including a first passage for fluidly communicating a fuel therethrough and a second passage in thermal communication with the first passage for fluidly communicating a heating medium therethrough to heat the fuel, the single heat exchanger structured to operate using steam or water as the heating medium; anda control valve system fluidly interconnecting the HRSG, the boiler and the single fuel heat exchanger and configured to selectively deliver the heating medium to the second passage of the single fuel heat exchanger as one of: the steam from the boiler and the hot feedwater from the HRSG.2. The fuel heating system of claim 1 , wherein the single fuel heat exchanger includes a printed circuit heat exchanger (PCHE).3. The fuel heating system of claim 1 , further comprising a condensate return passage fluidly communicating condensate from the single fuel heat exchanger from the steam to the boiler.4. The fuel heating system of claim 1 , wherein the HRSG is operatively coupled to the gas turbine system.5. The fuel heating system of claim 4 , further comprising a return passage fluidly communicating the hot feedwater from the single fuel heat exchanger to a boiler for a steam turbine system.6. The fuel heating system of claim 1 , wherein the control valve system includes:at least one control valve configured to control flow of the ...

ULTRA EFFICIENT TURBO-COMPRESSION COOLING SYSTEMS

Aspects of the present disclosure include a system for turbo-compression cooling. The system may be aboard a marine vessel. The system includes a power cycle and a cooling cycle. The power cycle includes a first working fluid, a waste heat boiler configured to evaporate the working fluid, a turbine, and a condenser. The condenser condenses the working fluid to a saturated or subcooled liquid. The cooling cycle includes a second working fluid, a first compressor configured to increase the pressure of the second working fluid, a condenser configured to condense the second working fluid to a saturated or subcooled liquid after exiting the first compressor, an expansion valve, and an evaporator. The turbine and first compressor are coupled one to the other. The waste heat boiler receives waste heat from engine jacket water and lubricating oil from a ship service generator. The evaporator cools water in a shipboard cooling loop. 1. A system for turbo-compression cooling in a facility having a cooling loop and a generator having a plurality of waste heat streams , the system comprising: a first working fluid;', 'a waste heat boiler configured to evaporate the working fluid, the waste heat boiler configured to receive waste heat from one or more of the plurality of waste heat streams from the generator;', 'a turbine configured to receive the evaporated first working fluid from the waste heat boiler, the turbine having a plurality of vanes disposed around a central shaft and configured to rotate about the central shaft, the plurality of vanes configured to rotate as the first working fluid expands to a lower pressure; and', 'a condenser configured to receive the first working fluid from the turbine and configured to condense the first working fluid to a saturated or subcooled liquid;, 'a power cycle comprising a second working fluid;', 'a first compressor configured to increase the pressure of the second working fluid;', 'a condenser configured to receive the second working ...

Water Driven Turbine Steam Engine

A closed loop steam engine that transfers its motive power to a flow of water using a steam injector. The resulting water jet then drives a turbine, is cooled in a heat exchanger to extract useful heat and then return to the steam injector water inlet. Part of the flow of water is reused as feed water to the boiler. 1. A heat engine , comprising:a boiler,a gas-into-liquid injector, wherein the boiler is configured to direct a flow of gas to the gas inlet of the injector and the injector is configured to direct part of the resulting flow of liquid to the inlet of the boiler,a turbine, wherein the injector is configured to direct part of the propelled flow of liquid to the inlet of the turbine,a heat exchanger, wherein the turbine is configured to direct its outflow of liquid to the heat exchanger and the heat exchanger is configured to direct its outflow of the liquid to the liquid inlet of the injector.2. The engine of further comprising a control valve claim 1 , wherein the injector is configured to instead of directing part of the flow of liquid to the boiler to direct that flow of liquid to the control valve and the control valve is configured to direct a flow of liquid to the inlet of the boiler claim 1 , the control valve also controlling the amount of liquid flowing into the boiler.3. The engine of further comprising a pump claim 1 , wherein the injector is configured to instead of directing part of the flow of liquid to the boiler to direct that flow to the pump and the pump is configured to direct a flow of liquid to the inlet of the boiler claim 1 , the pump also increasing the flow of the liquid flowing to the boiler claim 1 , the pump also regulating the flow of liquid to the boiler.4. The engine of further comprising a bypass claim 1 , wherein the injector is configured to direct an additional part of the flow of liquid from the outlet of the injector back to the inlet of the injector.5. The engine of further comprising a bypass claim 2 , wherein the ...

HEAT CYCLE SYSTEM

A heat cycle system includes a cooling circuit and a Rankine cycle circuit in which an organic medium circulates. The Rankine cycle circuit includes an evaporator, an expander, and a condenser. Before warm-up of an engine, a control device executes a warm-up mode in which the organic medium is circulated through the condenser, the expander and the evaporator in sequence; after the warm-up of the engine, the control device executes a waste heat recovery mode in which the organic medium is circulated through the evaporator, the expander and the condenser in sequence. In the warm-up mode, by supplying energy to the expander, the control device compresses the organic medium passing through the condenser and supplies the compressed organic medium to the evaporator; in the waste heat recovery mode, by depressurizing the organic medium passing through the evaporator by the expander, the control device recovers the energy generated by the expander. 1. A heat cycle system , comprising:a cooling circuit in which cooling water performing heat exchange with an internal combustion engine and exhaust of the internal combustion engine circulates; a first heat exchanger performing heat exchange between an organic medium having a lower boiling point than the cooling water and the cooling water of the cooling circuit,', 'an expander depressurizing the organic medium passing through the first heat exchanger and generating energy, and', 'a second heat exchanger performing heat exchange between the organic medium and outside air; and, 'a Rankine cycle circuit, comprisinga control device operating the Rankine cycle circuit in a warm-up mode in which the organic medium is circulated through the second heat exchanger, the expander, and the first heat exchanger in this order before warm-up of the internal combustion engine, and operating the Rankine cycle circuit in a waste heat recovery mode in which the organic medium is circulated through the first heat exchanger, the expander, and the ...

STEAM POWER PLANT WITH A SECOND LOW-PRESSURE TURBINE AND AN ADDITIONAL CONDENSING SYSTEM

A steam power plant with a low-pressure turbine is suggested with a second low-pressure turbine on a separated shaft line including a separate generator. The second low-pressure turbine is connected to an additional condensing system without cooling water consumption, thus allowing to maintain the power output at a high level, even if the main condensing system has a reduced capacity due to cooling water restrictions. 1. A steam power plant comprising at least one steam turbine comprising a low-pressure turbine and a main condensing system , a second low-pressure turbine and a second condensing system.2. The steam power plant according to claim 1 , wherein the second condensing system is of evaporative cooling claim 1 , non-evaporative cooling and/or once through cooling type.3. The steam power plant according to wherein the at least one steam turbine further comprises a high-pressure turbine and an intermediate-pressure turbine wherein the intermediate-pressure turbine and the first low-pressure turbine are connected by an overflow pipe.4. The steam power plant according to claim 3 , wherein the second low-pressure turbine is connected to the overflow pipe.5. The steam power plant according to claim 4 , wherein the overflow pipe comprises a branch piece.6. The steam power plant according to claim 5 , wherein between the branch piece and the first low-pressure turbine a first steam valve is installed.7. The steam power plant according to claim 5 , wherein between the branch piece and the second low-pressure turbine a second steam valve is installed.8. The steam power plant according to claim 1 , wherein the second condensing system comprises a fan. This application claims priority to European application 13153986.8 filed Feb. 5, 2013, the content of which is relied upon and incorporated herein by reference in its entirety.The claimed invention is related to a steam power plant including at least one steam turbine connected to a (main) condensing system.Steam power ...

WASTE HEAT RECOVERY WITH ACTIVE COOLANT PRESSURE CONTROL SYSTEM

A waste heat recovery (WHR) and coolant system with active coolant pressure control includes an engine cooling system, a WHR system, and a coolant pressure control system. A coolant heat exchanger positioned along each of the engine cooling and working fluid circuits, and is structured to transfer heat from the coolant fluid to the working fluid. The coolant pressure control system includes a pressure line operatively coupled to an air brake system and to the coolant tank. A valve is coupled to the pressure line upstream of the coolant tank. A coolant pressure controller is in operative communication with each of the valve, an air pressure sensor, and a coolant temperature sensor. The coolant pressure controller is structured to determine a target coolant pressure based on a coolant temperature and control a valve position of the valve so as to cause the air pressure to approach the target coolant pressure. 1. A system , comprising: a coolant tank,', 'an engine cooling circuit in coolant fluid receiving communication with the coolant tank, the engine cooling circuit comprising a first pump structured to circulate the coolant fluid through the engine cooling circuit,', 'a coolant heat exchanger positioned along the engine cooling circuit, and', 'a first temperature sensor positioned along the engine cooling circuit, the first temperature sensor structured to provide a coolant temperature value of the coolant fluid flowing through the engine cooling circuit;, 'an engine cooling system, comprising a working fluid circuit comprising a second pump structured to circulate a working fluid through the working fluid circuit, and', 'the coolant heat exchanger positioned along the working fluid circuit and structured to transfer heat from the coolant fluid to the working fluid; and, 'a waste heat recovery system, comprising a pressure line operatively coupled to a pressure source and to the coolant tank,', 'a valve operatively coupled to the pressure line upstream of the ...

COMBINED CYCLE PLANT AND PLANT BUILDING THEREOF

A plant building includes: a building main body that continues in an array direction in which a plurality of single-shaft combined units are arrayed, and has a roof that covers the upper side of the plurality of single-shaft combined units; a first overhead crane that is disposed inside the building main body, and has a girder capable of traveling in the array direction across a region including the upper side of gas turbines of the plurality of single-shaft combined units; and a second overhead crane that is disposed inside the building main body, and has a girder capable of traveling in the array direction across a region including the upper side of steam turbines of the plurality of single-shaft combined units. 1. A plant building of a combined cycle plant that includes a plurality of single-shaft combined units each having a gas turbine , a generator , and a steam turbine disposed on the same axis , the axes of the plurality of single-shaft combined units being parallel to one another , the plant building comprising:a building main body having a roof that continues in an array direction in which the plurality of single-shaft combined units are arrayed and covers the upper side of the plurality of single-shaft combined units;a first overhead crane that is disposed inside the building main body, and has a girder capable of traveling in the array direction across a region including the upper side of the gas turbines of the plurality of single-shaft combined units; anda second overhead crane that is disposed inside the building main body, and has a girder capable of traveling in the array direction across a region including the upper side of the steam turbines of the plurality of single-shaft combined units.2. The plant building according to claim 1 , whereinthe first overhead crane and the second overhead crane each have a pair of travel rails that are parallel to each other and extend in the array direction, andthe girders are respectively supported by the pairs ...

Energy collector system applicable to combustion engines

Disclosed is an energy collector system applicable to internal combustion engines. It may include: a) a collector of thermal energy from the exhaust gases; b) a thermal tank covered by helical tubes to gain heat by the exhaust gases; c) a heat exchanger; and d) an outer element capable of converting thermal energy into mechanical energy, such as a closed Brayton cycle turbine, a Stirling engine, a Rankine turbine or an open loop air motor for converting mechanical energy (coupling the difference in rpm) into electrical energy with an electrical generator. The thermal energy collector may be composed of a heat exchanger that collects energy from the exhaust gases. The electrical energy generated may be used for driving a hybrid vehicle. The thermal tank is capable of storing energy as heat, as well.

Pipeline connection system for steam turbine and boiler combination

Disclosed is a pipeline connection system for a steam turbine and boiler combination that includes a boiler including a boiler heating surface and a boiler outlet header, a high-level steam turbine, and a pipeline system connected between the boiler outlet header and the high-level steam turbine. The boiler outlet header is arranged adjacent to the high-level steam turbine, and a boiler external section of pipe bundle of a pipe bank of the boiler heating surface that is connected to the boiler outlet header is arranged as an L shape comprising a horizontal section of pipe bundle and a vertical section of pipe bundle.

HEAT RECOVERY AND UPGRADING METHOD AND COMPRESSOR FOR USING IN SAID METHOD

A heat recovery and upgrading method includes cycles of the subsequent steps of providing a working fluid including a liquid phase in a working fluid stream; transferring heat to the working fluid stream to partially evaporate working fluid in liquid phase to obtain a two-phase working fluid stream in liquid phase and gas phase; compressing the two-phase working fluid stream so as to increase a temperature and pressure of the working fluid and to evaporate working fluid in liquid phase; and transferring heat from the working fluid stream by element of condensation of working fluid. In the first step he working fluid is preferably in a predominantly single-phase working fluid stream in liquid phase when heat is transferred to the working fluid. In the third step working fluid in liquid phase is preferably evaporated so that a two-phase working fluid stream is maintained, especially a wet gas-phase working fluid. 1. heat recovery and upgrading method comprising cycles of the subsequent steps of{'b': '11', 'a.—providing a working fluid comprising a liquid phase in a working fluid stream ();'}{'b': 20', '11', '12, 'b.—transferring heat () to the working fluid stream () such as to partially evaporate working fluid in liquid phase to obtain a two-phase working fluid stream () in liquid phase and gas phase;'}{'b': 30', '12, 'c.—compressing () the two-phase working fluid stream () so as to increase a temperature and pressure of the working fluid and to evaporate working fluid in liquid phase; and'}{'b': 40', '60', '13', '14', '15, 'd.—transferring heat (, ) from the working fluid stream (, , ) by means of condensation of working fluid.'}211. The method according to claim 1 , wherein step a comprises providing the working fluid in a predominantly single-phase working fluid stream () in liquid phase.313. The method according to claim 1 , wherein step c comprises compressing working fluid to evaporate working fluid in liquid phase such that a two-phase working fluid stream () ...

Power Generation System and Power Generation Method

In order to enhance the tracking performance of power generation equipment with respect to a load variation and increase the reliability of the power generation equipment, a dynamic characteristic model simulating the dynamic characteristics of a multi-shaft gas turbine is used to calculate an output prediction value of a first power generator in a case where a combustor is controlled so as to match the output of the first power generator to an output target value; on the basis of the output target value and the output prediction value of the first power generator, a first power generator output instruction value as an instruction value for the output from the first power generator to a power system and a second power generator output instruction value as an instruction value for the output from a second power generator to the power system are calculated; and the combustor is controlled on the basis of the first power generator output instruction value and a frequency convertor is controlled on the basis of the second power generator output instruction value. 1. A power generation system comprising: a high pressure turbine shaft,', 'a compressor which generates compressed air according to rotation of the high pressure turbine shaft,', 'a combustor which generates a combustion gas by mixing and burning the compressed air and fuel,', 'a high pressure turbine which rotates by receiving the combustion gas and drives the high pressure turbine shaft,', 'a low pressure turbine shaft, and', 'a low pressure turbine which rotates by receiving a gas discharged from the high pressure turbine and drives the low pressure turbine shaft;, 'a multi-shaft gas turbine that includes'}a first power generator that is connected to a power system, generates power using the rotation of the low pressure turbine shaft, and outputs the generated power to the power system;a second power generator that accelerates or decelerates the high pressure turbine shaft according to input or output of ...

POWER SYSTEMS AND METHODS CONFIGURING AND USING SAME

Systems and methods based on the systems to convert a portion of thermal energy into to mechanical and/or electrical energy including a power generation subsystem (PGSS) comprising a vaporization and power generation subsystem (VPSS) including a heat recovery vapor generator (HRVG) and a turbine T a heating and cooling subsystem (HCSS) including three parallel configured heat exchange units HE HE and HE a single heat exchange unit HE and a first separator SP and a condensing subsystem (CSS) including a final condenser HEfrom a heat source subsystem (HSSS) including a heat source producing an initial heat source stream. 1. A process for generating power from a heat source stream comprising:{'b': 1', '3', '4', '5', '2', '1', '1, 'i': 'b', 'providing a heat source stream to a power generation subsystem (PGSS) comprising a vaporization and power generation subsystem (VPSS) including a heat recovery vapor generator (HRVG) and a turbine T, a heating and cooling subsystem (HCSS) including three parallel configured heat exchange units HE, HE, and HE, a single heat exchange unit HE, and a first separator SP, and a condensing subsystem (CSS) including a final condenser HEfrom a heat source subsystem (HSSS) including a heat source producing an initial heat source stream,'}{'b': '1', 'vaporizing and superheating a working solution stream in the HRVG using heat from the initial heat source stream to form a vaporized and superheated working solution stream and converting a portion of the heat associated with the vaporized and superheated working solution stream in the turbine T into a usable form of energy comprising mechanical and/or electrical energy in the VPSS producing a spent working solution stream,'}heating, cooling, separating, and combining streams derived from the spent working fluid stream to optimize utilization of residual heat in the spent working fluid stream in the heating and cooling subsystem HCSS to produce a condensing stream, andcondensing the condensing ...

AIR START STEAM ENGINE

A method and system using at least two different working fluids to be supplied to an expander to cause it to do mechanical work. The expander is started by providing a compressed gaseous working fluid at a sufficient pressure to the expander. At the same time the compressed gaseous working fluid is provided to the expander, a second working fluid that is liquid at ambient temperatures is provided to a heater to be heated. The second working fluid is heated to its boiling point and converted to pressurized gas Once the pressure is increased to a sufficient level, the second working fluid is injected into the expander to generate power, and the supply of the first working fluid may be stopped. After expansion in the expander, the working fluids are is exhausted from the expander, and the second working fluid may be condensed for separation from the first working fluid. Control circuitry controls the admission of the first and second working fluids responsive to monitoring the load on the expander. 1. A combined cooling , heating , and power generation unit comprising:a first vessel holding a quantity of a first pressurized gaseous working fluid that is gaseous at ambient temperature, being pressurized to a pressure substantially greater than ambient pressure;a second vessel holding a quantity of a second working fluid that is in a liquid state at ambient temperature;a controllable heater in controllable communication with at least said second vessel for heating at least said second working fluid;an expander in controllable communication with said heater and said first vessel, such that said expander can receive said first pressurized gaseous working fluid and/or receive said second working fluid, having been heated by said heater to be vaporized and form a second pressurized gaseous working fluid, said first and/or second pressurized gaseous working fluids being supplied to at least one chamber in said expander where said pressurized gaseous working fluids can expand, ...

EXHAUST STEAM WASTE HEAT RECOVERING AND SUPPLYING SYSTEM OF AIR-COOLING UNITS IN LARGE THERMAL POWER PLANTS

The present application relates to an exhaust steam waste heat recovering and supplying system used for air-cooling units in large thermal power plants. Each of the two steam turbines has independent exhaust steam extraction system, and the exhaust steam extraction system of each steam turbine is connected with corresponding pre-condenser to heat the return water of the heating network. The exhaust steam extraction system of each steam turbine is further connected with the corresponding steam ejector; the exhaust port of each steam is connected with the corresponding steam ejector condenser to heat the return water of the heating network. The exhaust steam waste heat of the air-cooling units in a thermal power plant can be recycled in high efficiency to improve the utility rate of the exhaust steam, increase heating capacity, reduce cold end loss to the largest extent, and maximize the energy saving benefits. 1. An exhaust steam waste heat recovering and supplying system used for air-cooling units in large thermal power plants , in which the air-cooling units in large thermal power plants comprises a first steam turbine and a second steam turbine and the corresponding condensing devices thereof , and the first steam turbine and the second steam turbine respectively have a first turbine low-pressure cylinder and a second turbine low-pressure cylinder , each of which is connected with the corresponding condensing device thereof via an exhaust pipe; wherein the exhaust steam waste heat recovering and supplying system comprises:a first exhaust steam extraction system and a second exhaust steam extraction system and corresponding first and second steam ejectors, pre-condensers, and steam ejector condensers thereof, in which the turbine exhaust steam is extracted by using an exhaust steam extraction system;each of the two steam turbines has its own independent exhaust steam extraction system, in which the exhaust steam extraction system of each steam turbine is connected ...

RANKINE CYCLE PLANT AND PROCESS FOR THE REGASIFICATION OF LIQUEFIED GAS

A Rankine cycle plant for the regasification of liquefied gas, includes: a Rankine closed loop system; a source of liquefied gas at a cryogenic temperature operatively coupled to a condenser to receive heat from a working fluid from an expansion turbine to take the liquefied gas to the gaseous state; a source of a heating fluid at a temperature higher than the cryogenic temperature operatively coupled to an evaporator to transfer heat to the working fluid coming from the condenser. The expansion turbine is radial centrifugal with at least one auxiliary outlet interposed between successive stages. The condenser is multilevel and has at least two condensing chambers, wherein a lower chamber being connected to an outflow opening of the expansion turbine and an upper chamber connected to the auxiliary outlet of the expansion turbine. 1. Rankine cycle plant for the regasification of liquefied gas , comprising: one evaporator; Подробнее

TURBINE CONDENSER FOR A STEAM TURBINE

A turbine condenser includes an area with condenser tubes for liquefying waste steam from the steam turbine, a chamber formed by condenser walls for receiving the waste steam, and a diverted steam channelling system for channelling diverted steam into the chamber in the turbine condenser, wherein the diverted steam channelling system includes an annular nozzle extending into the turbine condenser, the outlet end of which has an uneven edge. 1. A turbine condenser for a steam turbine , comprising:a region with condenser tubes for the liquefaction of exhaust steam from the steam turbine, having a chamber, formed by condenser walls, for receiving the exhaust steam, and having a bypass-steam introduction device for introducing bypass steam into said chamber of the turbine condenser,wherein the bypass-steam introduction device comprises a ring-shaped nozzle which extends into the turbine condenser, and the outlet end of which has a non-uniform edge.2. The turbine condenser as claimed in claim 1 ,wherein the edge is in the form of a serrated or toothed outlet edge.3. The turbine condenser as claimed in claim 2 ,wherein the edge has serrations or teeth distributed uniformly over the circumference.4. The turbine condenser as claimed in claim 3 ,wherein the serrations or teeth of the edge are at least partially inclined in the axial direction of the nozzle. This application is the US National Stage of International Application No. PCT/EP2014/065349 filed Jul. 17, 2014, and claims the benefit thereof. The International Application claims the benefit of European Application No. EP13178234 filed Jul. 26, 2013. All of the applications are incorporated by reference herein in their entirety.The invention relates to a turbine condenser for a steam turbine.Turbine condensers serve for the liquefaction of the exhaust steam of steam turbines. In the case of installations with combined gas and steam turbines, to be able to cover peak loads in energy demand, such installations are ...

EXHAUST CHAMBER COOLING APPARATUS AND STEAM TURBINE POWER GENERATING FACILITY

In one embodiment, an exhaust chamber cooling apparatus measures output of a generator driven by a steam turbine, a temperature in an exhaust chamber of the turbine, and a pressure in a condenser that changes steam from the turbine back to water. The apparatus further outputs a first signal when it is detected that a measurement value of the output is larger than a first setting value and a measurement value of the temperature is larger than a second setting value, and a second signal when it is detected that the measurement value of the output is smaller than the first setting value and a measurement value of the pressure or a calculation value obtained from the measurement value of the pressure is larger than a third setting value. The apparatus further controls supply of a cooling fluid into the chamber, based on the first or second signal. 1. An exhaust chamber cooling apparatus comprising:an output measuring module configured to measure output of a generator driven by a steam turbine;a temperature measuring module configured to measure a temperature in an exhaust chamber of the steam turbine;a pressure measuring module configured to measure a pressure in a condenser that changes steam from the steam turbine back to water;a first signal outputting module configured to output a first signal when it is detected that a measurement value of the output is larger than a first setting value and a measurement value of the temperature is larger than a second setting value;a second signal outputting module configured to output a second signal when it is detected that the measurement value of the output is smaller than the first setting value and a measurement value of the pressure or a calculation value obtained from the measurement value of the pressure is larger than a third setting value; anda controller configured to control supply of a cooling fluid into the exhaust chamber, based on the first or second signal.2. The apparatus of claim 1 , wherein the controller ...

OXYFUEL POWER PLANT PROCESS

An oxyfuel power plant having improved efficiency of operation by the provision of at least two condensation units, the first being a warmer operating direct contact cooler and the second being a colder operating direct contact cooler. Each apparatus is loaded with a different quantity of water, with the warmer direct contact cooler having two to three times the amount of water that is in the colder direct contact cooler. 1. An oxyfuel power plant system comprising:at least two condensation units for condensing water out of a flue gas emitted from a boiler of the oxyfuel power plant system,wherein the at least two condensation units are direct contact coolers andwherein a first direct contact cooler is operated at a warmer temperature in comparison to a second direct contact cooler.2. (canceled)3. The system as claimed in claim 1 , wherein the direct contact coolers are loaded with a different quantity of coolant.4. The system as claimed in claim 3 , wherein the first direct contact cooler is loaded with two to three times the amount of coolant compared to the second direct contact cooler.5. The system as claimed in claim 4 , wherein the direct contact coolers contain fillings or structured packings.6. The system as claimed in claim 5 , wherein the fillings or structured packings are made of ceramic or metal.7. The system as claimed in claim 6 , wherein the second direct contact cooler is stacked on top of the first direct contact cooler.8. A method of operating an oxyfuel power plant system comprising condensing water from a flue gas emitted from a boiler of the oxyfuel power plant system in at least two condensation units claim 6 ,wherein the at least two condensation units are direct contact coolers andwherein a first direct contact cooler is operated at a warmer temperature in comparison to a second direct contact cooler.9. The method as claimed in claim 8 , wherein the direct contact coolers are loaded with a different quantity of coolant.10. The method as ...

Steam generator turbine

A turbine-generator system that uses high pressure steam to turn a turbine connected to a power generator. High pressure steam is generated by a continuous flow of pressurized water. The pressure steam generator can be configured as a separate unit, or as a part of the turbine. Steam is applied to the turbine from one high pressure steam unit through at least one nozzle, applying the steam against the turbine blades.

SELF-OPERATED INCINERATOR SYSTEM

A self-operated incinerator system is disclosed. The self-operated incinerator system comprises: an incinerator; a steam boiler configured to receive waste heat from the incinerator so as to produce steam; a turbine device configured to generate a turbine rotational force by receiving the steam produced by the steam boiler; a generator configured to generate power by using the turbine rotational force generated by the turbine device; and a storage battery configured to store the power generated by the generator and to use the power for starting or normally operating at least one from among the incinerator and the steam boiler. 1. A self-operated incinerator system comprising:an incinerator;a steam boiler configured to receive waste heat from the incinerator so as to produce steam;a turbine device configured to receive the steam produced from the steam boiler to generate a turbine rotational force;a generator configured to generate power by using the turbine rotational force generated by the turbine device; and a storage battery configured to store the power generated by the generator and use the power for starting or normally operating at least one from the incinerator and the steam boiler.2. The self-operated incinerator system of claim 1 , wherein both of starting and normally operating are performed without an external power supply.3. The self-operated incinerator system of claim 2 , wherein each of the incinerator and the steam boiler is configured to start only with a power supplied from the storage battery without the external power supply claim 2 , and normally operate only with a power supplied from at least one of the generator and the storage battery without the external power supply.4. The self-operated incinerator system of claim 2 , wherein the storage battery is configured to be charged only with the power supplied from the generator without the external power supply except for an initial charging before installation.5. The self-operated incinerator ...

COMPRESSION SYSTEM

Provided is a compressor system. The compressor system includes: compressors receiving a first fluid from outside and compressing the first fluid; a motor receiving an electric current from outside to drive the compressors; a gear unit for connecting the compressors to the motor; a turbine generating a driving power from a second fluid that has exchanged heat with the first fluid that is discharged from the compressors; and a connection unit directly connected to the turbine and the gear unit. 1. A compressor system comprising:a compressor receiving a first fluid from outside and compressing the first fluid;a motor receiving an electric current from outside to drive the compressor;a gear unit for connecting the compressor to the motor;a turbine generating a driving power from a second fluid that has exchanged heat with the first fluid that is discharged from the compressor; anda connection unit directly connected to the turbine and the gear unit.2. The compressor system of claim 1 , further comprising a thermal exchanger claim 1 , in which the first fluid discharged from the compressor and the second fluid exchange heat claim 1 , for supplying the second fluid that has exchanged the heat to the turbine.3. The compressor system of claim 2 , wherein a plurality of the compressors and a plurality of thermal exchangers are provided claim 2 , and each of the plurality of thermal exchangers is arranged on a flow path through which the first fluid discharged from each of the plurality of compressors passes.4. The compressor system of claim 2 , further comprising a condenser for condensing the second fluid discharged from the turbine.5. The compressor system of claim 4 , further comprising a pump for supplying the second fluid discharged from the condenser to the thermal exchangers.6. The compressor system of claim 4 , wherein the condenser receives cooling water from outside claim 4 , and condenses the second fluid through heat exchange between the second fluid and the ...

Method to integrate regenerative rankine cycle into combined cycle applications using an integrated heat recovery steam generator

A system is disclosed that incorporates a regenerative Rankine cycle integrated with a conventional combined cycle. This novelty requires minimal changes to a conventionally designed Heat Recovery Steam Generator and uses an added duct firing array(s) to boost the enthalpy of combustion turbine exhaust. The higher enthalpy in said exhaust is then extracted with the co-shared heating elements of the conventionally designed combined cycle to produce high pressure main and reheat steam. In practice, the condensate stream from the condenser is bifurcated such that a separate and dedicated feedwater flow, used for regeneration, is directed to feedwater heaters and then converted to steam with the provided additional enthalpy at the same pressure and temperature as the main steam in the conventional combined cycle. The fractional amount of condensate that is not sent through the feedwater heaters is directed to the HRSG to be heated in conventional fashion. 1. A method for generating electric power that incorporates the use of a regenerative Rankine cycle with a combined cycle , the method comprising the steps of:Bifurcating the condensate from a condenser into two or more separate condensate feed streams whereby the condensate in at least one condensate feed stream is pressurized to feedwater and sent directly to a heat recovery steam generator and the condensate in at least one condensate feed stream is pressurized to feedwater and sent to one or more common heating elements that is co-shared with the first stream first being preheated by a one or more feedwater heaters utilizing extraction steam from an extraction turbine;generating steam in a parallel cycle using a regenerative Rankine cycle and co-mixing said steam with the steam produced in a traditional non-regenerative combined cycle and transferring the steam to an extraction steam turbine having one or more extraction ports;converting the steam into electricity through the use of an extraction steam turbine and ...

Output manifold for heat recovery steam generations

This disclosure provides manifolds, manifold components, and heat recover steam generator systems. An output line of an output manifold is fluidically connected to at least one downstream process. A first collection line is fluidically connected to a plurality of header lines by a first set of header links. A second collection line is fluidically connected to the plurality of header lines by a second set of header links. A connecting junction fluidically connects the first collection line and the second collection line to the output line.

HEAT ENGINE SYSTEM

An improved heat engine is disclosed. The heat engine comprises at least one heat pipe containing a working fluid flowing in a thermal cycle between vapor phase at an evaporator end and liquid phase at a condenser end. Heat pipe configurations for high-efficiency/high-performance heat engines are disclosed. The heat pipe may have an improved capillary structure configuration with characteristic pore sizes between 1μ and 1 nm (e.g. formed through nano- or micro-fabrication techniques) and a continuous or stepwise gradient in pore size along the capillary flow direction. The heat engine may have an improved generator assembly configuration that comprises an expander (e.g. rotary/turbine or reciprocating piston machine) and generator along with magnetic bearings, magnetic couplings and/or magnetic gearing. The expander-generator may be wholly or partially sealed within the heat pipe. A heat engine system (e.g. individual heat engine or array of heat engines in series and/or in parallel) for conversion of thermal energy to useful work (including heat engines operating from a common heat source) is also disclosed. The system can be installed in a vehicle or facility to generate electricity. 1. A heat engine system comprising:at least one heat engine comprising a heat pipe;a generator assembly comprising an expander and a generator;wherein each heat pipe contains a working fluid and comprises an evaporator section and a condenser section;wherein each heat pipe has a capillary structure for the flow of working fluid in liquid phase from the condenser section to the evaporator section;wherein the expander is installed within the heat pipe;wherein the expander is coupled to the generator by a coupling system, andwherein the capillary structure comprises a first capillary region adjacent the evaporator section having a first feature size and a second capillary region adjacent the condenser section having a second feature size, wherein the first feature size is smaller than ...

STEAM TURBINE WITH STEAM STORAGE SYSTEM

A steam turbine system including a steam source for generating a steam flow, a high pressure turbine providing a first steam exhaust, a low pressure turbine fluidly coupled to the high pressure turbine, and, a steam storage system having an inlet for receiving a portion of the first steam exhaust from the high pressure steam turbine and storing in the steam storage system, the steam storage system having an output with a pressure relief valve for discharging a second steam exhaust to the low pressure turbine. 1. A steam turbine system , comprising:a steam source for generating a steam flow;a high pressure turbine providing a first steam exhaust;a low pressure turbine fluidly coupled to the high pressure turbine;a steam storage system having an inlet for receiving a portion of the first steam exhaust from the high pressure steam turbine and storing in the steam storage system, the steam storage system having an output with a pressure relief valve for discharging a second steam exhaust to the low pressure turbine.2. The steam turbine system of claim 1 , wherein the steam source includes a first superheater and a second superheater claim 1 , the steam turbine system further comprising an interstage desuperheater operatively arranged between the first and second superheaters.3. The steam turbine system of claim 1 , further comprising a desuperheater between the first exhaust of the high pressure steam turbine and the inlet of the steam storage system.4. The steam turbine system of claim 1 , further comprising a heat exchanger operatively coupled between the first exhaust of the high pressure steam turbine and the inlet of the steam storage system.5. The steam turbine system of claim 4 , wherein the steam source is a heat recovery system generator (HRSG) having a low pressure system claim 4 , and the heat exchanger is configured to output into LP steam from the low pressure system of the HRSG.6. The steam turbine system of claim 1 , further comprising an intermediate ...

Evaporator with Integrated Heat Recovery

An evaporator with integrated heat recovery incorporates a vapor tube in a combustion chamber surrounded by a water jacket. The water jacket is in fluid communication with an exhaust gas heat exchanger. Coolant circulates through the exhaust gas heat exchanger to recover heat from exhaust gasses leaving the combustion chamber and then circulates through the water jacket surrounding the combustion chamber to recover heat not delivered to the operating fluid. The evaporator may incorporate a condenser within the housing and in fluid communication with the exhaust gas heat exchanger and water jacket. Coolant may enter the evaporator housing at the condenser before circulating through the exhaust gas heat exchanger and water jacket. 1. An evaporator with integrated heat recovery , said evaporator comprising:a housing;a combustion chamber within said housing, said combustion chamber surrounding a fuel burner combusting fuel to generate heat and a flow of heated combustion gasses;a vapor tube arranged in said combustion chamber, said vapor tube having an inlet end receiving a flow of operating fluid which absorbs heat from said heated combustion gasses and transitions to vapor, which leaves said vapor tube at an outlet end;an exhaust gas heat exchanger within said housing and comprising a plurality of exhaust tubes receiving said flow of heated combustion gasses from said combustion chamber;a coolant jacket at least partially surrounding said combustion chamber and in fluid communication with said exhaust gas heat exchanger,wherein coolant enters said housing and circulates through said exhaust gas heat exchanger and said coolant jacket before leaving said housing.2. The evaporator of claim 1 , wherein said coolant jacket includes an annular space surrounding a side wall of said combustion chamber and inside said housing.3. The evaporator of claim 1 , wherein said combustion chamber includes a thermal barrier at least partially surrounding said vapor tube.4. The ...

POWER SYSTEMS AND METHODS IMPLEMENTING AND USING SAME

Power systems and methods including a vaporization subsystem (VPSS), an energy conversion subsystem (ECSS), and a distillation condensation subsystem (DCSS), where the DCSS produces a fully condensed, lean working solution stream (LWSS) and a fully condensed, rich working solution stream (RWSS) from a multiple component working fluid using an external coolant stream, the VPSS vaporizes and superheats the LWSS and RWSS in a multi-stage vaporization process such that each LWSS remains in a state of subcooled liquid prior to being mixed with the RWSS or one or more intermediate solution streams to maximize heat extraction from an external heat source stream to form a combined working solution stream (CWSS) and converting a portion of the heat in the CWSS into a useable from of energy in the ECSS. 1. A system for power generation comprisinga distillation condensation subsystem (DCSS-50), where a spent combined working solution stream CWFS is fully condensed in a multi-stage distillation and condensation process using variable composition streams derived from the CWFS and an external coolant stream CS to produce a fully condensed rich working solution stream RWFS and a fully condensed lean working solution stream LWFS and a spent CS,a vaporization subsystem (VPSS), where heat from an external heat source stream HSS is used to heat, fully vaporize and superheat the RWFS and the LWFS in a multi-stage vaporization process such that each lean working solution stream remains in a state of supercooled liquid prior to being mixed with the rich working solution stream or one or more intermediate solution streams to maximize heat transfer from the HSS to produce a fully vaporized and superheated CWFS and a spent HSS, andan energy conversion subsystem (ECSS), where a portion of heat associated with the CWFS is converted into a useable form of energy producing a spent CWFS which is forwarded to the DCSS-50 closing the system,where all of the streams are derived from a single multi- ...

COGENERATION SYSTEM FOR INTEGRATION INTO SOLAR WATER HEATING SYSTEMS

A cogeneration system to generate thermal energy in form of hot water, using the system's solar collector directly as an evaporator and a heat exchanger integrated in a thermal tank used as a condenser. A variable capacity expander (turbine) is used and the organic working fluid selection is specific for this application. Thus is provided a technological alternative for the production of electricity and thermal energy using a renewable energy source. 1. A cogeneration system for integration into solar water heating systems comprising:a solar collector;a two-position, three-way valve interconnected to the solar connector;wherein in a first position the two-position, three-way valve allows a working fluid to flow towards a condenser, and in a second position the two-position, three-way valve conducts the working fluid towards an expansion device,wherein the working fluid that comes out of the expansion device is conducted towards the condenser and the condenser is a heat exchanger submerged in the thermal tank;wherein a condenser output is interconnected with the two-position, three-way valve; in the first position, the two-position, three-way valve allows the working fluid flow towards a fluid pump, and in a second position, the two-position, three-way valve leads the flow towards an auxiliary heat exchanger, the working fluid output of the auxiliary heat exchanger is interconnected to a receptor tank.2. The cogeneration system for integration into solar water heating systems according to claim 1 , wherein the system a first operation mode a water heating exclusively and second operation mode a water heating together with electric energy production.34. The cogeneration system for integration into solar water heating systems according to claim 2 , wherein for the water heating operation mode claim 2 , the system setting for exclusive production of hot water includes having the working fluid claim 2 , after exiting the collector claim 2 , conducted towards the valve ...

WASTE HEAT RECOVERY POWER GENERATION PLANT FOR SINTERING FACILITY

To provide a waste heat recovery power generation plant for sintering facility capable of efficiently recovering a waste heat of a sintering machine in addition to that of a sintered-ore cooler, while restraining that sulfuric anhydride contained in an exhaust gas of the sintering machine forms drops. An SM boiler is configured to heat all of or a part of hot water generated by an SC boiler, by introducing a high temperature part of an exhaust gas of a sintering machine. At this time, a temperature of the hot water to be supplied to the SM boiler is controlled such that a temperature of an exhaust gas at an exhaust-gas temperature of the SM boiler is maintained at a temperature higher than an acid dew point. 1. A waste heat recovery power generation plant to be applied to a sintering facility including a sintering machine and a sintered-ore cooler , the waste heat recovery power generation plant comprising:a multi-stage type steam turbine joined to a power generator;a sintered-ore-cooler waste heat boiler configured to heat condensate of the multi-stage type steam turbine by introducing an exhaust gas of the sintered-ore cooler so as to generate hot water and steam; anda sintering-machine waste heat boiler configured to heat all of or a part of the hot water generated by the sintered-ore-cooler waste heat boiler by introducing a high temperature part of the exhaust gas of the sintering machine so as to generate steam;wherein:the steam generated by the sintered-ore-cooler waste heat boiler and the steam generated by the sintering-machine waste heat boiler are supplied to a high-pressure stage of the multi-stage type steam turbine; anda temperature of the hot water to be supplied to the sintering-machine waste heat boiler is controlled such that a temperature of the exhaust gas at an exhaust-gas outlet of the sintering-machine waste heat boiler is maintained to be higher than an acid dew point.2. The waste heat recovery power generation plant for sintering facility ...

STEAM BYPASS CONDUIT

An arrangement for making a flow uniform, having a housing, which is designed to limit the flow, wherein the housing has holes through which the flow flows, as a jet, into a space outside the housing, wherein the holes are spaced apart in such a way that it is not possible for jets coming from two adjacent holes to merge. 1. A bypass steam system for introducing a flow of high-energy steam into a condenser , comprising:an arrangement making the flow uniform, wherein the arrangement has a housing, which is designed to limit the flow, wherein the housing has holes, through which the flow flows as a jet into a space outside the housing,wherein the spacing D of the holes is such that, at a distance A from the housing, it is not possible for jets coming from two adjacent holes to merge, where D=A,wherein the spacing D of two adjacent hole centers is at least D=50 mm.2. The arrangement as claimed in claim 1 ,wherein the arrangement is a perforated basket.3. The arrangement as claimed in claim 1 ,when the arrangement is a dump tube.4. The arrangement as claimed in claim 1 ,wherein the holes are formed as a hole differing from a circular cross section.5. The arrangement as claimed in claim 4 ,wherein the ratio of hole circumference to hole cross section is maximized.6. The arrangement as claimed in claim 4 ,wherein the hole is formed in the shape of a cloverleaf.7. The arrangement as claimed in claim 1 ,wherein the holes are designed in the shape of a Laval nozzle.8. A condenser comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'an arrangement as claimed in .'} This application is the US National Stage of International Application No. PCT/EP2019/066192 filed 19 Jun. 2019, and claims the benefit thereof. The International Application claims the benefit of European Application No. EP18181414 filed 3 Jul. 2018. All of the applications are incorporated by reference herein in their entirety.The invention relates to a steam bypass housing for introducing a flow of high ...

BOILER, COMBINED CYCLE PLANT, AND BOILER OPERATION METHOD

The purpose of the present invention is to maintain the intake pressure of a water supply pump at an operable pressure. A boiler is provided with: condensate pumps (a condensate pump and an auxiliary condensate pump); a branch line that causes water delivered by the condensate pumps to branch; a drum (a low-pressure drum) that is connected to one (a low-pressure branch line) of two lines into which the branch line branches; and a water supply pump that is connected to the other (a high-pressure branch line) of the two lines into which the branching line branches and that pumps water to an evaporator (a high-pressure evaporator). The boiler is additionally provided with pressure applying means that guides a portion of the water in the drum to the water supply pump side when the intake pressure on the inlet side of the water supply pump has become lower than a predetermined pressure. 1. A boiler comprising:a condensate pump;a branch line which causes water delivered by the condensate pump to branch;a drum which is connected to one of two lines into which the branch line branches; anda water supply pump which is connected to the other of the two lines into which the branch line branches and pumps water to an evaporator,wherein the boiler is provided with means for guiding a portion of the water in the drum to the water supply pump side in a case where an inlet side pressure of the water supply pump has become lower than a predetermined pressure.2. The boiler according to claim 1 ,wherein the means includesa bypass line which bypasses a portion of the branch line and connects the drum and the inlet side of the water supply pump to each other, anda check valve which is provided in the bypass line and allows the water to flow only from the drum side to the water supply pump side.3. The boiler according to claim 2 ,wherein an inner diameter of a path from the drum to the inlet side of the water supply pump which includes the bypass line is larger than an inner diameter of ...

SYSTEMS AND METHODS FOR GENERATING STEAM BY CREATING SHOCKWAVES IN A SUPERSONIC GASEOUS VORTEX

Steam may be generated using an apparatus that creates shockwaves in a supersonic gaseous vortex. The apparatus includes a chamber configured to receive, pressurize, and heat fuel gas and/or oxygen containing gas. One or more inlets positioned at a first end of the chamber and arranged to emit fuel gas, oxygen containing gas, or water as one or more jet streams tangentially to an internal surface of the chamber may create a gaseous vortex rotating about a longitudinal axis within the chamber. The inlet(s) may include one or more inlet nozzles structured to accelerate the one or more fuel gas, oxygen-containing gas, or water to a supersonic velocity and adjustably control frequency of shockwaves emitted into the gaseous vortex. Water can be injected into the chamber to stabilize internal chamber temperature where it may be converted into steam. An outlet may be configured to emit product gases and/or steam from the chamber. 1. A system for generating steam using an apparatus that creates shockwaves in a supersonic gaseous vortex , the system comprising: a chamber having an internal surface that is substantially axially symmetrical about a longitudinal axis, the chamber being configured to (1) receive at least fuel gas and/or oxygen containing gas, (2) pressurize the at least fuel gas and/or the oxygen containing gas, and (3) heat the at least fuel gas and/or the oxygen containing gas to a temperature exceeding an auto-ignition temperature of the fuel gas and/or the oxygen containing gas;', 'one or more inlets positioned at a first end of the chamber and arranged to introduce one or more of the fuel gas, the oxygen containing gas, or water as one or more jet streams tangentially to the internal surface of the chamber to effectuate a gaseous vortex rotating about the longitudinal axis within the chamber, the one or more inlets comprising one or more inlet nozzles configured to accelerate the one or more jet streams to a supersonic velocity, the one or more inlet ...

Steam turbine plant and cooling method for same

A steam turbine plant is provided with: a boiler; a fuel valve; a low-temperature steam generation source; a steam turbine; a main steam line that guides steam generated in the boiler to the steam turbine; a main steam adjustment valve that is provided to the main steam line; a low-temperature steam line that guides low-temperature steam from the low-temperature generation source to a position closer to the steam turbine-side than the main steam adjustment valve in the main steam line; a low-temperature steam valve provided to the low-temperature steam line; and a control device. During a stopping process of the steam turbine plant, the control device sends a command to close the fuel valve, and then sends a command to open the low-temperature steam valve.

STEAM TURBINE FACILITY AND COMBINED CYCLE PLANT

A steam turbine facility includes a rotor shaft, a pair of radial bearings for rotatably supporting the rotor shaft, a pair of low-pressure turbine blade rows disposed on the rotor shaft in a bearing span of the pair of radial bearings, and a high-pressure turbine blade row and an intermediate-pressure turbine blade row disposed on the rotor shaft in the bearing span and positioned between the pair of low-pressure turbine blade rows. 1. A steam turbine facility , comprising:a rotor shaft;a pair of radial bearings for rotatably supporting the rotor shaft;a pair of low-pressure turbine blade rows disposed on the rotor shaft in a bearing span of the pair of radial bearings; anda high-pressure turbine blade row and an intermediate-pressure turbine blade row disposed on the rotor shaft in the bearing span and positioned between the pair of low-pressure turbine blade rows.2. The steam turbine facility according to claim 1 , further comprising:a branched channel for introducing a part of steam flowing through a first low-pressure turbine blade row which is one of the pair of low-pressure turbine blade rows to an inlet of a second low-pressure turbine blade row which is the other of the pair of low-pressure turbine blade rows.3. The steam turbine facility according to claim 2 , further comprising:an inner casing for accommodating the high-pressure turbine blade row and the intermediate-pressure turbine blade row; andan outer casing for accommodating the inner casing and at least a part of the pair of low-pressure turbine blade rows,wherein the branched channel is formed at least partially by an outer circumferential surface of the inner casing and an inner circumferential surface of the outer casing.4. The steam turbine facility according to claim 3 ,wherein an insulator is disposed on the outer circumferential surface of the inner casing.5. The steam turbine facility according to claim 2 , further comprising:an inner casing for accommodating the high-pressure turbine blade ...

POWER GENERATION SYSTEM AND METHOD WITH PARTIALLY RECUPERATED FLOW PATH

The present disclosure relates to a power generation system and related methods that use supercritical fluids, whereby a portion of the supercritical fluid is recuperated. 1. A method for generating power in a system that includes a supercritical fluid cycle having a supercritical fluid flowing therethrough , an air-breathing cycle having air flowing therethrough that does not mix with the flow of the supercritical fluid , the method comprising:directing air along the air-breathing cycle to flow through a plurality of heat exchangers;compressing the supercritical fluid in a supercritical fluid compressor along the supercritical fluid cycle;splitting the supercritical fluid discharged from the supercritical fluid compressor into first and second discharge streams of compressed supercritical fluid, such that the first discharge stream of compressed supercritical fluid flows through a recuperating heat exchanger;mixing the supercritical fluid discharged from the recuperating heat exchanger with the second discharge stream of compressed supercritical fluid;directing a mixture of compressed supercritical fluid through one of the plurality of heat exchangers arranged and into an inlet of a supercritical fluid turbine, such that heat from the air along the air-breathing cycle is transferred to the mixture of compressed supercritical fluid;splitting the supercritical fluid discharged from the supercritical fluid turbine into a first and second discharge streams of expanded supercritical fluid such that the first discharge stream of expanded supercritical fluid flows through the recuperating heat exchanger so as to heat the first discharge stream of compressed supercritical fluid;mixing the expanded supercritical fluid discharged from the recuperating heat exchanger with the second discharge stream of expanded supercritical fluid; anddirecting a mixture of expanded supercritical fluid toward the inlet of the supercritical compressor,wherein heat from the mixture of expanded ...

Supercritical CO2 Generation System Applying Plural Heat Sources

The present invention relates to a supercritical COgeneration system applying plural heat sources. According to the present invention, each heat exchanger is effectively disposed according to conditions such as an inlet and outlet temperature, capacity, the number, etc. of the heat source, such that it is possible to use the same or smaller number of recuperators as compared to the number of heat sources, thereby simplifying the system configuration and implementing effective operation. 1. A supercritical COgeneration system applying plural heat sources , comprising:a pump circulating a working fluid;a plurality of heat exchangers heating the working fluid through external heat sources;a plurality of turbines operated by the working fluid heated by passing through the heat exchangers; anda plurality of recuperators cooling the working fluid passing through the turbines by heat exchange between the working fluid passing through the turbines and the working fluid passing through the pump,{'sub': '0', 'wherein the heat exchangers are heat sources using heat of waste heat gas exhausted from a waste heat source and include a plurality of constrained heat exchangers having an emission regulation condition of a discharge end, and an integrated flow rate (mt) of the working fluid is supplied to the recuperators.'}2. The supercritical COgeneration system applying plural heat sources of claim 1 , wherein the emission regulation condition is a temperature condition.3. The supercritical COgeneration system applying plural heat sources of claim 2 , wherein the number of recuperators is the same as or less than the number of heat exchangers.4. The supercritical COgeneration system applying plural heat sources of claim 3 , wherein the turbines include a low pressure turbine operating the pump and a high pressure turbine operating a generator claim 3 , and the integrated flow rate (mt) of the working fluid passing through the low pressure turbine and the high pressure turbine is ...

SUPERCRITICAL CO2 GENERATION SYSTEM APPLYING PLURAL HEAT SOURCES

The present invention relates to the supercritical COgeneration system applying plural heat sources. The supercritical COgeneration system applying plural heat sources includes a pump circulating a working fluid; a plurality of heat exchangers heating the working fluid using an external heat source and including a plurality of constrained heat sources having an emission regulation condition of an outlet end thereof and a plurality of general heat sources without the emission regulation condition; a plurality of turbines operated by the working fluid heated by passing through the heat exchangers; and a plurality of recuperators cooling the working fluid passing through the turbines by heat exchange between the working fluid passing through the turbines and the working fluid passing through the pump, wherein the working fluid passing through the turbine is branched into the recuperators, respectively. 1. A supercritical COgeneration system applying plural heat sources , comprising:a pump circulating a working fluid;a plurality of heat exchangers heating the working fluid using an external heat source and including a plurality of constrained heat sources having an emission regulation condition of an outlet end thereof and a plurality of general heat sources without the emission regulation condition;a plurality of turbines operated by the working fluid heated by passing through the heat exchangers; anda plurality of recuperators cooling the working fluid passing through the turbines by heat exchange between the working fluid passing through the turbines and the working fluid passing through the pump,wherein the working fluid passing through the turbines is branched into the recuperators, respectively.2. The supercritical COgeneration system applying plural heat sources of claim 1 , wherein the emission regulation condition is a temperature condition.3. The supercritical COgeneration system applying plural heat sources of claim 2 , wherein a number of the recuperators is ...

MODULE FOR CONDENSING EXPELLED VAPORS AND FOR COOLING TURBINE EFFLUENT

A module for a thermal power plant for condensing expelled vapors and cooling turbine effluent from the drained turbine includes a first unit designed to condense expelled vapors as well as a second unit designed to cool the turbine effluent, condensate from the first unit being transferable to the second unit. 1. A module for a thermal power plant for condensing vapor steam and for cooling turbine waste water from turbine drainage , comprising:a first unit which is designed to condense vapor steam anda second unit which is designed to cool the turbine waste water,wherein condensate produced in the first unit can be is passed to the second unit.2. The module as claimed in claim 1 , further comprising:a condensate line which serves to pass condensate from the first unit to the second unit.3. The module as claimed in claim 1 , further comprising:cooling water that flows through the first unit.4. The module as claimed in claim 3 ,wherein the cooling water is used in the second unit after flowing through the first unit.5. The module as claimed in claim 1 , further comprising:in the first unit, an outlet through which air, carried with the vapor steam into the first unit, is discharged, after condensation of the vapor steam.6. The module as claimed in claim 1 ,wherein the second unit has an inlet for turbine waste water.7. The module as claimed in claim 1 ,wherein the second unit has an outlet to the main condenser.8. The module as claimed in claim 1 , further comprising:a connection line, serving for pressure equalization, between the second unit and the main condenser.9. The module as claimed in claim 2 , further comprising:a steam trap in the condensate line.10. The module as claimed in claim 3 ,wherein the cooling water comprises cooling water which is provided for standpipes of a main condenser of the thermal power plant.11. The module as claimed in claim 4 ,wherein the cooling water is injected into the second unit.12. The module as claimed in claim 5 ,wherein the ...

SYSTEM AND METHOD FOR HEATING MAKE-UP WORKING FLUID OF A STEAM SYSTEM WITH ENGINE FLUID WASTE HEAT

A system including an engine and a heat exchanger coupled to the engine is provided. The engine includes an engine fluid and at least one of a compressor section configured to compress a gas, a lubricant path configured to circulate a lubricant, or a coolant path configured to circulate a coolant. The engine fluid comprises at least one of the gas, the lubricant, or the coolant, and the engine fluid is a source of heat derived from one or more operations of the engine. The heat exchanger is configured to receive the engine fluid from the engine and exchange heat between the engine fluid and a working fluid to produce a heated working fluid and a cooled engine fluid, and the heat exchanger is configured to export the heated working fluid to a steam system. 1. A system , comprising:an engine comprising an engine fluid and at least one of a compressor section configured to compress a gas, a lubricant path configured to circulate a lubricant, or a coolant path configured to circulate a coolant, wherein the engine fluid comprises at least one of the gas, the lubricant, or the coolant, and wherein the engine fluid is a source of heat derived from one or more operations of the engine; anda heat exchanger coupled to the engine, wherein the heat exchanger is configured to receive the engine fluid from the engine and exchange heat between the engine fluid and a working fluid to produce a heated working fluid and a cooled engine fluid, and the heat exchanger is configured to export the heated working fluid to a steam system.2. The system of claim 1 , comprising the steam system configured to receive the heated working fluid from the heat exchanger as a make-up water supply of working fluid to replace working fluid lost within a process of the steam system.3. The system of claim 2 , wherein the steam system comprises a deaerator configured to receive the heated working fluid from the heat exchanger and remove at least one of one or more corrosive substances and/or dissolved ...

PRODUCTION OF ELECTRIC POWER FROM FOSSIL FUEL WITH ALMOST ZERO POLLUTION

The present invention discloses a system for the separation and non-polluting disposal of carbon dioxide derived from the exhaust of burning fossil fuel, including a gas separation system which includes: a first stage of gas membranes C02 separators, means to transport exhaust gas to the first stage, the first stage separating C02 from other gases in the exhaust gas, a second stage of gas membrane C02 separators, means to transport permeant gas that passes through the membranes of the first stage to the second stage, the second stage producing C02 permeate gas of purity greater than 90%. 1. A system for the separation and non-polluting disposal of carbon dioxide derived from the exhaust of burning fossil fuel , including a gas separation system which includes: a first stage of gas membranes CO2 separators , means to transport exhaust gas to the first stage , the first stage separating CO2 from other gases in the exhaust gas , a second stage of gas membrane CO2 separators , means to transport permeant gas that passes through the membranes of the first stage to the second stage , the second stage producing CO2 permeate gas (that passes through the membranes of the second stage) of purity greater than 90% , a CO2s gas compressor , and means to transport the permeate gas that passes through the second stage to the compressor , wherein: the membranes of the first stage have a permeance greater than 800 GPU and a CO2/N2 selectivity of greater than 10 and the membranes of second stage have a permeance greater than 10 GPU and a CO2/N2 selectivity greater than 30.2. A system as in wherein the membranes of the first stage have a permeance of at least 4000 GPU.3. A system as in wherein the membranes of the second stage have a selectivity for CO2 greater than 100.4. A system as in and also including a first blower to compress gas entering the first stage and a second stage compressor to compress gas entering the second stage claim 1 , wherein in operation the gas is compressed ...

WASTE THERMAL ENERGY RECOVERY DEVICE

A waste heat recovery system includes a condenser to receive a working fluid in a vapor state and provide the working fluid in a liquid state; a pump in fluid communication with the condenser; a waste heat boiler in fluid communication with the pump, the waste heat boiler to receive the working fluid from the pump and vaporize the working fluid using waste heat from a mechanical system; an expander in fluid communication with the waste heat boiler and the condenser, the expander to receive the vaporized working fluid from the waste heat boiler and to provide the working fluid to the condenser, the expander to produce mechanical power; and a mechanical coupling system mechanically coupled between the expander and the mechanical system. 1. A waste heat recovery system comprising:a condenser to receive a working fluid in a vapor state and provide the working fluid in a liquid state;a pump in fluid communication with the condenser to receive the working fluid in the liquid state and to increase a pressure of the working fluid;a waste heat boiler in fluid communication with the pump, the waste heat boiler to receive the working fluid from the pump and vaporize the working fluid using waste heat from a mechanical system;an expander in fluid communication with the waste heat boiler and the condenser, the expander to receive the vaporized working fluid from the waste heat boiler and to provide the working fluid to the condenser, the expander to produce mechanical power;a mechanical coupling system mechanically coupled between the expander and the mechanical system;a pump bypass valve to receive working fluid downstream of the pump and to provide working fluid upstream of the pump; anda controller to control the pump bypass valve based on a saturation level of the vaporized working fluid upstream of the waste heat boiler.2. The waste heat recovery system of claim 1 , wherein the saturation is determined using a lookup table and a temperature upstream of the waste heat boiler ...

DEVICE FOR OIL SEPARATION AND REMOVAL FROM AN ORGANIC WORKING FLUID

Device for oil separation and removal from a working fluid of an organic Rankine cycle plant, said plant having at least a supply pump (), at least a heat exchanger (), an expansion turbine (), a condenser (), wherein the device is provided with a separator () and collection means (), located between the evaporator () and the condenser () or between the evaporator () and a regenerator () of the organic Rankine cycle plant. 2711421920. The device according to claim 1 , wherein said bypass line () is configured so as to connect a portion (′) of the evaporator () in which is present the vapor phase of the working fluid and the condenser () and wherein said separator () is a cyclone () and comprises in its terminal part a coalescent filter ().3. (canceled)48. The device according to wherein said first valve () is configured to continuously control the bypass flowrate in a range between 1/10000 and 1/1000 of the total plant flow-rate.59. The device according to wherein said second valve () is configured to adjust the pressure on the bypass line.6. The device according to wherein a calibrated hole disc is configured to determine the bypass flowrate.7. The device according to wherein a capillary tube is configured to determine the bypass flowrate.8. (canceled)915231533. The device according to further comprising a fourth valve () which is located between the separator () and the collection means () claim 1 , said fourth valve () being configured to isolate said collection means () so that the separator continues working while making the discharge of the collection means ().101. The device according to claim 1 , assembled on the head of the evaporator () by fastening means.1131. The device according to wherein said collection means () is configured to be welded on the evaporator () head claim 1 , so as to allow an easy control of the collecting working fluid temperature.123. The device according to wherein said collection means () is a separate device that is autonomously ...

DISPATCHABLE STORAGE COMBINED CYCLE POWER PLANTS

A dispatchable storage combined cycle power plant comprises a combustion turbine generator, a steam power system, a heat source other than the combustion turbine generator, and a thermal energy storage system. Heat from the heat source, from the thermal energy storage system, or from the heat source and the thermal energy storage system is used to generate steam in the steam power system. Heat from the combustion turbine may be used in series with or in parallel with the thermal energy storage system and/or the heat source to generate the steam, and additionally to super heat the steam. 1. A method of operating a combined cycle electric power plant , the method comprising:operating a combustion turbine generator to generate electricity and produce hot exhaust gases;{'b': '1', 'storing heat from a heat source other than the combustion turbine generator in a thermal energy storage system at a temperature T;'} [{'b': 1', '2', '1, 'producing steam in a first boiler by heating feedwater with heat supplied at temperature T from the thermal energy storage system by a heat transfer fluid, thereby cooling the heat transfer fluid, and storing heat from the cooled heat transfer fluid in the thermal energy storage system at a temperature T Подробнее