Настройки

Укажите год
-

Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

Подробнее
-

Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

Подробнее

Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Укажите год
Укажите год

Применить Всего найдено 2229. Отображено 199.
13-03-2018 дата публикации

ТРУБА ТЕПЛООБМЕННИКА И ОТОПИТЕЛЬНЫЙ КОТЕЛ, ИМЕЮЩИЙ ТАКУЮ ТРУБУ ТЕПЛООБМЕННИКА

Номер: RU2647012C2

Изобретение относится к теплотехнике и может быть применено в отопительных котлах. У трубы (5) теплообменника отопительного котла (2), имеющей наружную трубу (10), по которой могут протекать уходящие газы топки котла, и которая может быть окружена с наружной стороны греющей водой, и вдвинутую в наружную трубу профильную вставку (11), которая для увеличения внутренней поверхности наружной трубы (10) имеет ребра (14), проходящие в ее продольном направлении (12), и находится в теплопроводящем контакте с наружной трубой (10), первый продольный участок (22) наружной трубы (10) выполнен в виде гладкостенного цилиндра, а второй продольный участок (23) наружной трубы (10) имеет по меньшей мере один элемент (24) для сужения поперечного сечения, сужающий проточное поперечное сечение, при этом профильная вставка (11) распространяется исключительно по первому продольному участку (22) наружной трубы (10). Технический результат – повышение мощности передачи тепла газообразных продуктов сгорания греющей ...

Подробнее
10-09-2015 дата публикации

СИСТЕМЫ И СПОСОБЫ ОБЕСПЕЧЕНИЯ УСТОЙЧИВОГО ЭКОНОМИЧЕСКОГО РАЗВИТИЯ ПУТЕМ ИНТЕГРИРОВАННОЙ ВЫРАБОТКИ ВОЗОБНОВЛЯЕМОЙ ЭНЕРГИИ ПОЛНОГО СПЕКТРА

Номер: RU2562336C2

В одном варианте выполнения изобретения предложен способ подачи электроэнергии при помощи источника возобновляемой энергии, включающий: обеспечение первого источника возобновляемой энергии, причем первый источник возобновляемой энергии является непостоянным или не обеспечивает достаточного количества энергии; подачу энергии от первого источника возобновляемой энергии на электролизер с целью формирования энергоносителя посредством электролиза; избирательное реверсирование электролизера, позволяющее использовать его в качестве топливного элемента; и подачу энергоносителя на электролизер для выработки энергии, причем первый источник возобновляемой энергии, электролизер или энергоноситель получает дополнительное тепло от первого источника тепла; и первый источник тепла выбран из группы, состоящей из геотермального и солнечного источника тепла. 5 н. и 36 з.п. ф-лы, 26 ил.

Подробнее
10-06-2013 дата публикации

ЭЛЕКТРОЛИТИЧЕСКАЯ ЯЧЕЙКА И СПОСОБ ЕЕ ПРИМЕНЕНИЯ

Номер: RU2484182C2

Предложена электролитическая ячейка, содержащая герметизирующий сосуд, первый электрод, второй электрод, источник электрического тока, находящийся в электрическом сообщении с первым электродом и вторым электродом, электролит, имеющий жидкостное сообщение с первым электродом и вторым электродом; газ, причем этот газ образуется во время электролиза на первом электроде или вблизи него; при этом ячейка снабжена сепаратором, который имеет наклонную поверхность, и включает в себя электрод, чтобы можно было направлять поток электролита и газа за счет разности между плотностью электролита и суммарной плотностью электролита и газа таким образом, чтобы газ перемещался в направлении в сторону от второго электрода. Повышение циркуляции электролита при помощи наклонного сепаратора, а также увеличение эффективности массопередачи в процессе электролиза, является техническим результатом предложенного изобретения. Предложенная ячейка работает при отсутствии протоннообменной мембраны и позволяет быстро удалять ...

Подробнее
31-01-2018 дата публикации

ТРУБЧАТОЕ УСТРОЙСТВО ДЛЯ ТЕРМООБРАБОТКИ С ПОВЫШЕННОЙ ЭФФЕКТИВНОСТЬЮ ИСПОЛЬЗОВАНИЯ ЭНЕРГИИ

Номер: RU2643283C2

Изобретение относится к теплотехнике и может быть использовано в трубчатых теплообменниках пищевой промышленности. Трубчатое устройство для термообработки содержит некоторое количество труб, расположенных в виде некоторого количества групп. Каждая из данного количества групп выполнена с возможностью обработки продукта в заданном интервале температур. По меньшей мере, одна из групп охвачена листом так, что передача тепла к данной группе или от данной группы уменьшается. Технический результат - обеспечение возможности выполнения термообработки способом, более благоприятным для окружающей среды. 3 н. и 15 з.п. ф-лы, 14 ил.

Подробнее
28-12-2020 дата публикации

Номер: RU2017134410A3
Автор:
Принадлежит:

Подробнее
14-03-2017 дата публикации

ТРУБЧАТЫЙ ТЕПЛООБМЕННЫЙ АППАРАТ

Номер: RU169293U1

Полезная модель относится к теплообменным аппаратам и может быть использована в энергетике, ЖКХ и смежных с ними отраслях промышленности.Задачей полезной модели является достижение высокой эффективности теплообмена, снижения металлоемкости трубчатого теплообменного аппарата, а также температурных деформаций в трубах аппарата и возможности использования трубчатого теплообменного аппарата в широком интервале разности температур в трубных пучках трубчатого теплообменного аппарата, технический результат достигается тем, что трубчатый теплообменный аппарат выполнен нежесткой конструкции без кожуха.Преимуществом предлагаемого трубчатого теплообменного аппарата является возможность снижения температурных деформаций при удлинении труб трубных пучков под действием температуры независимо друг от друга.

Подробнее
06-11-2018 дата публикации

ТЕПЛООБМЕННИК

Номер: RU2671669C1

Изобретение относится к теплообменной технике и может быть использовано при создании теплообменных аппаратов. Теплообменник содержит цилиндрический корпус, во внутренней полости которого установлены концентрически соединенные между собой втулки, на наружной поверхности которых выполнены кольцевые каналы, соединенные с подводящим и отводящим коллекторами одного из теплоносителей, расположенными в одной из крышек, установленных на торце корпуса, с помощью двух диаметрально расположенных продольных каналов, при этом втулки одного теплоносителя и втулки другого теплоносителя чередуются между собой. 4 ил.

Подробнее
27-02-2014 дата публикации

КОАКСИАЛЬНЫЙ ВОЗДУХО-ВОЗДУШНЫЙ ТЕПЛООБМЕННИК ДЛЯ УСТАНОВКИ В КОЛЬЦЕВОЙ ОКОННОЙ РАМЕ

Номер: RU2012134998A
Принадлежит:

... 1. Кольцевой и коаксиальный теплообменник, состоящий из рамы, воздуховодов для подводимого и отводимого воздуха, а также вентиляторов, отличающийся тем, что имеет, по меньшей мере, одну внутреннюю диафрагму, расположенную коаксиально по отношению к внешней оболочке, и отделяющую друг от друга, по меньшей мере, два герметично отделенных воздуховода для подводимого и отводимого воздуха.2. Кольцевой и коаксиальный теплообменник по п.1, отличающийся тем, что форма поперечного сечения внутренней диафрагмы соответствует форме внешней оболочки.3. Кольцевой и коаксиальный теплообменник по п.1, отличающийся тем, что он имеет более чем одну внутреннюю диафрагму, расположенную коаксиально по отношению к внешней оболочке, при этом два созданных воздуховода по очереди проводят воздух, подаваемый в и отводимый из помещения.

Подробнее
20-02-1992 дата публикации

Номер: DE0003815608C2
Принадлежит: PUSCH, SIEGFRIED

Подробнее
14-10-2004 дата публикации

Oil cooling heat exchanger has outer pipe with helical rectangular section wire flute defining flow chamber with inner pipe

Номер: DE202004008737U1
Автор:
Принадлежит: SCHMIDPETER MICHAEL, SCHMIDPETER, MICHAEL

The heat exchanger has an outer pipe (2) and an inner pipe (3) between which is a helical partition wall defining a helical channel (6) for a heat exchange medium. The partition wall can be made out of wire with a near rectangular cross section, with a height to width ratio of not more than four. The partition wall is attached to the inner pipe at point connections.

Подробнее
06-08-2015 дата публикации

Verfahren zur Führung eines Fluidstroms, Strömungsapparat und dessen Verwendung

Номер: DE102014201908A1
Принадлежит:

Die Erfindung betrifft ein Verfahren zur Führung einer Fluidströmung (10) die einen Anström- und einen Abströmabschnitt (12, 13) mit einer im Wesentlichen parallelen, vorzugsweise koaxialen An- und Abströmachse (14, 15) aufweist. Dabei wird vorgeschlagen, dass die Fluidströmung (10) durch mindestens ein zwischen dem Anströmabschnitt (12) und die Abströmabschnitt (13) angeordneten Führungsmittel (20) in einem Umströmungsabschnitt um einen Umfangswinkel UW die An- und Abströmachse radial umlaufend gelenkt wird, wobei der Umfangswinkel UW größer als 0° ist. Weiters betrifft die Erfindung einen Strömungsapparat (50) zur Durchführung eines Verfahrens umfassend ein erstes Leitungssystem (60) zur Durchleitung eines ersten Fluidstroms (100), wobei das erste Leitungssystem (60) ein Führungsrohr (21) und mindestens ein, eine Strömungsrichtung des Fluidstroms (100) beeinflussendes Führungsmittel (20, 22) umfasst, so dass der Fluidstrom (100) zwischen einem Anströmbereich (61b) und einem Abströmbereich ...

Подробнее
31-07-2014 дата публикации

Doppelwandiges Wärmetauscherrohr

Номер: DE102013100886A1
Принадлежит:

Die vorliegende Erfindung betrifft einen Wärmetauscher für ein Kraftfahrzeug, insbesondere Abgaswärmetauscher, wobei der Wärmetauscher (1) eine äußere Hülle (2) aufweist und in der äußeren Hülle (2) Wärmetauscherrohre (3) insbesondere als Bündel angeordnet sind, der dadurch gekennzeichnet ist, dass mindestens usw. ein Wärmetauscherrohr (3) doppelwandig aus einem Außenrohr (4) und einem Innenrohr (5) ausgebildet ist, wobei ein erstes Medium (19) in der Hülle (2) und/oder in dem Innenrohr (5) strömt und ein zweites Medium (9) zwischen Außenrohr (4) und Innenrohr (5) strömt.

Подробнее
20-05-2010 дата публикации

Cooling device for use as exhaust gas cooler to cool exhaust gas of internal combustion engine of motor vehicle, has inlet openings and outlet openings that are arranged at axial ends of screwing body according to number of screw threads

Номер: DE102008056810A1
Принадлежит:

The device has an open inner pipe (2) that is flow throughable by a medium to be cooled i.e. exhaust gas, an outer pipe (12) and a screwing body (4) that is arranged between the pipes. The screwing body is made of molded sheet metal and implemented as multi-threaded. The body has screw threads (40, 42, 44) through which cooling agent flows. The screw threads are axially arranged one behind the other. Inlet openings (34) and outlet openings (46, 48) are arranged at respective axial ends (16, 22) of the screwing body according to the number of screw threads.

Подробнее
13-05-2015 дата публикации

Active cooling of medium voltage power umbilicals

Номер: GB0002519933A
Принадлежит:

An umbilical comprises an outer sheath defining an interior void; one or more power cores; and one or more forced convection cooling circuits disposed within the interior void proximate the power cores, typically at least one forced convection cooling circuit paired with each power core. The forced convection cooling circuit comprises a heat exchange delivery fluid conduit and a heat exchange return fluid conduit in fluid communication with the heat exchange delivery fluid conduit, where at least one of the fluid conduits is disposed either proximate to the other conduit or disposed within the other conduit. The forced convection cooling circuit has a length which has been determined to be sufficient to achieve a desired heat exchange that results in a desired efficient evacuation of heat energy from the power cores along a predetermined length of the umbilical.

Подробнее
23-01-2013 дата публикации

Annular axial flow ribbed heat exchanger

Номер: GB0201222390D0
Автор:
Принадлежит:

Подробнее
24-08-2011 дата публикации

Finned cylindrical heat exchanger

Номер: GB0201111887D0
Автор:
Принадлежит:

Подробнее
21-11-1929 дата публикации

Improvements in heat exchangers

Номер: GB0000321833A
Автор:
Принадлежит:

... 321,833. Cross, R. C.., and Ware, H. M. Nov. 21, 1928. Plate apparatus. - A heatexchanger has concentric tubes forming an annular space terminating in annular chambers formed in casings which embrace the ends of the tubes, and so held that the tubes with these end casings attached may be withdrawn one from the other by relative longitudinal movement in either direction. In the example, Fig. 1, the tubes A, B, secured in casings a, b with annular end chambers a<11>, b<11> are separated by an intermediate tube c terminating in packing glands R which when screwed home render the spaces between the tubes fluid-tight. In Fig. 2, the tubes C, D terminate in casings c, d secured by glands G. An outer casing A and inner core-tube B are also provided.

Подробнее
03-02-1988 дата публикации

FUEL COOLER

Номер: GB0008729420D0
Автор:
Принадлежит:

Подробнее
04-04-1984 дата публикации

Heat exchanger apparatus for extruding thermoplastic compositions

Номер: GB0002127183A
Принадлежит:

A heat exchange device for controlling the temperature of a resin after leaving an extruder and prior to extrusion through a die in an extrusion process, includes a heat exchanger (10) having an inlet (14) and outlet (16) for a heat- plastified resin and an inlet (32) and an outlet (36) for a heat exchange medium (e.g. oil or water). A selective heater (20) receives the medium from the exchanger (10) and heats it to a predetermined temperature during a start-up phase. A cooler (22) receives a portion of the medium from the heater and circulates a cooling medium in heat exchanging relationship with the heat exchange medium. Control means (42) directs a portion of the heat exchange medium to said cooler (22), in response to the temperature of the resin leaving the exchanger (10), and the balance of the medium to the exchanger (10). A pump (24) for circulates the medium between the heat exchanger (10), the heater (20), the cooler (22) and the control means (42). ...

Подробнее
07-01-1987 дата публикации

HEAT EXCHANGER

Номер: GB0002146424B
Принадлежит: SCANLAN HARRY J, HARRY J * SCANLAN

Подробнее
28-07-1993 дата публикации

A WATER COOLING AIR CONDITIONER

Номер: GB0009312336D0
Автор:
Принадлежит:

Подробнее
04-05-1960 дата публикации

Improvements relating to heat recuperators

Номер: GB0000834156A
Автор:
Принадлежит:

... 834,156. Furnace recuperators. ESCHER, H. Feb. 26, 1958 [April 12, 1957], No. 6193/58. Class 64(1) In a combustion furnace recuperator, air or other gas is heated in flowing through an annular jacket surrounding a conduit 1 through which hot gases from a furnace 3 are passed. Hollow fins extend from the conduit 1 into the heating gas stream and a proportion of the air or gas to be heated is directed through these hollow fins whilst the remainder flows through the jacket, the two streams being reunited in the lower and unfinned portion of the jacket surrounding the lower and mainly radiant heating zone 12 of the heating gas conduit 1. In the upper and coolest zone 14 of the conduit 1 where heating is mainly by convection, a guide tube 23 is provided, the upper end of which is closable by a valve 25. The valve 25 is constructed for simultaneous operation with a valve or cover 5 at the outlet end of conduit 1. Under conditions of maximum flow of the heating gas both valves are open and some ...

Подробнее
28-05-1981 дата публикации

HEAT EXCHANGER

Номер: GB0001590196A
Автор:
Принадлежит:

Подробнее
11-10-1978 дата публикации

HEAT EXCHANGER

Номер: GB0001528243A
Автор:
Принадлежит:

... 1528243 Heat exchanges PHILIPS GLOEILAIMPENFABRIEKEN NV 30 Jan 1976 [4 Feb 1975] 03748/76 Heading F4S In heat exchange apparatus in which a fluid such as air flowing in one passage 6 is heated by flue gas flowing in an adjacent passage 7 and wherein said passages are separated from each other by a heat conducting wall 5, the wall comprises two series connected sections 5a, 5b, and in that section 5b containing the flue gas outlet from the heat exchanger said wall is hollow and the space 10 therein contains a volatile fluid which, by a continuous evaporation/condensation cycle, transfers heat through the wall and also acts to equalize the wall temperature along the wall in the direction of fluid flow thereover in said section. The intention is to maintain the flue gas contacted surface of the wall adjacent the flue gas outlet above the dew point temperature of the flue gases. The apparatus may comprise either single passages for the flue gas and air streams, or an intercalated plurality ...

Подробнее
29-10-1980 дата публикации

METHODS OF MANUFACTURING A CONCENTRIC TUBE HEAT EXCHANGER

Номер: GB0001577809A
Автор:
Принадлежит:

Подробнее
15-05-2006 дата публикации

VERFAHREN ZUR ENTNAHME VON WÄRME BEI UMGEBUNGSTEMPERATUR

Номер: AT0000413734B
Принадлежит:

A novel method converts heat into mechanical work. In a cyclic process, a working medium is compressed while giving off heat and it is subsequently brought in thermal contact with the surroundings via a first heat exchanger. Then it is expanded while obtaining mechanical work, whereupon the cyclic process is run through once more. A high degree of efficiency is achieved by virtue of the fact that the working medium, after expansion, is guided through another heat exchanger, which is situated inside a rapidly rotating rotor and which, on the exterior thereof, is surrounded by at least one substantially annular gas space from whose exterior heat is dissipated. There is also disclosed a device for carrying out the novel method.

Подробнее
15-02-2004 дата публикации

WÄRMETAUSCHER

Номер: ATA9872001A
Автор:
Принадлежит:

Подробнее
15-10-1977 дата публикации

PROCEDURE AND DEVICE FOR KUHLEN HIGH TEMPERATURES OF A SUSPENDED MECHANISM

Номер: AT0000030474A
Автор:
Принадлежит:

Подробнее
15-01-1977 дата публикации

DEVICE TO THE SUPPLY OF MATERIALS INTO A ZONE OF HIGH TEMPERATURE

Номер: AT0000575074A
Автор:
Принадлежит:

Подробнее
15-09-2013 дата публикации

Elektrolyseur

Номер: AT0000512537B1
Принадлежит:

Um einen Elektrolyseur zur Erzeugung von Wasserstoff und Sauerstoff sehr flexibel einsetzbar zu machen, wird vorgeschlagen, eine Trocknungseinheit vorzusehen, in der ein mehrkreisiger Wärmetauscher (20) mit einem ersten Kreis zur Kühlung des erzeugten Wasserstoffs (H2) und einem zweiten Kreis zur Kühlung des erzeugten Sauerstoffes (O2) vorgesehen ist, wobei beide Kreise des mehrkreisigen Wärmetauschers (20) einen gemeinsamen Kältekreis (27) aufweisen.

Подробнее
15-03-2014 дата публикации

Wärmetauscher

Номер: AT0000513300A1
Автор: BENZ JOACHIM
Принадлежит:

The heat exchanger (10) comprises a heat transfer tube portion (12) including two heat exchanger tubes (14,16) which are arranged concentrically and between which an annular space (18) for guiding the heat-absorbing medium is formed. The inlet (20) and the outlet (22) communicate with the space, so that the space and the outlet form a closed pipe system. Several baffles (28) are arranged in the space. The inlet and the outlet are arranged in the heat transfer tube portion in traverse form.

Подробнее
15-09-1972 дата публикации

PROCEDURE FOR THE PRODUCTION OF A BUNDLE OF IN DISTANCES ARRANGEMENT CAPILLARIES FOR A DIAPHRAGM CAPILLARY EXCHANGER

Номер: AT0000302252B
Автор:
Принадлежит:

Подробнее
27-09-1971 дата публикации

Hydro-motor with radial driving elements

Номер: AT0000293127B
Автор:
Принадлежит:

Подробнее
14-04-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00036138877B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
04-12-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00039456975B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
21-08-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00034090836B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
08-06-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00035910384B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
26-10-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00035596539B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
12-11-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00037983418B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
24-01-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00034490181B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
10-05-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00039152751B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
15-03-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00039811972B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
13-05-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00034985474B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
14-05-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00035623087B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
26-08-2000 дата публикации

VЕRFАНRЕN ZUR ЕNТNАНМЕ VОN WÄRМЕ ВЕI UМGЕВUNGSТЕМРЕRАТUR

Номер: AT00031730821B
Принадлежит:

А nоvеl mеthоd соnvеrts hеаt intо mесhаniсаl wоrk. In а сусliс prосеss, а wоrking mеdium is соmprеssеd whilе giving оff hеаt аnd it is subsеquеntlу brоught in thеrmаl соntасt with thе surrоundings viа а first hеаt ехсhаngеr. Тhеn it is ехpаndеd whilе оbtаining mесhаniсаl wоrk, whеrеupоn thе сусliс prосеss is run thrоugh оnсе mоrе. А high dеgrее оf еffiсiеnсу is асhiеvеd bу virtuе оf thе fасt thаt thе wоrking mеdium, аftеr ехpаnsiоn, is guidеd thrоugh аnоthеr hеаt ехсhаngеr, whiсh is situаtеd insidе а rаpidlу rоtаting rоtоr аnd whiсh, оn thе ехtеriоr thеrеоf, is surrоundеd bу аt lеаst оnе substаntiаllу аnnulаr gаs spасе frоm whоsе ехtеriоr hеаt is dissipаtеd. Тhеrе is аlsо disсlоsеd а dеviсе fоr саrrуing оut thе nоvеl mеthоd.

Подробнее
14-02-1984 дата публикации

RECUPERATOR WITH FLOATING INTERIOR HOUSING

Номер: CA1162185A
Принадлежит: MIDLAND ROSS CORP, MIDLAND-ROSS CORPORATION

A metal recuperator is described as having an exterior casing with a replaceable inner housing which forms with the casing a pair of separated fluid passageways through which two fluids, at different temperatures, are circulated into heat exchanging relationship. Special seals are provided to allow relative movement between the casing and the housing while sealing the passageways from each other and the ambient atmosphere.

Подробнее
16-08-2001 дата публикации

TREATMENT OF FLUOROCARBON FEEDSTOCKS

Номер: CA0002398464A1
Принадлежит:

A method of treating a fluorocarbon feedstock includes heating, by means of radio frequency induction, a heating zone to a high temperature, allowing a fluorocarbon feedstock, comprising at least one fluorocarbon compound, to heat up in the heating zone so that the fluorocarbon compound dissociates into at least one fluorocarbon precursor or reactive species, and cooling the fluorocarbon precursor or reactive species, thereby forming, from the fluorocarbon precursor or reactive species, at least one more desired fluorocarbon compound.

Подробнее
14-02-1984 дата публикации

RECUPERATOR WITH FLOATING INTERIOR HOUSING

Номер: CA0001162185A1
Автор: SARVIS ROBERT E
Принадлежит:

Подробнее
05-12-2002 дата публикации

HEAT TRANSFER OPTIMIZATION IN MULTISHELL REFORMER

Номер: CA0002448776A1
Принадлежит:

A hydrocarbon fuel processing reactor for generating a hydrogen-enriched reformate from hydrocarbons is disclosed. A plurality of shells (36,46,56,66,76) are arranged coaxially having a gap defined between each of the successive shells, thereby forming a plurality of coaxial zones. The shells are configured to permit heat transfer from one zone to another. Fluid streams for reactions within the reactor are preheated by heat transfer from adjacent zones.

Подробнее
01-03-2018 дата публикации

METHOD AND ASSEMBLY FOR ASEPTICALLY HEATING A LIQUID PRODUCT IN A HEAT EXCHANGER UNIT OF THE HEATER ZONE OF A UHT SYSTEM

Номер: CA0003034302A1
Принадлежит: RIDOUT & MAYBEE LLP

The invention relates to a method for aseptically heating a liquid product (P) in a heat exchanger unit (22) of the heater zone of an assembly (20) in a UHT system according to the preamble of the sub-claims 1 or 2. The aim of the invention is to provide a method of the generic type, an assembly for carrying out the method, and a heat exchanger unit for said assembly which reduces the product fouling in the regions adjoining the product input of the heat exchanger unit and additionally overall when treating the liquid products. According to one embodiment of the method, this is achieved by the following method steps among others: (A1) measuring discrete product temperatures (TP; TP1 to TPn) at specified measurement points (22.3) in the product flow (FP); (C) measuring a product-specific temperature curve (TP(Ix)) between the product output (AP) and the product input (EP) at the specified measurement points (22.3); (D1) comparing the temperature curves of method steps (A1) and (C) and calculating ...

Подробнее
18-05-2021 дата публикации

METHOD AND ASSEMBLY FOR ASEPTICALLY HEATING A LIQUID PRODUCT IN A HEAT EXCHANGER UNIT OF THE HEATER ZONE OF A UHT SYSTEM

Номер: CA3034302C
Принадлежит: GEA TDS GMBH

The invention relates to a method for aseptically heating a liquid product (P) in a heat exchanger unit (22) of the heater zone of an assembly (20) in a UHT system according to the preamble of the sub-claims 1 or 2. The aim of the invention is to provide a method of the generic type, an assembly for carrying out the method, and a heat exchanger unit for said assembly which reduces the product fouling in the regions adjoining the product input of the heat exchanger unit and additionally overall when treating the liquid products. According to one embodiment of the method, this is achieved by the following method steps among others: (A1) measuring discrete product temperatures (TP; TP1 to TPn) at specified measurement points (22.3) in the product flow (FP); (C) measuring a product-specific temperature curve (TP(Ix)) between the product output (AP) and the product input (EP) at the specified measurement points (22.3); (D1) comparing the temperature curves of method steps (A1) and (C) and calculating ...

Подробнее
26-08-2010 дата публикации

ELECTROLYTIC CELL AND METHOD OF USE THEREOF

Номер: CA0002752825A1
Принадлежит:

In one embodiment of the present invention an electrolytic cell is provided comprising a containment vessel; a first electrode; a second electrode; a source of electrical current in electrical communication with the first electrode and the second electrode; an electrolyte in fluid communication with the first electrode and the second electrode; a gas, wherein the gas is formed during electrolysis at or near the first electrode; and a separator; wherein the separator includes an inclined surface to direct flow of the electrolyte and the gas due to a difference between density of the electrolyte and the combined density of the electrolyte and the gas such that the gas substantially flows in a direction distal to the second electrode.

Подробнее
31-01-1971 дата публикации

Doppelmanteliger, rohrförmiger Wärmeaustauscher

Номер: CH0000502569A
Принадлежит: ESCHER WYSS GMBH

Подробнее
31-01-1971 дата публикации

Hydromotor

Номер: CH0000502509A
Принадлежит: RIVA CALZONI SPA, RIVA CALZONI S. P. A.

Подробнее
31-10-1968 дата публикации

Elément d'échange de chaleur

Номер: CH0000464259A

Подробнее
15-03-1966 дата публикации

Echangeur thermique pour fluides, comprenant des cylindres concentriques

Номер: CH0000408979A
Принадлежит: LECLERCQ PIERRE, LECLERCQ,PIERRE

Подробнее
15-06-1972 дата публикации

Multiple countercurrent exchanger

Номер: CH0000524122A
Принадлежит: CIBA GEIGY AG, CIBA-GEIGY AG

A multiple countercurrent exchanger comprises a casing, a bundle of tubes in the casting, two end walls in one of which walls the one end of the bundle of tubes is fastened, while the other end of the bundle is fastened in the other wall, the tubes of the bundle having orifices on the outward sides of the end walls; a chamber containing the bundle therein extending between the two end walls; an arrangement for charging the tube openings on one end of the bundle with a first fluid and for removing the latter from the tube openings at the other end of the bundle, as well as inlet means and outlet means for the passage of a second fluid through the chamber; and inset consisting of a plurality of walls forming between them a plurality of individual tubular channels being open at both ends, the inset being fastened in such a manner in the chamber that through the interior of each of the individual tubular channels there passes at least one of the tubes, while in the zones of the interior of ...

Подробнее
29-04-1977 дата публикации

Номер: CH0000587463A5
Автор:

Подробнее
14-10-1977 дата публикации

Номер: CH0000591889A5
Автор:
Принадлежит: AGFA GEVAERT AG, AGFA-GEVAERT AG

Подробнее
31-08-1978 дата публикации

Номер: CH0000604117A5
Принадлежит: BORG WARNER, BORG-WARNER CORP.

Подробнее
31-05-1978 дата публикации

Номер: CH0000599521A5
Принадлежит: SULZER AG, SULZER (GEBRUEDER) AG

Подробнее
14-07-1978 дата публикации

Номер: CH0000601761A5
Принадлежит: FRYMA MASCH AG, FRYMA-MASCHINEN AG

Подробнее
30-09-1987 дата публикации

WAERMETAU.

Номер: CH0000662411A5
Автор: MEIER, RENE
Принадлежит: MENTEC AG

Подробнее
15-10-2009 дата публикации

Heat exchanger fitted with thermal solar collector comprises inner pipe, through which stale air is removed, fresh air being fed in through space between it and second pipe, allowing transfer of heat from stale air and from collector

Номер: CH0000698750B1
Автор: SCHLATTER GEORGES
Принадлежит: SCHLATTER GEORGES, GEORGES SCHLATTER

Heat exchanger fitted with a thermal solar collector comprises three coaxial pipes. Stale air is removed via the inner pipe (01) and fresh air is fed in through the annular space between it and a second pipe (02), allowing transfer of heat from the stale air and from the solar collector. The outer pipe (03) is transparent.

Подробнее
31-10-2013 дата публикации

Heat exchanger for use in e.g. central heating system, has a heat transfer tube portion including two heat exchanger tubes which are arranged concentrically and between which an annular space for guiding heat-absorbing medium is formed

Номер: CH0000706383A2
Автор: BENZ JOACHIM [DE]
Принадлежит:

The heat exchanger (10) comprises a heat transfer tube portion (12) including two heat exchanger tubes (14,16) which are arranged concentrically and between which an annular space (18) for guiding the heat-absorbing medium is formed. The inlet (20) and the outlet (22) communicate with the space, so that the space and the outlet form a closed pipe system. Several baffles (28) are arranged in the space. The inlet and the outlet are arranged in the heat transfer tube portion in traverse form.

Подробнее
30-06-2014 дата публикации

Heat exchanger for using the waste heat in flue gases and exhaust gases.

Номер: CH0000706383B1
Автор: BENZ JOACHIM, JOACHIM BENZ
Принадлежит: BENZ JOACHIM, JOACHIM BENZ

Ein Wärmetauscher zum Einsetzen in einen von einem Wärmeträger durchströmten Rohrabschnitt umfasst ein erstes und ein zweites Rohr (114, 116), die konzentrisch angeordnet sind und die zwischen sich einen ersten Ringraum (118) zur Führung des wärmeaufnehmenden Mediums ausbilden, einen ersten Zulauf (120) und einen ersten Ablauf (122) in dem ersten Rohr (114) für das wärmeaufnehmende Medium, wobei der erste Zulauf (120) und der erste Ablauf (122) mit dem ersten Ringraum (118) kommunizieren, so dass der erste Ringraum (118) und der erste Ablauf (122) ein Leitungssystem für das wärmeaufnehmende Medium bilden, und Umlenkschikanen, die in dem ersten Ringraum vorgesehen sein können.

Подробнее
30-09-2013 дата публикации

BOILER - UTILIZER

Номер: EA0201390473A1
Автор:
Принадлежит:

Подробнее
26-12-2019 дата публикации

HEAT TRANSFER PIPE AND BOILER COMPRISING ONE SUCH HEAT TRANSFER PIPE

Номер: UA0000120547C2
Автор:
Принадлежит:

Подробнее
11-09-1987 дата публикации

Gas-layer heat exchanger

Номер: FR0002595459A1
Принадлежит:

Подробнее
26-05-1978 дата публикации

PROCEDE DE FABRICATION D'UN ECHANGEUR DE CHALEUR A TUBES CONCENTRIQUES

Номер: FR0002369034A
Принадлежит:

Procédé simple et rapide de fabrication d'un échangeur de chaleur à tubes concentriques. Il comprend l'application aux tubes 20, 22, d'une force de déformation dirigée radialement d'intensité suffisante pour fournir une déformation permanente. Application à la fabrication d'échangeur de chaleur carburant-huile pour moteur à turbine à gaz.

Подробнее
10-08-2007 дата публикации

TOGETHER OF CONDITIONING AND DISTRIBUTION Of a PRODUCT

Номер: FR0002885495B1
Автор: LASSERRE, SANCHEZ
Принадлежит: L'OREAL

Подробнее
08-03-1950 дата публикации

Номер: FR0000958391A
Автор:
Принадлежит:

Подробнее
08-01-1954 дата публикации

exchanger of heat

Номер: FR0001050648A
Автор:
Принадлежит:

Подробнее
17-07-1961 дата публикации

heat exchanger

Номер: FR0001266823A
Автор:
Принадлежит:

Подробнее
08-07-1966 дата публикации

exchanger of heat to encasable elements

Номер: FR0001444936A
Автор:
Принадлежит:

Подробнее
28-11-2014 дата публикации

PREHEATING HEAT EXCHANGER FOR FUEL CELL

Номер: FR0002921718B1
Принадлежит: SNECMA

Подробнее
29-10-1976 дата публикации

IMPROVEMENTS WITH THE APPARATUSES OF COOLING OF LIQUIDS

Номер: FR0002306421A1
Автор:
Принадлежит:

Подробнее
26-05-1978 дата публикации

IMPROVEMENTS WITH THE EXCHANGERS OF HEAT, IN PARTICULAR FOR THE HEATING OF MOTOR VEHICLES

Номер: FR0002369528A1
Автор:
Принадлежит:

Подробнее
17-10-1975 дата публикации

Vertical tube water heater - has two interfitting sets of peripheral tubes bent top and bottom for support

Номер: FR0002265052A2
Автор:
Принадлежит:

Подробнее
21-06-1963 дата публикации

exchanger of heat

Номер: FR0001330305A
Автор:
Принадлежит:

Подробнее
06-10-1989 дата публикации

FUEL COOLING AGENT

Номер: FR0002608683B3
Принадлежит:

Подробнее
16-05-2019 дата публикации

Устройство трубы для теплообменных аппаратов

Номер: RU0000189235U1

Полезная модель относится к теплообменным устройствам, а точнее к элементу зоны теплообмена в теплообменных аппаратах типа труба в трубе, и может быть использовано в энергетике и транспорте, в частности в судовых теплообменных устройствах.Задачей полезной модели является расширение возможностей для увеличения массовой скорости теплообмена. Технический результат заключается в реализации этого назначения за счет возможности расслоения потоков «целевой» и «вспомогательной» жидкостей и создавая при этом чередование каналов в радиальном направлении для протекания слоев «целевой» жидкости и «вспомогательной» жидкости, приводящее к формированию дополнительных поверхностей для теплообмена в толще «целевой» и «вспомогательной» жидкостей, что способствует увеличению скорости отвода тепла из массы «целевой» жидкости за счет теплопроводности.Определенная таким образом задача решается тем, что в отличие от известного устройства промежуточной трубы для зоны теплообмена теплообменных аппаратов, содержащей две соосные тонкостенные цилиндрические формы, имеющие разные диаметры, жестко и герметично соединенные с перемычками, образовывая стенки со сквозными полостями, причем перемычки имеют выступание за пределы внутренней и внешней поверхностей полой стенки трубы, образуя ребра на обеих ее поверхностях, предлагается устройство промежуточной трубы, включающее по крайней мере две трубы, каждая из которых имеет сквозные полости в стенке и ребра, выступающие за пределы внутренней и внешней поверхностей этой стенки, расположенные соосно. Трубы с полыми стенками имеют жесткое и герметичное соединение с кольцевыми перемычками, установленными с торцевых сторон этих труб и формирующими равномерный зазор между ними. В полой стенке каждой из труб между тонкостенными цилиндрическими формами введены патрубки, жестко и герметично соединенные с обеими цилиндрическими формами, формируя радиальные сквозные отверстия в полых стенках, причем эти отверстия размещают вблизи торцевых сторон труб. ...

Подробнее
19-01-2012 дата публикации

Annular Axial Flow Ribbed Heat Exchanger

Номер: US20120012289A1
Автор: Michael Andrew Martin
Принадлежит: Dana Canada Corp

A cylindrical, annular axial flow heat exchanger for use as a gas cooler in a thermal regenerative machine such as a Stirling engine is provided. The heat exchanger includes an outer shell of sufficient strength and thickness to withstand the pressure exerted by the working fluid and a tubular member positioned adjacent to and in contact with the outer shell, the tubular member having spaced apart sidewalls defining a flow passage therebetween. At least one of the sidewalls of the tubular member is embossed with ribs, the ribs being in contact with the inner surface of the outer shell thereby defining axially extending flow passages between the outer shell and tubular member along the circumference thereof for the flow of a second, gaseous fluid through the heat exchanger. The first fluid flows circumferentially through tubular member, while the second fluid flows axially between the outer shell and the tubular member.

Подробнее
27-09-2012 дата публикации

Thermal Gradient Hydroelectric Power System and Method

Номер: US20120240576A1
Принадлежит: Rowland Xavier Johnson

A thermal gradient hydroelectric power system and method is disclosed herein. Specifically, the method can comprise cycling through a submersed evaporator warm from a natural warm water source, said warm water source having a first temperature. The method also can comprise evaporating a working fluid using said evaporator, and routing the working fluid from the evaporator through a vapor line to a condenser above said evaporator. Finally, the method can also comprise cycling through a condenser cold water from a natural cold water source, the cold water source having a second temperature, and condensing the working fluid, the working fluid having a boiling point between said first temperature and said second temperature.

Подробнее
09-05-2013 дата публикации

HEAT EXCHANGER

Номер: US20130112380A1
Автор: TANIGAWA Shigetoshi
Принадлежит:

The heat exchanger uses multi-layer tubes, performing efficient heat exchange. Each heat transfer tube includes an outer tube and an inner tube. Header unit directs first fluid through gaps between the inner tube and the outer tube from outer circumferences of the inner tube. The header units are stacked in a top-bottom direction with gap-forming members therebetween, leaving predetermined gap portion. Furthermore, a header cover directs the second fluid through the inner tubes extending from the header units, and is fitted from the outer side, and the second fluid is introduced. With this configuration, the second fluid flowing from the header cover is directed through the inside of the inner tubes and over outer surfaces of the outer tubes along the axial direction via the gap portions, enabling heat exchange to be performed from both inside and outside of the outer tubes. 1. A heat exchanger using heat transfer tubes each including an outer tube and an inner tube , the heat exchanger performing heat exchange between first fluid flowing through a gap between the outer tube and the inner tube and second fluid flowing through the inner tube , the heat exchanger comprising:header units that direct the first fluid through the gaps between the inner tubes and the outer tubes from the outer circumferences of the inner tubes, the ends of the inner tubes extending from the outer tubes;second headers that direct second fluid through the inner tubes extending from the header units; andgap portions provided between the stacked header units, through which the second fluid from the second headers flows,wherein the second fluid from the second headers is directed through the inside of the inner tubes and over outer surfaces of the outer tubes along the axial direction via the gap portions.2. A heat exchanger using heat transfer tubes each including an outer tube and an inner tube , the heat exchanger performing heat exchange between first fluid flowing through a gap between the ...

Подробнее
09-05-2013 дата публикации

HEAT EXCHANGE DEVICE WITH IMPROVED SYSTEM FOR DISTRIBUTING COOLANT FLUID

Номер: US20130112381A1
Автор: Valente Piero
Принадлежит: ALFA LAVAL CORPORATE AB

A heat exchange device comprises plural tubes arranged parallel to one another to form one or more tube bundles inserted axially in a cylindrical shell. A first fluid supplied through one or more first inlet holes at a first end of the cylindrical shell and oriented axially, flows inside the tubes and a second fluid, supplied through a second inlet hole, flows inside the cylindrical shell to effect heat transfer with the first fluid through the tube walls. One end of the tubes is connected to a tube plate at first inlet hole(s), which separates the second fluid from the first fluid. At least two impingement plates, each provided with plural through holes, are placed in succession between each first inlet hole and the tube plate. The impingement plates are parallel to one another and orthogonal to the cylindrical shell central axis to distribute the first fluid inside the tubes. 1. Heat exchange device comprising a plurality of tubes arranged parallel one to the other in order to form one or more tube bundles inserted axially in a cylindrical shell , a first fluid , supplied through one or more first inlet holes located at a first end of the cylindrical shell and oriented axially , flowing inside the tubes and a second fluid , supplied through a second inlet hole , flowing inside said cylindrical shell in order to carry out the heat transfer with the first fluid through the walls of the tubes , a first end of the tubes being connected to a tube plate located at said one or more first inlet holes , separating the second fluid from the first fluid , wherein between each first inlet hole of the first fluid and the tube plate at least two impingement plates are placed in succession , each of them provided with a plurality of through holes , said impingement plates being disposed parallel one to the other and orthogonally as regards the central axis of the cylindrical shell to distribute in the most uniform way the first fluid inside the tubes.234343434. Heat exchange ...

Подробнее
04-07-2013 дата публикации

Exhaust gas system with circulation heat pipe

Номер: US20130167517A1
Принадлежит: Benteler Automobiltechnik GmbH

An exhaust gas system includes an exhaust gas pipe with an integrated evaporator. In order to make the evaporator independent of the site of installation and the mounting position, a capillary structure is arranged between the outer sleeve pipe and the exhaust gas pipe. For increasing the efficiency of the evaporator, vapor grooves are provided in an area of an outer sheath surface of the exhaust gas pipe and fluid grooves are provided in an area of an inner mantle surface of the sleeve pipe.

Подробнее
18-07-2013 дата публикации

WASTE HEAT BOILER

Номер: US20130180475A1
Принадлежит:

A waste heat boiler has heat exchange tubes for indirect heat exchange of a relatively hot process gas and a cooling media, and a by-pass tube for by-passing a part of the process gas; a process gas collector collects and mixes a part of the heat exchanged process gas and at least a part of the by-passed process gas before the mix is lead via a control valve to the process gas outlet of the waste heat boiler together with the rest of the heat exchanged process gas. 2. Waste heat boiler according to claim 1 , wherein the outlet process gas collector further comprises mixing means located upstream of the control valve claim 1 , for mixing the relatively hot process gas exiting the at least one by-pass tube with the cooled process gas exiting a part of the heat exchange tubes.3. Waste heat boiler according to claim 1 , comprising one by-pass tube claim 1 , wherein the outlet process gas collector collects the process gas exiting the bypass tube gas and the exiting process gas of at least one of the heat exchange tubes.4. Waste heat boiler according to claim 1 , wherein the process gas inlet section is lined with a ceramic liner.5. Waste heat boiler according to claim 4 , wherein further the inside wall of the bypass tube is lined and at least part of the outlet process gas collector is lined with a ceramic liner .6. Waste heat boiler according to claim 1 , wherein the cooling media is water or steam or both water and steam.7. Waste heat boiler according to claim 1 , wherein said shell has a substantially cylindrical shape and said at least two tube sheets have a substantially circular shape.8. Waste heat boiler according to any claim 1 , wherein said heat exchange tubes are arranged in a circular array in the tube sheets and said by-pass tube is arranged substantially in the center of said array.9. Process for heat exchanging a relatively hot process gas with a cooling media in a waste heat boiler according to any of the preceding claims comprising the steps of claim 1 ...

Подробнее
22-08-2013 дата публикации

Annular Heat Exchanger

Номер: US20130213017A1
Принадлежит: Dana Canada Corp

An annular heat exchanger for cooling hot gases comprises an inner shell, an intermediate shell and an outer shell. Where the heat exchanger is integrated with a catalytic converter for treatment of hot exhaust gases in a motor vehicle, the inner shell contains a catalyst for treatment of the exhaust gases. Inner and outer gas flow passages are provided between the shells, and a coolant flow passage is provided, either on the outer surface of the outer shell, or inbetween the intermediate and outer shells. The exhaust gases change direction twice as they pass through the heat exchanger, and the annular structure of the heat exchanger provides a large surface area, and a large flow section, relative to volume, and thereby provides effective heat exchange without significantly increasing space requirements.

Подробнее
22-08-2013 дата публикации

HEAT EXCHANGER ELEMENT

Номер: US20130213620A1
Принадлежит: NGK Insulators, Ltd.

There is provided a heat exchanger element having a cylindrical outer peripheral wall and partition walls which are made mainly of SiC and form a plurality of cells functioning as passages for a first fluid inside the outer peripheral wall. More specifically, in the heat exchanger element, the outer peripheral wail and the partition wails mediate heat exchange between the first fluid and the second fluid, and the thickness T of the outer peripheral wall, the equivalent circle diameter D calculated from the area of the portion inside the outer peripheral wall in a cross section perpendicular to an axial direction of the outer peripheral wall, and thickness t of the partition walls satisfy the following formulae (1) to (3): Formula (1): 0.3 mm≦T≦4.0 mm, Formula (2): 15 mm≦D≦120 mm, and Formula (3): 0.04×T≦t≦0.6 mm. 1. A heat exchanger element comprising:a cylindrical outer peripheral wall made of ceramic containing SiC as a main component, andpartition walls which are made of ceramic containing SiC as a main component and separate and form a plurality of cells functioning as passages for a first fluid in a portion inside the outer peripheral wall;wherein the outer peripheral wall and the partition walls mediate heat exchange between the first fluid flowing through the portion inside the outer peripheral wall and the second fluid flowing through the portion outside the outer peripheral wall, and [{'br': None, '0.3 mm≦T≦4.0 mm \u2003\u2003Formula (1)'}, {'br': None, '15 mm≦D≦120 mm \u2003\u2003Formula (2)'}, {'br': None, 'i': '×T≦t≦', '0.040.6 mm. \u2003\u2003Formula (3)'}], 'the thickness T of the outer peripheral wall, the equivalent circle diameter D calculated from the area of the portion inside the outer peripheral wall in a cross section perpendicular to an axial direction of the outer peripheral wall, and thickness t of the partition walls satisfy the following formulae (1) to (3)2. The heat exchanger element according to claim 1 , wherein the thickness T of the ...

Подробнее
27-02-2014 дата публикации

Structure of Exhaust Pipe for Exhaust Heat Recovery

Номер: US20140054008A1
Автор: Ki Chul Park
Принадлежит: Hyundai Motor Co

An exhaust pipe heats coolant with heat of exhaust gas. The structure of the exhaust pipe can increase heat exchange efficiency because a flow direction of the coolant is arranged to be opposite to a flow direction of the exhaust gas. The coolant can smoothly flow inside the housing, because density of the coolant decreases as the coolant is heated while flowing in a lower side of the housing and flowing out of an upper side of the housing. In addition, the heat transfer pipe of which one surface is in contact with the exhaust gas and the other side is in contact with the coolant has wrinkle portions which are formed on a surface of the heat transfer pipe, where heat exchange is performed, and thereby, a heat exchange area can be increased and the coolant can be more rapidly heated without increasing a size of the housing.

Подробнее
12-01-2017 дата публикации

Heat Exchanger Floating Head Manipulation Device

Номер: US20170010057A1
Автор: Griffis, JR. David E.
Принадлежит:

A device for the manipulation of a floating head between secured and removed positions relative to a heat exchanger housing, and for suspension of the floating head between said positions as heat exchanging tubes are replaced or cleaned. The floating head has holding means such as a ring welded to the exterior for affixation of a lifting member, such as a chain, of a lifting means, such as a crane. The device comprises an elongated body having first and second opposed ends. The body has at least one opening for selective receipt of means for attaching the body to the holding means, whereby when the device is affixed to the floating head, the floating head may be manipulated and suspended at a pre-selected degree, such as approximately a 90 degree angle relative to the heat exchanger. A spinal projection extends from one end of the device body and is offset relative to the body at a pre-selected degree, such as approximately a 45 degree angle. A securing member is provided on the projection for selective receipt of the lifting member. 1) A device for the manipulation of a floating head between secured and removed positions relative to a heat exchanger housing , said floating head having holding means on the exterior thereof for affixation of a lifting member of a lifting means , comprising:(a) An elongated body having first and second opposed ends, said body having at least one opening there through for selective receipt of means for attaching said elongated body to said holding means on said floating head, whereby when the device is affixed to the floating head, said floating head may be manipulated and suspended at a pre-selected degree angle relative to said heat exchanger;(b) a spinal projection extending from one end of said device body and offset relative to said body at approximately a 45 degree angle and including a spinal opening there through; and(c) a securing member received within said spinal opening on said projection for selective receipt of said ...

Подробнее
10-01-2019 дата публикации

HEAT EXCHANGERS

Номер: US20190011199A1
Автор: Turney Joseph
Принадлежит:

A counter-flow heat exchanger comprising a heat exchanger core including an inner wall and an outer wall radially outward and spaced apart from the inner wall. A first flow path is defined within the inner wall and a second flow path is defined between the inner wall and the outer wall. The heat exchanger core includes a primary flow inlet, a primary flow outlet and a middle portion therebetween. The inner and outer walls are concentric at the primary flow inlet of the heat exchanger core. The inner wall defines a first set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core diverging away from a radial center of the heat exchanger core. The inner wall and the outer wall define a second set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core converging toward the radial center of the heat exchanger core. 1. A method of manufacturing a counter-flow heat exchanger core , the method comprising:forming a heat exchanger core body using additive manufacturing, wherein the heat exchanger core body includes an inner wall and an outer wall radially outward and spaced apart from the inner wall, wherein a first flow path is defined within the inner wall and a second flow path is defined between the inner wall and the outer wall, wherein the heat exchanger core body includes a primary flow inlet, a primary flow outlet and a middle portion therebetween, wherein the inner and outer walls are concentric at the primary flow inlet of the heat exchanger core body, wherein the inner wall defines a first set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core body diverging away from a radial center of the heat exchanger core body, and wherein the inner wall and the outer wall define a second set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core body converging toward ...

Подробнее
19-01-2017 дата публикации

Heat exchange structure of power generation facility

Номер: US20170016201A1
Принадлежит: Chugoku Electric Power Co Inc

A heat exchange structure of a power generation facility including a piping system that is embedded in a reinforced concrete underground structure that is integrally formed with the power generation facility, and a heat medium that is fluid and is stored in the piping system. The piping system circulates the heat medium used for heat exchange in the power generation facility.

Подробнее
19-01-2017 дата публикации

METHOD AND DEVICE FOR CLEANING TUBE BUNDLES

Номер: US20170016687A1
Принадлежит: LOBBE INDUSTRIESERVICE GMBH & CO KG

A method for cleaning tube bundles with open end faces, in particular tube bundles of heat exchangers, air coolers, or condensers. A cleaning device which has at least one cleaning unit is positioned adjacently to the open ends of the tube bundle, and the at least one cleaning unit which has a high-pressure hose is then arranged in a successive manner by a controller so as to be flush with the respective tube of the tube bundle. The cleaning unit is inserted into the respective tube and supplied with a liquid under high-pressure. The aim of the invention is to improve such a method and device such that a reliable cleaning process is carried out without operating errors. This is achieved in that the insert depth is measured when inserting the at least one cleaning unit into the respective tube and monitored by the controller. 1. A method for cleaning of tube bundles with open end faces , especially tube bundles of heat exchangers , air coolers or condensers , comprising the steps of: positioning a cleaning device having at least one cleaning unit adjacent to the open ends of the tube bundle and then arranging the cleaning unit comprising at least one high-pressure hose by a control unit successively flush with a particular tube of the tube bundle and inserting the cleaning unit into the particular tube and supplying the cleaning unit with a liquid under high pressure , wherein during the inserting of the at least one cleaning unit into the respective tube a depth of insertion is measured and monitored by the control unit.2. The method according to claim 1 , wherein the particular depth of insertion is saved in the control unit or in a storage and documentation unit connected to the control unit and documented for the particular cleaning process.3. The method according to claim 2 , wherein the documentation involves the construction of a three-dimensional fouling profile of the tube bundle.44. The method according to claim 1 , wherein a cleaning device has several ...

Подробнее
26-01-2017 дата публикации

COMPLIANT HEATING SYSTEM COMPRISING A COMPRESSIVE SEAL EXPANSION JOINT

Номер: US20170023316A1
Принадлежит:

A compliant heating system includes a dynamic component including a heat exchanger; a pressure vessel shell encompassing at least a portion of the heat exchanger; and a compressive seal expansion that connects the dynamic component and the pressure vessel shell. 1. A compliant heating system , comprising:a dynamic component comprising a heat exchanger;a pressure vessel shell encompassing at least a portion of the heat exchanger; anda compressive seal expansion joint that connects the dynamic component and the pressure vessel shell.2. The compliant heating system of claim 1 , wherein a thermal expansion of the dynamic component and a thermal expansion of the pressure vessel when the heat exchanger exchanges heat are different.3. The compliant heating system of claim 1 ,wherein the pressure vessel shell further comprises a pressure vessel shell conduit, andwherein the compressive seal expansion joint comprises a conduit compressive seal expansion joint disposed on the pressure vessel shell conduit.4. The compliant heating system of claim 3 ,wherein the pressure vessel shell conduit is disposed along an axial axis and on an end of the pressure vessel shell,wherein the dynamic component further comprises an exhaust plenum, which is disposed on an end of the heat exchanger,wherein the exhaust plenum is connected to an exhaust gas port that axially extends through the pressure vessel shell conduit, andwherein the exhaust gas port is connected to the pressure vessel shell conduit via the conduit compressive seal expansion joint.5. The compliant heating system of claim 3 ,wherein the pressure vessel shell conduit comprises a pressure vessel flange,wherein the pressure vessel flange is connected to a combustion gas exhaust port flange via the conduit compressive seal expansion joint, andwherein the combustion gas exhaust port flange is rigidly attached to an exhaust port via a connection flange.6. The compliant heating system of claim 3 ,wherein the pressure vessel shell ...

Подробнее
01-05-2014 дата публикации

HEAT EXCHANGER

Номер: US20140116663A1
Принадлежит: TAIYO NIPPON SANSO CORPORATION

Provided is a heat exchanger in which heat exchange between a low-temperature cooling medium and brine and heat exchange between brine and hydrogen gas can be efficiently performed and downsizing of cooling facilities or reduction in facility cost can be attained. The heat exchanger comprises: a vacuum insulated container 12 which is filled with brine, a lid 13 closing an upper portion opening of the container, a rotation axis 14 arranged in the axis direction of the container, a propeller 15 provided on the rotation axis, a helical hydrogen gas cooling tube 16, 17 provided in a vertically two-stage structure around the rotation axis and the propeller, and a cooling medium tube 18 for cooling brine which is arranged around the hydrogen gas cooling tubes. 1. A heat exchanger which cools hydrogen gas with brine cooled by a low-temperature cooling medium characterized by comprising:a vacuum insulated container with which brine is filled;a lid which closes the upper portion opening of the container;a rotation axis arranged in the axis direction of the container;a propeller provided along the rotation axis;a helical hydrogen gas cooling tube arranged around the rotation axis and the propeller; anda cooling medium tube for cooling brine arranged around the hydrogen gas cooling tube.2. The heat exchanger according to claim 1 , wherein the hydrogen gas cooling tube is provided with a plurality of hydrogen gas cooling tubes having a vertically multistage structure.3. The heat exchanger according to claim 1 , wherein the upper end and the lower end of the cooling medium tube are communicatively connected to an annular upper portion manifold and an annular lower portion manifold claim 1 , respectively claim 1 , and a cooling medium is circulated in the cooling medium tube from the lower end to the upper end direction.4. The heat exchanger according to claim 1 , wherein a gas-phase portion between the inner surface of the lid and the liquid surface of brine in the container is ...

Подробнее
12-02-2015 дата публикации

Heat Exchanger for an Oxygenator and Method for Producing Such a Heat Exchanger

Номер: US20150041107A1
Принадлежит:

A heat exchanger for an oxygenator comprises multiple tube sections, each having a longitudinal tube axis, wherein the tube sections are disposed as a bundle having a longitudinal bundle axis, and the tube sections are connected to each other in at least one connecting section of the bundle by joining by way of chemical and/or physical bonded joints. A method for producing the heat exchanger is also provided. 1. A heat exchanger for an oxygenator , comprising:multiple tube sections disposed as a bundle having a longitudinal bundle axis with each one of the individual tube sections a longitudinal tube axis; andthe multiple tube sections connected to each other in at least one connecting section of the bundle by joining by way of chemical and/or physical bonded joints; andwherein the bundle (a) is comprised of individual tube sections connected to each other by adhesive bonding forming a tube bundle that is dimensionally stable, (b) is disposed in a housing and having a pair of connecting sections at opposite ends of the bundle, and (c) is adhesively bonded at each one of the connecting sections and the housing.2. The heat exchanger according to claim 1 , wherein the tube sections are made of plastic.3. The heat exchanger according to claim 1 , wherein the longitudinal tube axes form an angle with the longitudinal bundle axis which is greater than 10°.4. The heat exchanger according to claim 1 , wherein the longitudinal tube axes of the tubes of the bundle extend non-linearly.5. The heat exchanger according to any claim 1 , wherein the bundle is disposed at least sectionally in the housing.6. The heat exchanger according to claim 4 , wherein the tubes of the bundle extend curvilinearly.7. The heat exchanger according to claim 3 , wherein the longitudinal tube axes form an angle greater than 20°.8. The heat exchanger according to claim 1 , wherein the bundle is generally cylindrical claim 1 , and has a non-variable cross-sectional surface along the longitudinal bundle ...

Подробнее
09-02-2017 дата публикации

SUPPLY AND EXTRACTION OF TUBE FLOWS AT INTERMEDIATE TEMPERATURE IN HELICALLY COILED HEAT EXCHANGERS

Номер: US20170038149A1
Принадлежит:

A heat exchanger for the indirect exchange of heat between a first fluid and a second fluid, the heat exchanger having a casing surrounding a casing chamber that accommodates the first fluid. A core tube may extend within the casing. A tube bundle is arranged in the casing chamber and has multiple tubes to accommodate the second fluid. The tubes are helically wound around a longitudinal axis of the chamber or around the core tube in a coil region extending from a lower coil end to an upper coil end. At least one tube is coiled only in a section of the coil region. Outside of the section of the coil region the at least one tube extends as a straight tube to the lower coil end, the upper coil end, or to both the lower coil end and the upper coil end. 1. A heat exchanger for the indirect exchange of heat between a first fluid and a second fluid , the heat exchanger comprising:a casing extending along a longitudinal axis and surrounding a casing chamber, the casing chamber for accommodating the first fluid;a tube bundle arranged in the casing chamber, the tube bundle having multiple tubes for accommodating the second fluid;wherein in a coil region extending along the longitudinal axis, the tubes of the tube bundle are helically coiled around the longitudinal axis from a lower coil end to an upper coil end;wherein at least one tube of the tube bundle is coiled around the longitudinal axis in only a section of the coil region; andwherein the at least one tube extends as a straight tube below the section of the coil region along the longitudinal axis to the lower coil end; orwherein the at least one tube extends as a straight tube above the section of the coil region along the longitudinal axis to the upper coil end; orwherein the at least one tube extends as a straight tube below the section of the coil region along the longitudinal axis to the lower coil end and as a straight tube above the section of the coil region along the longitudinal axis to the upper coil end.2. ...

Подробнее
18-02-2021 дата публикации

COOLING TOOL FOR AN EXTRUDER

Номер: US20210046690A1
Принадлежит:

A cooling tool () for a food or an animal feed extruder (E), the cooling tool has: an inlet end () at which extrudate () can be led into the cooling tool (); an outlet end () where the cooled extrudate can be discharged; an extrudate flow channel () extending from the inlet end to the outlet end; and at least one coolant flow channel (′) connected to the extrudate flow channel in a heat-transmitting manner. In a cross section (X-X) along the primary flow direction (), the extrudate flow channel is substantially formed as a ring section; and the outer wall () of the extrudate flow channel () is formed at least from first and second segments (). The first and second segments are connected to each other by mechanical connection elements (). The cooling tool is suitable for wet texturing of food and animal feed. 118-. (canceled)19. A food- or feed-extruder cooling die , havingi) an inlet end, which is able to be fastened to a food or feed extruder and at which the extrudate is introducible into the cooling die;ii) an outlet end, at which cooled extrudate is able to be discharged;iii) an extrudate flow duct, which extends substantially from the inlet end to the outlet end;iv) at least one coolant flow duct, to which the extrudate flow duct is connected for heat transfer;wherein, in a cross section to a main direction of flow,v) the extrudate flow duct is configured substantially as a ring sector; andvi) an outer wall of the extrudate flow duct is formed at least from a first segment and a second segment, wherein the first segment and the second segment are connected together via mechanical connecting elements.20. The cooling die according to claim 19 , wherein the extrudate flow duct is configured in cross section to the main direction of flow substantially as a ring sector claim 19 , in particular as a circular ring sector claim 19 , of at least 300° claim 19 , preferably at least 325° claim 19 , particularly preferably at least 350°.21. The cooling die according to ...

Подробнее
16-02-2017 дата публикации

HEAT EXCHANGER

Номер: US20170045308A1
Принадлежит:

A heat exchanger for an internal combustion engine may include a base tube and a flange extending at least partially around the base tube. The flange may be formed as a forged piece. 1. A heat exchanger for an internal combustion engine , comprising a base tube and a flange extending at least partially around the base tube , wherein the flange is formed as a forged piece.2. The heat exchanger as claimed in claim 1 , wherein the heat exchanger is formed as an exhaust gas heat exchanger.3. The heat exchanger as claimed in claim 1 , wherein the flange is one of welded claim 1 , brazed claim 1 , pressed claim 1 , or adhesively bonded to the base tube.4. The heat exchanger as claimed in claim 1 , wherein the flange is formed as a closed ring.5. The heat exchanger as claimed in claim 1 , wherein the flange has a V-shaped cross section.6. The heat exchanger as claimed in claim 1 , wherein the flange has at least one contact section with which the flange rests flatly on the base tube.7. The heat exchanger as claimed in claim 1 , wherein the base tube has two connecting pieces via which a fluid is led into an interspace delimited by tubes of the base tube and the base tube.8. The heat exchanger as claimed in claim 1 , wherein the flange has a thread.9. The heat exchanger as claimed in claim 1 , wherein a wall thickness t of the flange is in the range of 2 mm≦t≦3.0 mm.10. The heat exchanger as claimed in claim 1 , wherein a wall thickness t of the flange is 2.3 mm.11. A motor vehicle comprising at least one heat exchanger having a base tube and a flange extending at least partially around the base tube claim 1 , wherein the flange is formed as a forged piece.12. The heat exchanger as claimed in claim 2 , wherein the flange is one of welded claim 2 , brazed claim 2 , pressed claim 2 , or adhesively bonded to the base tube.13. The heat exchanger as claimed in claim 2 , wherein the flange is formed as a closed ring.14. The heat exchanger as claimed in claim 2 , wherein the ...

Подробнее
13-02-2020 дата публикации

Heat Exchanger

Номер: US20200049411A1
Принадлежит:

A heat exchanger includes a first flow path through which a first fluid flows, a second flow path through which a second fluid flows, and an adjustment layer disposed between the first flow path and the second flow path adjacent to each other and that adjusts an amount of heat exchange between the first flow path and the second flow path. The adjustment layer includes a first portion and a second portion having a heat transfer performance lower than that of the first portion, and has a heat transfer performance varied depending on a position in the adjustment layer. 110-. (canceled)11. A heat exchanger comprising:a first flow path through which a first fluid flows;a second flow path through which a second fluid flows; andan adjustment layer disposed between the first flow path and the second flow path adjacent to each other and that adjusts an amount of heat exchange between the first flow path and the second flow path; whereinthe first flow path, the second flow path, and the adjustment layer each include a planar flow path layer and are stacked on each other;the adjustment layer includes a first portion and a second portion having a heat transfer performance lower than that of the first portion, and has a heat transfer performance varied depending on a position in the adjustment layer; andthe first portion and the second portion include heat conduction structures that make a connection between the first flow path and the second flow path adjacent to each other and having different heat transfer performances.12. The heat exchanger according to claim 11 , wherein in the adjustment layer claim 11 , the second portion is provided within a predetermined range including a portion that overlaps a vicinity of an inlet or a vicinity of an outlet of the second fluid.13. The heat exchanger according to claim 11 , whereinthe second flow path includes a risk area in which an inner surface temperature of the second flow path is closest to a temperature of the first fluid; andin ...

Подробнее
15-05-2014 дата публикации

HEAT EXCHANGER ARRANGEMENT, ESPECIALLY FOR A VEHICLE HEATER

Номер: US20140131461A1
Автор: HUMBURG Michael

A heat exchanger arrangement, especially for a vehicle heater, includes a pot-like heat exchanger housing () extending in the direction of a longitudinal axis (L) of the housing. The heat exchanger housing includes an outer housing part () with the outer circumferential wall () and with an outer bottom wall () as well as an inner housing part () with the inner circumferential wall () and with an inner bottom wall (). A heat carrier medium flow connecting piece (), open towards the heat carrier medium flow space, is provided at an axial end area () of the outer circumferential wall of the outer housing part, the end area being located at a distance from the outer bottom wall. A waste gas flow connecting piece () is open towards an interior space () of the heat exchanger housing, which interior space is enclosed by the inner wall. 1. A heat exchanger arrangement for a vehicle heater , the heat exchanger arrangement comprising:a pot-shaped heat exchanger housing extending in a direction of a longitudinal axis of the housing, the heat exchanger housing comprising an outer housing part with an outer circumferential wall and with an outer bottom wall and an inner housing part with an inner circumferential wall and with an inner bottom wall, wherein a heat carrier medium flow space is formed between the outer walls and the inner walls;a heat carrier medium flow connecting piece, open towards the heat carrier medium flow space, provided at the outer wall, the heat carrier medium flow connecting piece being provided at an axial end area of the outer circumferential wall of the outer housing part, which said end area is located at a distance from the outer bottom wall; anda waste gas flow connecting piece, open towards an interior space of the heat exchanger housing, which said interior space is surrounded by the inner wall.2. A heat exchanger arrangement in accordance with claim 1 , further comprising another heat carrier medium flow connecting piece claim 1 , such that two ...

Подробнее
05-06-2014 дата публикации

METHOD FOR EXTRACTION HEAT FROM AN EFFLUENT, ESPECIALLY WASTE WATER, CIRCULATING IN A CONDUIT, HEAT EXCHANGER AND MATERIAL FOR IMPLEMENTING SAID METHOD

Номер: US20140151005A1
Автор: DUONG Frédéric
Принадлежит: LYONNAISE DES EAUX FRANCE

The invention relates to a method for extracting heat from an effluent () circulating in a conduit (), especially a waste water collector, according to which a heat exchanger (E) is installed, at least in the bottom of the conduit, said heat exchanger (E) lying in the effluent and being formed by coating tubes () with sufficiently heat-conductive concrete cast around the tubes intended for the circulation of a heat-transfer fluid, the heat exchange with the effluent of the conduit being carried out through the moulded coating. The concrete () of the coating consists of a least 50 weigh % of silicon carbide, a load of needles made of a heat-conductive and mechanically resistant material, a binding agent and the remainder of alumina, metal powder or carbon. 1. A method for extracting heat from an effluent flowing along a pipe , notably a sewer , the method comprising installing , at least in the bottom of the pipe , a heat exchanger (E) which is immersed in the effluent the heat exchanger (E) being formed by coating tubes with a sufficiently thermally conductive concrete poured around tubes through which a heat-transfer fluid is intended to circulate , the exchange of heat with the effluent of the pipe taking place through the cast coating ,wherein the coating concrete is made up of at least 50% by weight of silicon carbides of an acicular filler of needles of a thermally conductive and mechanically strong material, of a binder and the rest being alumina, metallic powder or carbon.2. The method as claimed in claim 1 , wherein the acicular filler of needles represents more than 2% by weight.3. The method as claimed in claim 1 , wherein claim 1 , the needles of the acicular filler are made of metal claim 1 , particularly of carbon steel or of aluminum claim 1 , or are made of carbon.4. The method as claimed in claim 1 , wherein the diameter of the needles is less than five-tenths of a millimeter for a length generally of less than 10 mm.5. The method as claimed in claim ...

Подробнее
19-06-2014 дата публикации

HEAT TRANSFERRING DEVICE AND METHOD FOR MANUFACTURING THE SAME

Номер: US20140166251A1

The disclosure provides a heat transferring device and a method for manufacturing the heat transferring device. The heat transferring device includes: a flexible heat transfer substrate including a first surface, a second surface, at least one solid portion and at least one characteristic hole portion. The at least one solid portion is formed between the first surface and the second surface. The at least one characteristic hole portion includes several characteristic holes penetrating through the first surface and the second surface. The flexible heat transfer substrate further includes: a first end and a second end, and the second end is corresponding to the first end. The flexible heat transfer substrate is rolled from the first end towards the second end to form the heat transferring device with a predetermined shape. 1. A heat transferring device , comprising:a flexible heat transfer substrate comprising a first surface, a second surface, at least one solid portion and at least one characteristic hole portion, wherein the second surface is corresponding to the first surface, the at least one solid portion is formed between the first surface and the second surface, the at least one characteristic hole portion comprises a plurality of characteristic holes penetrating through the first surface and the second surface; the flexible heat transfer substrate further comprising: a first end and a second end, wherein the second end is corresponding to the first end, the flexible heat transfer substrate is rolled from the first end towards the second end to form the heat transferring device with a predetermined shape.2. The heat transferring device according to claim 1 , wherein the flexible heat transfer substrate further comprises a plurality of spacers disposed on the first surface claim 1 , a predetermined distance is formed between the spacers claim 1 , and the spacers are disposed in the at least one solid portion.3. The heat transferring device according to claim 1 ...

Подробнее
28-03-2019 дата публикации

BLOOD PROCESSING UNIT WITH MODIFIED FLOW PATH

Номер: US20190091395A1
Принадлежит:

A blood processing apparatus may include a heat exchanger and a gas exchanger. At least one of the heat exchanger and the gas exchanger may be configured to impart a radial component to blow flow through the heat exchanger and/or gas exchanger. The heat exchanger may be configured to cause blood flow to follow a spiral flow path. 1. A blood processing apparatus comprising:a housing having a blood inlet and a blood outlet, the blood inlet extending into an interior of the housing;a heat exchanger core arranged within the housing and having a core aperture disposed near a first end of the housing such that blood passing from the blood inlet may flow through the core aperture to an exterior of the heat exchanger core;heat exchanger hollow fibers disposed about the heat exchanger core such that a heat exchanger fluid may flow through the heat exchanger hollow fibers and blood passing from the core aperture may flow across the heat exchanger hollow fibers;a cylindrical shell extending coaxially about the heat exchanger core and having an annular shell aperture disposed near a second end of the housing such that blood passing from the core aperture may flow to the annular shell aperture imparting a longitudinal blood flow component to the blood; andgas exchanger hollow fibers disposed about the cylindrical shell such that gases may flow through the gas exchange hollow fibers and blood passing from the annular shell aperture may flow across the gas exchanger hollow fibers.2. The blood processing apparatus of claim 1 , wherein the cylindrical shell includes an inner surface and one or more shell ribs that protrude from the inner surface and extend toward the heat exchanger core claim 1 , the one or more shell ribs configured to impart a shell radial flow component to the blood to deflect the blood away from the inner surface and inward toward the heat exchanger core as the blood passes-from the core aperture to the annular shell aperture.3. The blood processing apparatus of ...

Подробнее
28-03-2019 дата публикации

Heat Exchanger with Annular Coolant Chamber

Номер: US20190093605A1
Принадлежит:

A heat exchanger for cooling heated gas using a liquid coolant includes a tubular housing with one or more intake apertures circumferentially spaced around a coolant distribution portion of the housing. A tube retention cap sealedly engages the front end of the tubular housing, and includes at least one gas tube orifice. An annular coolant chamber surrounds the coolant distribution portion, which distributes liquid coolant around the intake apertures and directs coolant into the cavity and within the tubular housing. Positioned within the tubular housing is at least one elongated gas tube, which is sealedly engaged with the tube orifice. Liquid coolant flowing in, through a coolant inlet, is directed around the annular coolant chamber and distributed into the cavity of the tubular housing, immersing the elongated gas tube and facilitating heat exchange from the heated gas flowing through the elongated gas tubes immersed within the liquid coolant. 1. A heat exchanger for cooling heated gas using liquid coolant , said heat exchanger comprising:a tubular housing having a front end and a rear end, and including one or more coolant intake apertures circumferentially spaced within a coolant distribution portion of the tubular housing that is substantially proximate the front end, said tubular housing having one or more walls that at least partially define a cavity;a tube retention cap sealedly engaged proximate to the front end of the tubular housing, said tube retention cap including at least one gas tube orifice;an annular coolant chamber surrounding said coolant distribution portion of the tubular housing, said annular coolant chamber adapted to distribute liquid coolant around the one or more coolant intake apertures and to, in turn, direct liquid coolant around and through the one or more coolant intake apertures into the cavity of the tubular housing;a coolant inlet integrated with the annular coolant chamber, said coolant inlet adapted to receive liquid coolant and ...

Подробнее
23-04-2015 дата публикации

DOUBLE-WALLED HEAT EXCHANGER TUBE

Номер: US20150107806A1
Автор: Glass Michael T.
Принадлежит:

A heat exchanger for a motor vehicle, in particular an exhaust gas heat exchanger, includes an outer casing in which heat exchanger tubes are arranged as bundles. At least one heat exchanger tube is configured double-walled, and formed from an outer tube and an inner tube, wherein a first medium flows in the casing and/or in the inner tube and a second medium flows between the outer tube and the inner tube. 112.-. (canceled)13. A heat exchanger for a motor vehicle , in particular exhaust gas heat exchanger , comprising:an outer sheath; andheat exchanger tubes arranged in the outer sheath, said heat exchanger tubes each comprising an outer tube and an inner tube received in the outer tube, said outer tube and inner tubes being separately produced components,wherein an opening is provided in a region of an end of the outer tube for flow of a first medium into or out of the inner tube,wherein the first medium flows in the outer sheath and in the inner tube and a second medium flows between the outer tube and the inner tube, andwherein the outer tube and the inner tube are form fittingly and/or materially bodingly coupled with each other via a collar provided on the opening.14. The heat exchanger of claim 13 , wherein the heat exchanger tubes are arranged as bundle.15. The heat exchanger of claim 13 , wherein the opening is provided in an outer surface of the outer tube.16. The heat exchanger according to claim 13 , wherein the collar is configured so that the inner tube is fixed in position relative to the outer tube by the coupling of the inner tube to the outer tube via the collar.17. The heat exchanger of claim 13 , further comprising a sealing cap and/or a sealing plug is arranged on each of respective ends of the inner tube.18. The heat exchanger of claim 13 , wherein the sealing cap and/or a sealing plug is arranged the respective ends of the inner tube in a materially bonding and/or form fitting manner.19. The heat exchanger of claim 13 , wherein a gap is formed ...

Подробнее
19-04-2018 дата публикации

Heat Exchanger

Номер: US20180106550A1
Принадлежит: COLMAC COIL MANUFACTURING, INC.

A heat exchanger is described and which includes an exterior container having an internal cavity; a refrigerant distribution tube is positioned within the internal cavity and which is further coupled in fluid receiving relation relative to a first source of refrigerant; and a multiplicity of closely nested refrigerant tubes are located within the internal cavity and are further disposed in a closely spaced, radially outwardly oriented positions relative to the refrigerant distribution tube, and which additionally have a predetermined and similar length dimension, and individually form helical coils which have a given and similar length dimension, and a variable pitch, and which are further coupled to a second source of a refrigerant. 1. A heat exchanger , comprising:an exterior container which defines an internal cavity;a refrigerant distribution tube which is positioned within the internal cavity, and which is further coupled in fluid receiving relation relative to a first source of refrigerant; anda multiplicity of closely nested, refrigerant tubes which are located within the internal cavity of the exterior container, and which are further disposed in closely spaced, radially outwardly oriented positions relative to the refrigerant distribution tube, and wherein the respective refrigerant tubes each have a predetermined length dimension, and individually form a helical coil which has a given length dimension, and pitch, and wherein each of the refrigerant tubes, and the respective helical coils that the individual refrigerant tube forms have the same length dimension, and wherein the respective refrigerant tubes are each coupled in fluid receiving relation relative to a second source of a refrigerant.2. A heat exchanger as claimed in claim 1 , and wherein the first source of the refrigerant is a low pressure refrigerant claim 1 , and the second source of the refrigerant is a high pressure refrigerant.3. A heat exchanger as claimed in claim 1 , and wherein the ...

Подробнее
27-04-2017 дата публикации

Heat exchangers

Номер: US20170115072A1
Принадлежит: Hamilton Sundstrand Corp

A baffle for a shell and tube heat exchanger comprises a one piece helical flight extending from a central core. The helical flight has a plurality of aligned openings for receiving tubes of the heat exchanger. The helical flight may be made by machining from a casting or solid block of material, or by an additive manufacturing process.

Подробнее
18-04-2019 дата публикации

NESTED-FLOW HEAT EXCHANGERS AND CHEMICAL REACTORS

Номер: US20190113284A1
Автор: Vernon Milton Edward
Принадлежит: BayoTech, Inc.

Disclosed is a technology based upon the nesting of tubes to provide chemical reactors or chemical reactors with built in heat exchanger. As a chemical reactor, the technology provides the ability to manage the temperature within a process flow for improved performance, control the location of reactions for corrosion control, or implement multiple process steps within the same piece of equipment. As a chemical reactor with built in heat exchanger, the technology can provide large surface areas per unit volume and large heat transfer coefficients. The technology can recover the thermal energy from the product flow to heat the reactant flow to the reactant temperature, significantly reducing the energy needs for accomplishment of a process. 13.-. (canceled)4. A process for making ammonia , the process comprising:flowing a reactant comprising hydrogen and nitrogen in a first flow path in a first direction;reacting the hydrogen and the nitrogen through the first flow path to produce a product comprising ammonia;flowing the product through a second flow path in a second direction, the second direction being opposite the first direction, wherein:the first flow path is in fluid communication with the second flow path,the first flow path and the second flow path are coaxial about a longitudinal axis.5. The process of claim 4 , wherein:reacting the hydrogen and the nitrogen comprises using a catalyst, andthe catalyst is disposed to define a portion of the second flow path.6. The process of claim 4 , wherein the first flow path and the second flow path are in a bayonet configuration.7. The process of claim 4 , wherein:the reactant comprises one molar part nitrogen and three molar parts hydrogen.8. The process of claim 4 , wherein:the product comprises unreacted nitrogen and unreacted hydrogen.9. The process of claim 4 , wherein:a first tube defines a portion of the first flow path, anda second tube and the first tube define a portion of the second flow path.10. The process of ...

Подробнее
04-05-2017 дата публикации

EVAPORATOR

Номер: US20170122676A1
Принадлежит:

The present invention is a cross-flow evaporator adapted to generate vapor from the heat of the exhaust gases from an internal combustion engine. The evaporator is constituted, among other elements, by two plates spaced from one another which contain chambers. The heat exchange tubes alternately communicate the chambers of both plates, establishing a specific path for the fluid intended to change phase. The tubes extending between the chambers of the two plates are arranged transverse to the flow of the hot gas. 212122231323112112221323. The evaporator according to claim 1 , wherein one or both plates ( claim 1 , ) is formed by a first elemental plate (. claim 1 , .) having perforations to allow for the passage of heat exchange tubes () and a second elemental claim 1 , die-cut plate (. claim 1 , .) with perforations to configure the chambers (. claim 1 , .) claim 1 , the first elemental plate (. claim 1 , .) and the second elemental plate (. claim 1 , .) being attached to one another.31323. The evaporator according to claim 2 , wherein the second elemental claim 2 , die-cut plate (. claim 2 , .) is a composite plate claim 2 , comprising a plurality of die-cut plates stacked on one another to reach a greater thickness.411121111217127711112111121. The evaporator according to claim 1 , wherein inner walls (.. claim 1 , ..) of the chamber (. claim 1 , .) in which the cap () is housed are perpendicular to the main plane of the plate ( claim 1 , ) claim 1 , and wherein said cap () has walls (.) attached to the inner walls (.. claim 1 , ..) of said chamber (. claim 1 , .)5111211717. The evaporator according to claim 4 , wherein the inner walls (.. claim 4 , ..) and the walls (.) of the cap () are parallel.6774. The evaporator according to claim 1 , wherein at least one of the caps () is dome-shaped (.) having a semicircular section.7123. The evaporator according to claim 1 , wherein at least the first plate () claim 1 , the second plate () and the heat exchange tubes () ...

Подробнее
04-05-2017 дата публикации

EVAPORATOR

Номер: US20170122677A1
Принадлежит:

The present invention is a cross-flow evaporator adapted to generate vapor from the heat of the exhaust gases from an internal combustion engine. The evaporator is constituted, among other elements, by two plates spaced from one another which contain chambers. The heat exchange tubes alternately communicate the chambers of both plates, establishing a specific path for the fluid intended to change phase. The tubes extending between the chambers of the two plates are arranged transverse to the flow of the hot gas. This evaporator is suitable for heat recovery systems using a Rankine cycle, making use of the heat from the exhaust gases. 1. An evaporator for the evaporation of a first fluid by means of the heat provided by a second fluid , the second fluid being a hot gas , wherein said evaporator comprises:{'b': 1', '2', '1', '2', '1', '1', '2', '1, 'a first plate () and a second plate () facing one another and arranged spaced from one another, defining an inner face, the face facing the other plate, and an outer face opposite the inner face; wherein each of the plates (, ) comprises a plurality of chambers (., .);'}{'b': 4', '5', '1', '1', '2', '1', '1', '2, 'an intake manifold () of the first fluid and an exhaust manifold () of the first fluid situated in fluid communication with one another and with at least one different chamber (., .) of any of the plates (, );'}{'b': 3', '3', '1', '1', '1', '2', '1', '2', '1', '1', '2', '1', '1', '2', '1', '1', '2', '1', '1', '2', '3', '1', '1', '2', '1', '4', '5, 'a plurality of heat exchange tubes () wherein each of the heat exchange tubes () extends between a chamber (.) of the first plate () and a chamber (.) of the second plate (); wherein each chamber (., .) of one plate (, ) is in fluid communication with two or more chambers (., .) of the other plate (, ) by means of at least two heat exchange tubes (), except the chambers (., .) in fluid communication with the intake manifold () or the exhaust manifold ();'}{'b': 3', '4 ...

Подробнее
03-06-2021 дата публикации

HEAT EXCHANGERS

Номер: US20210164739A1
Автор: Turney Joseph
Принадлежит:

A counter-flow heat exchanger comprising a heat exchanger core including an inner wall and an outer wall radially outward and spaced apart from the inner wall. A first flow path is defined within the inner wall and a second flow path is defined between the inner wall and the outer wall. The heat exchanger core includes a primary flow inlet, a primary flow outlet and a middle portion therebetween. The inner and outer walls are concentric at the primary flow inlet of the heat exchanger core. The inner wall defines a first set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core diverging away from a radial center of the heat exchanger core. The inner wall and the outer wall define a second set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core converging toward the radial center of the heat exchanger core. 1. A counter-flow heat exchanger comprising:a heat exchanger core including an inner wall and an outer wall radially outward and spaced apart from the inner wall, wherein a first flow path is defined within the inner wall and a second flow path is defined between the inner wall and the outer wall, wherein the heat exchanger core includes a primary flow inlet, a primary flow outlet and a middle portion therebetween, wherein the inner and outer walls are concentric at the primary flow inlet of the heat exchanger core, wherein the inner wall defines a first set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core diverging away from a radial center of the heat exchanger core, and wherein the inner wall and the outer wall define a second set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core converging toward the radial center of the heat exchanger core.2. The counter-flow heat exchanger as recited in claim 1 , wherein the inner wall is corrugated to ...

Подробнее
30-04-2020 дата публикации

NESTED-FLOW HEAT EXCHANGERS AND CHEMICAL REACTORS

Номер: US20200132383A1
Автор: Vernon Milton E.
Принадлежит:

Disclosed is a technology based upon the nesting of tubes to provide chemical reactors or chemical reactors with built in heat exchanger. As a chemical reactor, the technology provides the ability to manage the temperature within a process flow for improved performance, control the location of reactions for corrosion control, or implement multiple process steps within the same piece of equipment. As a chemical reactor with built in heat exchanger, the technology can provide large surface areas per unit volume and large heat transfer coefficients. The technology can recover the thermal energy from the product flow to heat the reactant flow to the reactant temperature, significantly reducing the energy needs for accomplishment of a process. 1. (canceled)2. A chemical reactor comprising:a first tube;a second tube positioned in the first tube and defining an annular space between the first tube and the second tube; anda manifold assembly coupled to a first end of the first tube and a first end of the second tube, wherein the manifold assembly defines a first opening in direct fluid communication with the annular space between the first tube and the second tube and a second opening in direct fluid communication with a channel along the length of the second tube,wherein a second end of the second tube is open proximate a second end of the first tube.3. The chemical reactor of claim 2 , wherein the first tube and the second tube are coaxial.4. The chemical reactor of claim 2 , wherein a bayonet flow path is defined by the annular space claim 2 , the first and second openings claim 2 , and the channel claim 2 , and comprising a catalyst disposed along the bayonet flow path.5. The chemical reactor of claim 2 , comprising a heating assembly disposed around the manifold assembly.6. The chemical reactor of claim 2 , comprising a water shift reaction (WSR) unit configured to receive a product gas generated in the chemical reactor.7. The chemical reactor of claim 2 , wherein a ...

Подробнее
10-06-2021 дата публикации

Condensing Heat Exchanger for Air to Liquid Heat Pumps

Номер: US20210172657A1
Автор: William P. Bernardi
Принадлежит: United States ThermoAmp Inc

A heat exchange device may include a first pipe including a first inlet, a first outlet, and a first sidewall extending therebetween; a second pipe including a second inlet, a second outlet, and a second sidewall extending therebetween; and a plurality of dimples extending between the first sidewall and the second sidewall. The second sidewall may surround and extend about the first sidewall, the first sidewall may define a first fluid passage configured to permit flow of a first fluid, and the second sidewall and the first sidewall may define a second fluid passage configured to permit flow of a second fluid.

Подробнее
24-05-2018 дата публикации

EXTREME ENVIRONMENT HEAT EXCHANGER

Номер: US20180142970A1
Автор: Jarmon David C.
Принадлежит: UNITED TECHNOLOGIES CORPORATION

The heat exchanger () includes a ceramic matrix composite () (stable at temperatures up to 1,650° C.) surrounding and defining a hot fluid conduit (). A hardenable material () having a high thermal conductivity is formed into a heat transfer layer () surrounding the ceramic matrix composite (). A metal pipe () is coextensive with the heat transfer layer () and defines at least a portion () of at least one cool fluid passage () defined adjacent to and in heat exchange relationship with the heat transfer layer () so that a fluid passing through the cool fluid passage () absorbs heat passing through the heat transfer layer () from the hot fluid passing through the hot fluid conduit (). 117-. (canceled)18. A method of manufacturing an extreme environment heat exchanger , the method comprising:a. forming a ceramic matrix composite into an elongate form that defines a hot fluid conduit within the ceramic matrix composite, the ceramic matrix composite being configured to have mechanical stability at temperatures up to about 1,650 degrees Celsius;{'sup': '2', 'b. then, bonding a hardenable material having a thermal conductivity of at least 20 Btu/(hr. ft° F.) to the ceramic matrix composite so that the hardenable material surrounds and is coextensive with the hot fluid conduit;'}c. then, machining the hardenable material to produce a heat transfer layer surrounding the ceramic matrix composite that, with the ceramic matrix composite, defines about a uniform thickness between an exterior surface of the heat transfer layer and the hot fluid conduit;d. securing the heat transfer layer and attached ceramic matrix composite within a circumferentially displaced metal pipe such that the metal pipe defines at least a portion of at least one cool fluid passage adjacent to an in heat exchange relationship with the heat transfer layer, wherein the circumferentially displaced metal pipe is circumferentially displaced from the heat transfer layer so that the cool fluid passage is a ...

Подробнее
04-06-2015 дата публикации

Exhaust-gas heat exchanger

Номер: US20150152762A1
Принадлежит: TENNECO GMBH

An exhaust-gas heat exchanger for an exhaust system for cooling an exhaust-gas flow, having an inner pipe and an outer pipe, wherein the two pipes are indirectly or directly welded to one another in sealing fashion at the inlet side, a jacket pipe is arranged around the outside of the outer pipe and an annular gap for coolant is arranged between the outer pipe and the jacket pipe, and the inner pipe has an axial flow cross section (A 2 ) at the end as viewed in the flow direction (S) and has a perforation (P 2 ), which forms a radial flow cross section, in a direction at right angles to a flow direction (S). Between the inner pipe and the outer pipe there is formed an exhaust-gas duct for the exhaust-gas flow, wherein an intermediate pipe which is mounted in displaceable and/or rotatable fashion on the inner pipe is provided with a perforation (P 4 ) by which the axial flow cross section (A 2 ) of the inner pipe can be at least partially closed off.

Подробнее
04-09-2014 дата публикации

CO-FIRED ABSORPTION SYSTEM GENERATOR

Номер: US20140245768A1
Принадлежит: ROCKY RESEARCH

A co-fired generator for use in a continuous-cycle absorption heating and cooling system may provide heat to the interior of an annulus chamber from a first heat exchanger, such as a firetube heat exchanger, supplemented by heat to the exterior of the annulus chamber from a second heat exchanger containing fluid heated by an external source. Some embodiments may circulate fluid heated in a solar-heated collector through the second heat exchanger. Other embodiments may route exhaust gas from a combustion engine through the second heat exchanger. The second heat exchanger may be provided with a plurality of fins to increase the surface area available for thermal transfer between the heated fluid and the annulus chamber. 1. A continuous-cycle absorption heating and/or cooling system comprising:a closed circuit comprising a condenser, an absorber, and an evaporator; a firetube heat exchanger,', 'an annulus configured to contain a first fluid, the annulus having an interior surface and an exterior surface, the interior surface in thermal communication with the firetube heat exchanger, and', 'a supplemental heat exchanger in thermal communication with the exterior surface of the annulus and configured to contain a second fluid; and, 'a generator comprisinga heating device coupled to the supplemental heat exchanger and configured to heat the second fluid.2. The system of claim 1 , further comprising a fluid motive means configured to circulate the second fluid through the heating device and the supplemental heat exchanger.3. The system of claim 1 , wherein the heating device comprises a solar collector.4. The system of claim 1 , wherein the second fluid is a heat transfer fluid.5. The system of claim 4 , wherein the heat transfer fluid is an oil claim 4 , glycol claim 4 , glycol/water mixture claim 4 , paraffin claim 4 , silicone claim 4 , terpene claim 4 , phenyl claim 4 , cycloalkane claim 4 , an alkyl-based heat transfer medium claim 4 , or water as a single phase or in ...

Подробнее
14-06-2018 дата публикации

WASHER FLUID HEATING SYSTEM AND APPARATUS

Номер: US20180162327A1
Автор: Lansinger Jere Rask
Принадлежит:

A washer fluid heater disposed within a vehicle having an engine cooling system and a washer fluid dispensing system. The washer fluid heater includes a plurality of thin walled, closely spaced tubular members concentrically arranged around a central axis of the washer fluid heater. Each of the tubular members is separated from an adjacent tubular member by one of a plurality of flow channels. The plurality of flow channels includes first and second groups of flow channels. The washer fluid heater also includes a first end cap and a second end cap, where the first end cap includes a first washer fluid port and a first coolant port and the second end cap includes a second washer fluid port and a second coolant port. The first and second washer fluid ports are coupled to the first group of flow channels while the first and second coolant ports are coupled to the second group of flow channels. 1. A washer fluid heater for use with a vehicle having an engine cooling system and a washer fluid dispensing system , wherein the washer fluid dispensing system comprises a washer fluid reservoir and at least one nozzle , the washer fluid heater comprising:a plurality of tubular members concentrically arranged around a central axis and spaced apart from each other forming a plurality of flow channels, wherein each of the plurality of tubular members is separated from an adjacent tubular member by a respective one of the plurality of flow channels and wherein the plurality of flow channels comprises a first group of flow channels and a second group of flow channels different and fluidly isolated from the first group of flow channels; a first washer fluid port configured to receive washer fluid from the washer fluid reservoir; and', 'a first coolant port configured to receive heated coolant from the engine cooling system; and, 'a first end cap coupled to a first end portion of the washer fluid heater, comprising a second washer fluid port coupled to the at least one nozzle, ...

Подробнее
14-06-2018 дата публикации

Heat exchanger including twisted tubes

Номер: US20180164047A1
Автор: Hafez Raeisi Fard
Принадлежит: Individual

A heat exchanger comprising a shell having a first end and a second end, a first end plate and a second end plate defining a first volume with the shell that receives a first fluid therein, and at least one heat exchanger tube having a first end affixed to the first end plate and a second end affixed to the second end plate. The at least one heat exchanger tube extends through the second volume and including a cross-section defined by a plurality of lobes extending radially outwardly from the longitudinal center axis thereof. A first fluid passes through the first volume of the shell and a second fluid comprising a hot combustion gas passes through the at least one heat exchanger tube. The cross-section is constant along an entire length of the at least one heat exchanger tube.

Подробнее
15-06-2017 дата публикации

MULTIPHASE PUMPING SYSTEM WITH RECUPERATIVE COOLING

Номер: US20170167809A1
Принадлежит:

A multiphase pumping system for transporting a fluid includes a multiphase pump configured to increase pressure within the fluid and a recuperator in fluid communication with the multiphase pump. The recuperator is configured to remove thermal energy from a fluid upstream of the multiphase pump and is further configured to add thermal energy to a fluid downstream of the multiphase pump. The multiphase pumping system further includes a cooler configured to remove thermal energy from the fluid upstream of the multiphase pump. 1. A multiphase pumping system for transporting a fluid , said system comprising:a multiphase pump configured to increase pressure within the fluid;a recuperator in fluid communication with said multiphase pump, said recuperator configured to remove thermal energy from a fluid upstream of said multiphase pump and thermal energy to a fluid downstream of said multiphase pump; anda cooler configured to remove thermal energy from the fluid upstream of said multiphase pump.2. The multiphase pumping system of claim 1 , wherein said recuperator comprises a heat exchanger configured to transfer thermal energy between the fluid upstream of said cooler and the fluid downstream of said pump.3. The multiphase pumping system of claim 2 , wherein said heat exchanger is at least one of a counter flow heat exchanger claim 2 , a shell and tube heat exchanger claim 2 , and a plate heat exchanger.4. The multiphase pumping system of further comprising a separator configured to separate a gas phase of the fluid from a liquid phase of the fluid claim 1 , said separator positioned downstream from said multiphase pump claim 1 , wherein said recuperator is integrated within said separator.5. The multiphase pumping system of further comprising:a separator configured to separate a gas phase of the fluid from a liquid phase of the fluid, said separator positioned downstream from said multiphase pump;an inlet tank located upstream from said recuperator configured to mix the ...

Подробнее
18-09-2014 дата публикации

TUBE BUNDLE FOR SHELL-AND-TUBE HEAT EXCHANGER AND METHOD OF CONSTRUCTING SAME

Номер: US20140262171A1
Автор: Ljubicic Blazo
Принадлежит: Koch Heat Transfer Company, LP

A tube bundle is provided for a shell-and-tube heat exchanger. The tube bundle includes a plurality of elongated tubes, each of which has an intermediate portion that has a cross section in the form of a flattened circle with at least one axis of symmetry. The ends of the tubes may have a circular cross section, with the diameter of one of the circular ends being less than the other end and also less than the length of a shorter axis of symmetry of the intermediate portion of the tube. This tube construction allows the tube bundle to be assembled by inserting the smaller-diameter end of the tube through the aligned openings in the spaced-apart baffles in the tube bundle. The non-circular cross section of the intermediate portion of the tubes increases the tube-side and shell-side heat transfer coefficients. 1. A tube bundle for a shell-and-tube heat exchanger , said tube bundle comprising:a plurality of hollow, elongated tubes extending in parallel and spaced-apart relationship to each other in a preselected pattern, each of said tubes having a first end for entry of a first fluid for flow within the tube along a longitudinal length of the tube and an opposite second end for the first fluid to exit the tube and an intermediate portion between the first and second ends, said intermediate portion of the tube having a cross section in the form of a flattened circle with at least one axis of symmetry;a first tube sheet having holes into which the first ends of the tubes extend and are secured; anda plurality of baffles positioned at spaced apart positions along the longitudinal length of the tubes for supporting the tubes and guiding flow of a second fluid exteriorly of said tubes, each of said baffles having a cutout for passage of fluid and a plurality of openings through which at least some of said tubes are inserted, wherein said cutouts of adjacent ones of said baffles are rotationally offset around a center longitudinal axis of said tube bundle.2. The tube bundle ...

Подробнее
18-09-2014 дата публикации

TUBE BUNDLE FOR SHELL-AND-TUBE HEAT EXCHANGER AND A METHOD OF USE

Номер: US20140262172A1
Автор: Ljubicic Blazo
Принадлежит: Koch Heat Transfer Company, LP

A tube bundle is provided for a shell-and-tube heat exchanger. The tube bundle includes a plurality of elongated tubes, each of which has an intermediate portion that has a cross section in the form of a flattened circle with at least one axis of symmetry. The tubes are arranged in concentric circles with the axis of symmetry extending tangentially to the circle to facilitate rotational flow of a shell-side fluid. 1. A tube bundle for a shell-and-tube heat exchanger , said tube bundle comprising:a plurality of hollow, elongated tubes extending in parallel and spaced-apart relationship to each other and arranged in a preselected pattern, each of said tubes having a first end for entry of a first fluid for flow within the tube along a longitudinal length of the tube and an opposite second end for the first fluid to exit the tube and an intermediate portion between the first and second ends;a first tube sheet having holes into which the first ends of the tubes extend and are secured;a plurality of baffles positioned at spaced apart positions along the longitudinal length of the tubes for supporting the tubes and guiding flow of a second fluid exteriorly of said tubes, each of said baffles having a cutout for passage of fluid and a plurality of openings through which at least some of said tubes are inserted, wherein said cutouts of adjacent ones of said baffles are rotationally offset around a center longitudinal axis of said tube bundle; anda plurality of flow-diverting plates, each of said plates extending in one direction between and in contact with adjacent ones of said baffles and extending in an opposite direction along said cutouts in said adjacent ones of said baffles.2. The tube bundle of claim 1 , wherein said intermediate portion of each tube has a cross section in the form of a flattened circle with at least one axis of symmetry.3. The tube bundle of claim 2 , wherein said preselected pattern in which said tubes are arranged is a series of concentric circles ...

Подробнее
22-06-2017 дата публикации

SOLUTION CONVEYING AND COOLING APPARATUS

Номер: US20170176109A1
Автор: HARUYAMA Hideyuki
Принадлежит: NANOTEC CO., LTD.

To provide a solution conveying and cooling apparatus that enables removal of a deposit of solid material, or a fouling deposit, inside the apparatus with extremely simple work equipment by fewer on-site workers in a short tune without any dangerous work such as hydroblasting. The solution conveying and cooling apparatus has a rigid outer tube for a cooling medium and a plurality of rigid outer tubes for solution arranged parallel to each other inside the rigid outer tube for a cooling medium. A thin inner tube is disposed inside each of the rigid outer tubes for solution, this thin inner tube having an outer diameter smaller than an inner diameter of the rigid outer tube for solution at normal temperature and pressure, and expanding by an increase in at least one of temperature and pressure of a solution conveyed and as a result contacting with an inner surface of the rigid outer tube for solution that is cooled by the cooling medium. 1. A solution conveying and cooling apparatus having a rigid outer tube for a cooling medium and a plurality of rigid outer tubes for solution arranged parallel to each other inside the rigid outer tube for a cooling medium , the apparatus being characterized in thata thin inner tube is disposed inside each of said rigid outer tubes for solution, said thin inner tube having an outer diameter smaller than an inner diameter of said rigid outer tube for solution at normal temperature and pressure, expanding by an increase in at least one of temperature and pressure of a solution conveyed and, as a result, contacting with an inner surface of said rigid outer tube for solution, and moreover contracting in diameter, by cooling or pressure drop of said solution.2. The solution conveying and cooling apparatus according to claim 1 , wherein said thin inner tube is made of an SUS300-based stainless steel.3. The solution conveying and cooling apparatus according to claim 1 , wherein said thin inner tube is made of an aluminum alloy.4. The ...

Подробнее
28-06-2018 дата публикации

Modular Shell-and-Tube Heat Exchanger Apparatuses and Molds and Methods for Forming Such Apparatuses

Номер: US20180180363A1
Принадлежит:

Modular tubing apparatuses for use in a shell-and-tube heat exchanger are described. Multiple apparatuses may be connected in series to form a high density, small tube diameter, long length tube apparatus assembly. Casting molds for forming modular tubing apparatuses are likewise described, including methods for casting such apparatuses. 1. A modular tube apparatus for a heat exchanger , the apparatus comprising:a connecting plate;a plurality of tubes extending from a bottom surface of the connecting plate, wherein each tube of the plurality of tubes comprises a distal open end and a hollow portion extending from the distal open end to the connecting plate;a plurality of receiving cups, wherein each receiving cup of the plurality of receiving cups is recessed into a top surface of the connecting plate to a depth partially through the connecting plate and disposed opposite a respective tube of the plurality of tubes, and wherein each receiving cup of the plurality of receiving cups defines an internal contour that conforms to an outer contour of the distal open end of the respective tube of the plurality of tubes;a first plurality of fluid paths inside the connecting plate, wherein each fluid path of the first plurality of fluid paths extends from each receiving cup of the plurality of receiving cups to the hollow portion of each respective tube of the plurality of tubes; anda second plurality of fluid paths through the connecting plate, wherein each fluid path of the second plurality of fluid paths extends from the top surface of the connecting plate to the bottom surface of the connecting plate.2. The apparatus of claim 1 , wherein the apparatus is formed as a unitary body.3. The apparatus of claim 2 , wherein the unitary body comprises a cast material.4. The apparatus of claim 3 , wherein the cast material comprises a metal.5. The apparatus of claim 1 , wherein each tube of the plurality of tubes is substantially cylindrical.6. The apparatus of claim 1 , wherein ...

Подробнее
22-07-2021 дата публикации

HEAT EXCHANGERS

Номер: US20210222966A1
Принадлежит:

A counter-flow heat exchanger core includes a first wall defining a longitudinal axis. The first flow path is defined within the first wall. The first flow path includes a primary flow inlet and a primary flow outlet downstream from the primary flow inlet. The heat exchanger core includes at least two hollow vanes circumferentially spaced apart and extending in a radially inward direction from the first wall. Each of the at least two hollow vanes includes a first vane wall and a second vane wall. The heat exchanger core includes a second flow path defined within the at least two hollow vanes between the first vane wall and second vane wall of each of the at least two hollow vanes. The heat exchanger core includes at least one fin extending between two of the at least two circumferentially spaced apart vanes. 1. A counter-flow heat exchanger core comprising:a first wall defining a longitudinal axis;a first flow path defined within the first wall, wherein the first flow path includes a primary flow inlet and a primary flow outlet downstream from the primary flow inlet;at least two hollow vanes circumferentially spaced apart and extending in a radially inward direction from the first wall, wherein each of the at least two hollow vanes includes a first vane wall and a second vane wall;a second flow path defined within the at least two hollow vanes between the first vane wall and second vane wall of each of the at least two hollow vanes; andat least one fin extending between two of the at least two hollow vanes.2. The counter-flow heat exchanger core as recited in claim 1 , wherein the at least one fin is at least one of a non-linear fin or a portion of a cylindrical wall.3. The counter-flow heat exchanger core as recited in claim 1 , further comprising a second wall radially inward from the first wall.4. The counter-flow heat exchanger core as recited in claim 1 , wherein the at least one non-linear fin includes a plurality of non-linear fins between two of the hollow ...

Подробнее
13-07-2017 дата публикации

HEAT EXCHANGERS

Номер: US20170198990A1
Автор: Turney Joseph
Принадлежит:

A counter-flow heat exchanger comprising a heat exchanger core including an inner wall and an outer wall radially outward and spaced apart from the inner wall. A first flow path is defined within the inner wall and a second flow path is defined between the inner wall and the outer wall. The heat exchanger core includes a primary flow inlet, a primary flow outlet and a middle portion therebetween. The inner and outer walls are concentric at the primary flow inlet of the heat exchanger core. The inner wall defines a first set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core diverging away from a radial center of the heat exchanger core. The inner wall and the outer wall define a second set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core converging toward the radial center of the heat exchanger core. 1. A counter-flow heat exchanger comprising:a heat exchanger core including an inner wall and an outer wall radially outward and spaced apart from the inner wall, wherein a first flow path is defined within the inner wall and a second flow path is defined between the inner wall and the outer wall, wherein the heat exchanger core includes a primary flow inlet, a primary flow outlet and a middle portion therebetween, wherein the inner and outer walls are concentric at the primary flow inlet of the heat exchanger core, wherein the inner wall defines a first set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core diverging away from a radial center of the heat exchanger core, and wherein the inner wall and the outer wall define a second set of channels extending axially from the primary flow inlet to the middle portion of the heat exchanger core converging toward the radial center of the heat exchanger core.2. The counter-flow heat exchanger as recited in claim 1 , wherein the inner wall is corrugated to ...

Подробнее
26-07-2018 дата публикации

NESTED-FLOW HEAT EXCHANGERS AND CHEMICAL REACTORS

Номер: US20180209743A1
Автор: Vernon Milton Edward
Принадлежит: BayoTech, Inc.

Disclosed is a technology based upon the nesting of tubes to provide chemical reactors or chemical reactors with built in heat exchanger. As a chemical reactor, the technology provides the ability to manage the temperature within a process flow for improved performance, control the location of reactions for corrosion control, or implement multiple process steps within the same piece of equipment. As a chemical reactor with built in heat exchanger, the technology can provide large surface areas per unit volume and large heat transfer coefficients. The technology can recover the thermal energy from the product flow to heat the reactant flow to the reactant temperature, significantly reducing the energy needs for accomplishment of a process. 1. (canceled)2. A process of making hydrogen , the process comprising:flowing a first reactant comprising methane through a first flow path;flowing a second reactant comprising air through a second flow path;reacting air and methane to produce an exhaust and an amount of heat;heating the first reactant and the second reactant with a first portion of the amount of heat;flowing the exhaust through a third flow path;flowing a third reactant through a fourth flow path, wherein the third reactant comprises water and methane;heating the third reactant with a second portion of the amount of heat;reacting the third reactant to produce a product comprising hydrogen and carbon monoxide;flowing the product through a fifth flow path; andtransferring heat from the product to the third reactant in the fourth flow path, wherein:the first flow path, the second flow path, the third flow path, the fourth flow path, and the fifth flow path are coaxial about a longitudinal axis.3. The process of claim 2 , wherein the product is produced by steam methane reforming using the third reactant.4. The process of claim 2 , wherein:the third reactant further comprises carbon monoxide, andthe product is produced by the water shift reaction using the third ...

Подробнее
04-08-2016 дата публикации

ADSORBER

Номер: US20160223229A1
Принадлежит:

In an adsorber, a sintered body, which is formed by sintering metal powder particles, is joined to an outer surface of a heat medium tube, in which heat medium flows. An adsorbent is held by the sintered body. A groove is formed in an outer surface of the heat medium tube, and a groove is formed in an inner surface of the heat medium tube. 1. An adsorber comprising:a heat medium tube, through which heat medium flows;a sintered body that is joined to an outer surface of the heat medium tube, wherein the sintered body is porous and is formed by sintering metal powder particles; andan adsorbent that is held by the sintered body, wherein:a groove is formed in the outer surface of the heat medium tube, and a groove is formed in an inner surface of the heat medium tube.2. The adsorber according to claim 1 , wherein:the groove of the outer surface and the groove of the inner surface extend in a direction that crosses an axial direction of the heat medium tube;the groove of the outer surface is one of a plurality of grooves, which are formed in the outer surface; andthe groove of the inner surface is one of a plurality of grooves, which are formed in the inner surface.3. The adsorber according to claim 1 , wherein the groove of the outer surface and the groove of the inner surface are spiral grooves claim 1 , respectively claim 1 , which extend in a direction that crosses an axial direction of the heat medium tube.4. The adsorber according to claim 3 , wherein the groove of the inner surface satisfies a relationship of hi/di>0.058 where hi denotes a depth of the groove claim 3 , and di denotes an inner diameter of the heat medium tube.5. The adsorber according to claim 4 , wherein the groove of the inner surface satisfies a relationship of hi/di>0.070.6. The adsorber according to claim 5 , wherein the groove of the inner surface satisfies a relationship of hi/di≧0.099.7. The adsorber according to claim 4 , wherein the groove of the inner surface satisfies a relationship of ...

Подробнее
02-08-2018 дата публикации

NESTED-FLOW HEAT EXCHANGERS

Номер: US20180216893A1
Автор: Vernon Milton Edward
Принадлежит: BayoTech, Inc.

Disclosed is a technology based upon the nesting of tubes to provide chemical reactors or chemical reactors with built in heat exchanger. As a chemical reactor, the technology provides the ability to manage the temperature within a process flow for improved performance, control the location of reactions for corrosion control, or implement multiple process steps within the same piece of equipment. As a chemical reactor with built in heat exchanger, the technology can provide large surface areas per unit volume and large heat transfer coefficients. The technology can recover the thermal energy from the product flow to heat the reactant flow to the reactant temperature, significantly reducing the energy needs for accomplishment of a process. 1. A heat exchanger comprising of three or more nested tubes for thermal energy transfer from one fluid flow to another fluid flow in which the flow path is maintained open through the use of substantially-non-flow-blocking spacers.2. A heat exchanger , the heat exchanger comprising:a first tube having a first end;a second tube having a second end;a third tube having a third end; and the first tube, the second tube, and the third tube are coaxial about a longitudinal axis,', 'the first tube defines a portion of a first flow path,', 'the first tube and the second tube define a portion of a second flow path,', 'the second tube and the third tube define a portion of a third flow path,', 'the second flow path and the third flow path are annular flow paths,', 'the second end is the end of the second tube closest to the first end,', 'the third end is the end of the third tube closest to the first end,', 'the manifold assembly is in contact with the first end, the second end, and the third end,', 'the manifold assembly defines an input and an outlet,', 'the input is in fluid communication with at least one of the first flow path, the second flow path, or the third flow path, and', 'the outlet is in fluid communication with at least one of ...

Подробнее
11-08-2016 дата публикации

Air-to-Air Heat Exchanger

Номер: US20160231016A1
Автор: Roos Christoph
Принадлежит:

Air-to-air heat exchanger for ventilation systems with two countercurrent air flows disposed inside a cylindrical housing, a first air flow circulating inside the heat exchanger inside closed pipes, whilst the second air flow is in spaces between the pipes and cylindrical housing, and a fan moving the countercurrent air flows and disposed at one end of the cylindrical housing, with the fan including concentric inner and outer rings separated by a wall for moving air in opposite directions, a bunch of straight, parallel pipes whose end elements at the fan side are tightly gathered together, in the end of a cylindrical wall and, on the opposite side, in the end of a cylindrical pipe fitting, and between end elements, taper into middle sections between which are spaces, and a sleeve lining the inner wall of the housing at the middle sections and constricts the inner diameter of the housing. 1. Air-to-air heat exchanger for ventilation systems with two countercurrent air flows , comprising:a cylindrical housing for housing the heat exchanger;pipes inside the cylindrical housing and inside which a first air flow circulates in the closed pipes inside the heat exchanger while a second air flow is disposed in spaces between the pipes and the cylindrical housing for producing a second air flow which is countercurrent to the first air flow;a fan for moving the countercurrent air flows, the fan being disposed at one end of the cylindrical housing, with the fan comprising an inner ring and an outer ring arranged concentrically around the inner ring for moving the air in the opposite countercurrent directions, with spaces occupied by the outer ring and inner ring being separated from each other by a cylindrical wall,wherein the pipes are formed as a bunch of straight, parallel pipes having end elements at an end closest to the fan tightly disposed together and enclosed in a ring-shaped end of the cylindrical wall and, at an opposite side, are tightly disposed together and ...

Подробнее
09-08-2018 дата публикации

Heat Exchanger for an Oxygenator and Method for Producing Such a Heat Exchanger

Номер: US20180224211A1
Принадлежит:

A heat exchanger for an oxygenator comprises multiple tube sections, each having a longitudinal tube axis, wherein the tube sections are disposed as a bundle having a longitudinal bundle axis, and the tube sections are connected to each other in at least one connecting section of the bundle by joining by way of chemical and/or physical bonded joints. A method for producing the heat exchanger is also provided. 1. A method for producing a heat exchanger for an oxygenator , comprising:providing multiple tube sections, each having a longitudinal tube axis;disposing the tube sections to form a bundle having a longitudinal bundle axis, wherein the longitudinal tube axes are in particular oriented parallel to each other; andconnecting the tube sections to each other on at least one connecting section of the bundle by joining the tube sections by way of chemical and/or physical bonded joints.2. The method according to claim 1 , further comprising twisting the bundle about the longitudinal bundle axis after the tube sections have been connected.3. The method according to claim 1 , further comprising inserting the bundle into a housing.4. The method according to claim 3 , wherein the bundle is inserted into the housing in such a way that a connecting section that is disposed at each bundle end is disposed at least sectionally outside the housing.5. The method according to claim 1 , wherein the bundle is severed at the at least one connecting section.6. The method according to claim 3 , wherein the housing into which the bundle is inserted is tubular.7. The method according to claim 2 , wherein twisting of the bundle about the longitudinal bundle axis disposes the longitudinal tube axes of the tubes of the bundle at an angle relative to the longitudinal bundle axis.8. The method according to claim 1 , further comprising compressing the bundle along the longitudinal bundle axis after the tube sections have been connected to impart a curvature to the tube sections of the bundle. ...

Подробнее
18-07-2019 дата публикации

Multilayer pipe cooling cold storage

Номер: US20190219322A1
Автор: Kunio Osawa
Принадлежит: CHUON CO Ltd

A cold storage box 1 comprises a housing 2 internally having a storage space S for a cold storage object, and one or more heat exchanger tubes 3 provided in the storage space S; wherein the heat exchanger tubes 3 are each a multilayer tube comprising an outer tube with thermal conductivity having an outer surface facing the storage space S, and as inner tube provided inside the outer tube; a first brine solution that does not freeze at 0° C. is contained between the outer tube and the inner tube; and a refrigerant, or a second brine solution that does not freeze at 0° C. is contained inside the inner tube.

Подробнее
24-08-2017 дата публикации

Method to Control Fluid Flow Variations Among Fluid Tubes of Heat Exchangers in Transfer Line Exchangers and Like Applications

Номер: US20170241722A1
Автор: MONTESTRUC ALFRED N.
Принадлежит:

Tube-bundle heat exchangers are commonly used to quench reacting fluids to drop the temperature of the reacting fluid below a specific temperature which cuts off undesirable chemical reactions in a minimal time as practical. A common commercial application is production of olefins. Shell and tube type and bundles of tube in tube exchanges are used in this application, the method is applicable to both. Significant variations in reacting fluid mass flow rates in the tubes of the tube-bundle can cause sub-optimal performance of the process. By placement of precise partial obstruction to flow of the reacting fluids at the tube exits to an outlet plenum chamber, these flow variations can be controlled. By adding remotely readable temperature measurement, and making the obstructions adjustable, the operator of the production facility can minimize production losses due to the variations in flow between tubes in the tube-bundle. 1) A method to reduce variation in mass flow between individual tubes in a plurality of fluid tubes in a tube-bundle of a heat exchanger used to quench chemical reactions in the fluid , said heat exchanger comprising;a) an inlet plenum chamber from which the hot fluid flows into the tubes of the tube-bundle through an inlet tube-sheet,b) a plurality of fluid tubes in a tube-bundle used to cool the fluid with some form of pressure containing shell to contain a different cooling fluid, including either a shell and inlet and outlet tube-sheets, or a plurality of outer tubes with the fluid tubes forming a bundle of tube in tube heat exchangers surrounding each fluid tube, and joined at inlet and outlet tube sheets,c) an outlet plenum chamber where flow from each of the tubes in the tube-bundle merge,d) the imposition of some precision designed and positioned object or set of objects in the outflow of at least some portion of the individual tubes such that the fluid mass flow from those tubes is reduced by predictable amounts, the effect of which is to ...

Подробнее
21-09-2017 дата публикации

Method and Apparatus for Reclaiming Heat During Liquid Purification Using Heat Exchanges

Номер: US20170268827A1
Принадлежит:

A system capable of providing a liquid purification process using heat regenerating or recovering via heat exchangers (“HEs”). The system, in one embodiment, includes a first set of thermal conductive channels (“TCC”), a second set of TCC, and a third set of TCC. The first set of TCC configured in a first HE is arranged in cylindrical shape which is able to surround or enclose a boiler. A function of TCC is to guide a liquid flow traveling through an HE. The second set of TCC configured in a second HE guides a second liquid flow traveling through the second HE. The third liquid flow such as a cold water stream, for example, flows through the third set of TCC adjacent to the first set of TCC and extracts heat from the first liquid flow such as hot purified water via TCC.

Подробнее
29-09-2016 дата публикации

Nested-Flow Heat Exchangers and Chemical Reactors

Номер: US20160282052A1
Автор: Vernon Milton Edward
Принадлежит:

Disclosed is a technology based upon the simple nesting of tubes to provide heat exchangers, chemical reactors or chemical reactors with built in heat exchanger. As a chemical reactor, the technology provides the ability to manage the temperature within a process flow to better control the process for improved performance, control the location of product production to control corrosion issue, or implement multiple steps for a process within the same piece of equipment. As a heat exchanger, the technology can provide large surface areas per unit volume and large heat transfer coefficients. As a combined heat exchanger and chemical reactor, the technology can recover the thermal energy from the product flow to heat the reactant flow to the reactant temperature, significantly reducing the energy needs for accomplishment of a process. Combined heat exchanger and chemical reactor examples for hydrogen production and ammonia production are presented, along with a urea production example that integrates the product formation, resonance time conversion and stripping steps for urea production all within a single process unit. 1. A process for making hydrogen comprising the steps of steam methane reforming and water shift reaction; using nested-flow technology to maximize the energy utilization , maximize the thermal coupling between the reforming and combustion , and to improve the performance of the catalyst beds.2. A process for making hydrogen of claim 1 , wherein the energy required for heating up the steam and methane reactants is obtained from cooling down the carbon-monoxide claim 1 , carbon-dioxide and hydrogen products; wherein the hardware required for that energy transfer is internal to the chemical process reactor; and wherein a significantly reduction in the energy needs for product formation is observed.3. A process for making hydrogen of claim 1 , wherein the energy required for heating up the combustion reactants is obtained from cooling down the combustion ...

Подробнее
27-10-2016 дата публикации

Metal hydride hydrogen storage tank for containing hydrides

Номер: US20160312956A1

A tank for storing hydrogen by absorption in a hydrogen storage material, including: a chamber; a hydrogen supplier to supply hydrogen into the chamber and/or collect hydrogen in the chamber; an inner structure for storing hydrogen storage material, the inner structure including at least two cups, each cup including a base, a side wall, and a closing element forming a volume impermeable to the hydrogen storage material, at least part of each cup being permeable to hydrogen, and the inner structure including a passage provided at least between part of an outer face of the side wall of the cup and an inner face of the chamber.

Подробнее
27-10-2016 дата публикации

Cylindrical Tubular Heat Exchanger Type 1

Номер: US20160313074A1
Автор: Taylor Ronald Paul
Принадлежит:

A tubular heat exchanger employing radially arranged heat exchange tubes surrounding and attached to a center tube enclosing a heat source by an annular top flange attached to a removable top cover above the tube arrangement. The heat exchange tubes are connected at the bottom to an exhaust collection manifold which is in turn connected to an exhaust outlet pipe vented to the atmosphere. As heated fluid ascends inside the center tube, it is forced outwardly inside the top cover, apportioning the heated fluid into equally spaced radially arranged heat exchange tubes. The heated fluid descends inside the heat exchange tubes, disbursing heat outwardly through the walls of the heat exchange tubes into the ascending heat transfer fluid. The mostly cooled heated fluid is collected and recombined in the exhaust collection manifold and into the exhaust outlet pipe. The heat transfer fluid ascends above the top cover for final utilization. 1. A cylindrical tubular heat exchanger type 1 for more efficient heat exchange and better serviceability comprising:means for general assembly of the overall tubular heat exchanger;means for encompassing the heat source and combustion area, providing the initial flow conduit for the internal heated fluid ascending from the heat source, as well as helping form a flow path for the inner portion of the heat exchange fluid;means for enclosing a descending internal heated fluid and transferring heat from the internal heated fluid through the outside walls of the heat exchange tubes into the ascending heat transfer fluid surrounding the outside of the heat exchange tubes;means for connecting the top of the center tube with the surrounding heat exchange tubes in sealing engagement, and providing a sealing mounting flange for the removable top cover, tightly fitted to said means for enclosing a descending internal heated fluid and transferring heat from the internal heated fluid through the outside walls of the heat exchange tubes into the ...

Подробнее
27-10-2016 дата публикации

Cylindrical Tubular Heat Exchanger Type 2

Номер: US20160313075A1
Автор: Taylor Ronald Paul
Принадлежит:

In accordance with the present invention, there is provided a tubular heat exchanger wherein a central tube is employed to enclose an internal heated fluid which ascends inside the central tube. The heated fluid is then radially disbursed as it converges toward the internal surface of a top cover of the heat exchanger assembly, being forced outwardly under the top flange by the updraft force of the heated fluid, which forces the heated fluid downwardly apportioning the heated fluid around equally spaced axially arranged heat transfer tubes surrounded by an outer tube which are in sealed engagement with the top flange and attach at the bottom in sealing engagement with the exhaust collection manifold. The heated fluid descends around the tubes and enters an exhaust manifold exiting through an exhaust pipe. The heat transfer fluid enters a lower plenum and flows around the heat exchanger core into an upper plenum. 1. A cylindrical tubular heat exchanger type 2 for more efficient heat exchange and better serviceability comprising:means for encompassing the heat source, combustion area;means for enclosing the ascending inner portion of the heat transfer fluid, transferring heat from the descending heated fluid surrounding the outside of the heat exchange tubes into the ascending heat transfer fluid which is inside the heat exchange tubes via conduction through the tube walls;means for covering and sealing the outer tube, and providing a secondary heat exchange area, the top mounting area for the heat exchange tubes, and a sealable mounting flange for the removable top cover. when removed allows internal access into the outer tube to remove the heat exchange tubes for cleaning, rigidly connected to said means for enclosing the ascending inner portion of the heat transfer fluid, transferring heat from the descending heated fluid surrounding the outside of the heat exchange tubes into the ascending heat transfer fluid which is inside the heat exchange tubes via conduction ...

Подробнее
02-11-2017 дата публикации

GAS-LIQUID MIXING AND DISTRIBUTING DEVICE, AND SHELL AND TUBE TYPE HEAT EXCHANGER

Номер: US20170312707A1
Автор: Park Jong Heon
Принадлежит:

Disclosed herein is a gas-liquid mixing and distributing device. The gas-liquid mixing and distributing device includes a mixing head including a chamber, a plurality of gas spray nozzles, and a plurality of liquid spray nozzles; and a liquid supplying part connected to the mixing head and supplying a liquid to the mixing head, wherein the plurality of gas spray nozzles and the plurality of liquid spray nozzles included in the mixing head are uniformly mixed and distributed so that the liquid and gas sprayed from the mixing head are uniformly mixed with each other. 1. A gas-liquid mixing and distributing device , comprising:a mixing head including a chamber, a plurality of gas spray nozzles, and a plurality of liquid spray nozzles; anda liquid supplying part connected to the mixing head and supplying a liquid to the mixing head,wherein the plurality of gas spray nozzles and the plurality of liquid spray nozzles included in the mixing head are uniformly mixed and distributed so that the liquid and gas sprayed from the mixing head are uniformly mixed with each other.2. The gas-liquid mixing and distributing device of claim 1 , wherein the plurality of gas spray nozzles spray a gas supplied from a gas supplying part of a shell and tube type heat exchanger in which the gas-liquid mixing and distributing device is installed claim 1 , andgas-liquid mixing fluid that the gas and the liquid are mixed with each other is supplied to tubes through a tube sheet of the shell and tube type heat exchanger.3. The gas-liquid mixing and distributing device of claim 2 , wherein the plurality of gas spray nozzles are formed as a tube type nozzle that penetrates through the chamber claim 2 , andthe plurality of liquid spray nozzles are formed as an orifice nozzle formed in a top plate of the chamber.4. The gas-liquid mixing and distributing device of claim 2 , wherein the mixing head further includes a liquid stack pulverizing nozzle for pulverizing a liquid stack stacked on a region ...

Подробнее
25-10-2018 дата публикации

HEAT EXCHANGER ARRANGEMENT FOR AN INDUSTRIAL PRODUCTION PLANT

Номер: US20180306518A1
Принадлежит: ARVOS GMBH

An industrial production plant including at least one reactor for producing a flue gas and including a heat exchanger system having a first heat exchanger section for heat exchange between the flue gas and a fluid and a second heat exchanger section for heat exchange between the flue gas and reaction air for the reactor, which can be preheated by the second heat exchanger section. The first heat exchanger section is configured as a double-tube heat exchanger with first tubes each arranged one-way in a respective first jacket tube, and the second heat exchanger section is configured as a tube bundle heat exchanger with a tube bundle of second tubes arranged in a second jacket tube and each arranged one-way in the jacket tube. 110-. (canceled)11. A carbon black production plant comprising:at least one reactor for producing a flue gas and comprising a heat exchange system having a first heat exchange section for heat exchange between the flue gas and a fluid and a second heat exchange section for heat ex-change between the flue gas and reaction air for the reactor, wherein the reaction air can be preheated by the second heat ex-change section,wherein said first heat exchange section is designed as a double-tube heat exchanger comprising first tubes each arranged in a single-path configuration in a respective first casing tube, and wherein said second heat exchange section is designed as a tube-bundle heat exchanger comprising a tube bundle which is arranged in a second casing tube and which includes second tubes each arranged in a single-path configuration in the casing tube, said first and second tubes being adapted to have the flue gas flow through them,wherein said double-tube heat exchanger and said tube-bundle heat exchanger are arranged vertically, wherein the respective upper ends of the first and second tubes are connected to each other via a tube conduit, the flue gas flowing through the double-tube heat exchanger is an ascending direction and through the tube ...

Подробнее
10-11-2016 дата публикации

BLOOD PROCESSING UNIT WITH HEAT EXCHANGER CORE FOR PROVIDING MODIFIED FLOW PATH

Номер: US20160325036A1
Принадлежит:

A blood processing apparatus may include a heat exchanger and a gas exchanger. At least one of the heat exchanger and the gas exchanger may be configured to impart a radial component to blow flow through the heat exchanger and/or gas exchanger. The heat exchanger may be configured to cause blood flow to follow a spiral flow path. 112.-. (canceled)13. A blood processing apparatus comprising:a housing having a blood inlet and a blood outlet, the blood inlet extending into an interior of the housing;a heat exchanger core arranged within the housing, the heat exchanger core configured to impart a radial flow to blood passing from the blood inlet to an exterior of the heat exchanger core, the core including one or more ribs defining indentations;heat exchanger hollow fibers disposed about the heat exchanger core such that a heat exchanger fluid may flow through the heat exchanger hollow fibers and blood from the core aperture may flow across the heat exchanger hollow fibers;wherein the heat exchanger hollow fibers are supported by the one or more ribs of the heat exchanger core;a cylindrical shell extending coaxially about the heat exchanger core, the cylindrical shell including an annular shell aperture disposed near a second end of the housing, the shell aperture configured to impart a longitudinal blood flow component to blood passing to an exterior of the cylindrical shell; andgas exchanger hollow fibers disposed about the cylindrical shell such that gases may flow through the gas exchange hollow fibers and blood passing from the annular shell aperture may flow across the gas exchanger hollow fibers.14. The blood processing apparatus of claim 13 , wherein the one or more ribs include one or more radially disposed core ribs configured to support the heat exchanger hollow fibers as well as provide a radial component to blood flow across the heat exchanger hollow fibers.15. The blood processing apparatus of claim 13 , wherein the one or more ribs include one or more ...

Подробнее
10-11-2016 дата публикации

Vertical straight tube countercurrent condenser

Номер: US20160327341A1
Автор: Artamo Arvi, Juhola Pentti
Принадлежит:

The subject of the invention is a vertical shell and tube straight tube countercurrent condenser, wherein the condensing steam flows on the shell side of the condenser, and the cooling water on the tube side. The invention is characterized in that the countercurrent condenser is two pass on both the shell side and the tube side, whereby the heat surface of the first pass on the shell side is formed from heat surface tubes in the steam space of this pass attached at their upper end to an upper tube sheet and at their lower end to a lower tube sheet through which tubes cooling water of second pass on tube-side flows; and the heat surface of the second pass on the shell side is formed from heat surface tubes in steam space of this pass and attached at their upper end to the upper tube sheet and at their lower end to another lower tube sheet, through which tubes cooling water of first pass on tube-side flows, whereby said steam spaces are interconnected through an opening between the upper end of a separating wall, dividing the shell space, and an upper tube sheet; whereby the flow direction of the steam in the steam space of the shell side first pass is upwards; and in the other steam space downwards, and the flow direction of the cooling water in the heat surface tubes of both passes is countercurrent to the steam flow flowing outside said tubes. 1. A vertical jacketed straight tube countercurrent condenser for operation at sub-atmospheric pressures , wherein condensing steam flows on the shell side of the condenser and the cooling water on the tube side , wherein the countercurrent condenser is two pass on both the shell side and the tube side , whereby the heat surface of the first pass on the shell side is formed from heat surface tubes attached at their upper end to an upper tube sheet and at their lower end to a lower tube sheet; and the heat surface of the second pass on the shell side is formed from heat surface tubes attached at their upper end to an upper ...

Подробнее
17-10-2019 дата публикации

WASTE HEAT RECOVERY AND CONVERSION SYSTEM AND RELATED METHODS

Номер: US20190316846A1
Автор: FILIPPONE Claudio
Принадлежит:

Various embodiments of a waste heat recovery and conversion system are disclosed. In one exemplary embodiment, the waste heat recovery system may include a heat exchanger for transferring heat from a first fluid to a second fluid and a power conversion unit configured to convert the energy transferred from the first fluid to the second fluid into usable energy. The heat exchanger may include an outer duct defining an inlet and an outlet through which the first fluid flows in and out, respectively, of the outer duct. The heat exchanger may also include an inner duct disposed inside the outer duct and defining an inner channel inside the inner duct and an outer channel between an outer surface of the inner duct and an inner surface of the outer duct. The inner duct may define an internal flow channel through which the second fluid flows to exchange heat energy with the first fluid. 113-. (canceled)14. A system for recovering waste heat from a heat source and converting the recovered waste heat into useable energy , the system comprising:a heat exchanger configured to transfer heat from the heat source to a working fluid;an expander driven by the working fluid and configured to expand the working fluid;a generator-motor coupled to the expander;a compressor coupled to the generator-motor and configured to compress intake air;a condenser defining a fluid reservoir of the working fluid; anda pump disposed between the generator-motor and the compressor and configured to pump the working fluid from the fluid reservoir to the heat exchanger,wherein the heat exchanger, the expander, the fluid reservoir, and the pump comprise a thermodynamic loop that drives the generator-motor.15. The system of claim 14 , wherein the expander claim 14 , the generator-motor claim 14 , and the compressor constitute a power conversion unit for converting the heat from the working fluid into useable energy claim 14 , and wherein the power conversion unit is integrated with a housing of the ...

Подробнее
03-12-2015 дата публикации

Oil-free air compressor having vented cylinder supports

Номер: US20150345486A1
Автор: Mark W. Wood
Принадлежит: Mat Industries LLC

A compressor frame structure is provided for providing flow paths of cooling substance near an upper region of a cylinder, and includes a center ring on the frame structure having an opening for accommodating insertion of the cylinder, a plurality of flow channels near the upper region of the cylinder around an inner surface of the frame structure, and wherein the plurality of flow channels include a plurality of outer flow channels around an outer circumferential surface of the center ring, and a plurality of inner flow channels around an inner circumferential surface of the center ring.

Подробнее
24-11-2016 дата публикации

Improved tube for a heat exchanger

Номер: US20160341491A1
Принадлежит: NEOTISS SAS

A heat exchanger element includes a tubular body with a wall at least partly delimited by an inner surface and an outer surface. The wall has a twisted shape on a segment of the body. The inner surface has a groove with a shape corresponding to the wall. The groove extends helically over the segment. On the segment, the outer surface has a diameter between 18 and 30 millimeters, the groove has a pitch of less than 3.5 millimeters and a depth such that the ratio of the pitch at a real power between 1.5 and 2.5 to the depth is less than a threshold value close to 24. A heat exchanger, for example of condenser type, can include such an element.

Подробнее
01-12-2016 дата публикации

THERMOSYPHON COOLERS FOR COOLING SYSTEMS WITH COOLING TOWERS

Номер: US20160348978A1
Принадлежит:

In one embodiment, a cooling system may include a thermosyphon cooler that cools a cooling fluid through dry cooling and a cooling tower that cools a cooling fluid through evaporative cooling. The thermosyphon cooler may use natural convection to circulate a refrigerant between a shell and tube evaporator and an air cooled condenser. The thermosyphon cooler may be located in the cooling system upstream of, and in series with, the cooling tower, and may be operated when the thermosyphon cooler is more economically and/or resource efficient to operate than the cooling tower. According to certain embodiments, factors, such as the ambient temperature, the cost of electricity, and the cost of water, among others, may be used to determine whether to operate the thermosyphon cooler, the cooling tower, or both. 1. A method for operating a cooling system , comprising:determining a temperature of a cooling fluid exiting a dry heat rejection device;comparing the temperature of the cooling fluid exiting the dry heat rejection device to a cooling temperature set point;reducing a fan speed of one or more fans of the dry heat rejection device when the temperature of the cooling fluid exiting the dry heat rejection device is less than the cooling temperature set point;determining an economic efficiency of operation of the one or more fans of the dry heat rejection device based on a water cost, or an electricity cost, or both when the temperature of the cooling fluid exiting the dry heat rejection device equals or exceeds the cooling temperature set point;increasing the fan speed of the one or more fans of the dry heat rejection device when the economic efficiency of operation of the one or more fans of the dry heat rejection device exceeds a threshold and when the temperature of the cooling fluid exiting the dry heat rejection device equals or exceeds the cooling temperature set point; andreducing the fan speed of the one or more fans of the dry heat rejection device and initiating ...

Подробнее
01-12-2016 дата публикации

THERMOSYPHON COOLERS FOR COOLING SYSTEMS WITH COOLING TOWERS

Номер: US20160348979A1
Принадлежит:

In one embodiment, a cooling system may include a thermosyphon cooler that cools a cooling fluid through dry cooling and a cooling tower that cools a cooling fluid through evaporative cooling. The thermosyphon cooler may use natural convection to circulate a refrigerant between a shell and tube evaporator and an air cooled condenser. The thermosyphon cooler may be located in the cooling system upstream of, and in series with, the cooling tower, and may be operated when the thermosyphon cooler is more economically and/or resource efficient to operate than the cooling tower. According to certain embodiments, factors, such as the ambient temperature, the cost of electricity, and the cost of water, among others, may be used to determine whether to operate the thermosyphon cooler, the cooling tower, or both. 1. A cooling system , comprising:a cooling fluid loop configured to cycle a cooling fluid therethrough;a dry heat rejection system disposed along the cooling fluid loop and configured to transfer heat from the cooling fluid to a refrigerant in an evaporator of the dry heat rejection system, wherein the dry heat rejection system is configured to transfer heat from the refrigerant to ambient atmosphere through dry cooling;a cooling tower disposed downstream of the dry heat rejection system along the cooling fluid loop and configured to transfer heat from the cooling fluid to the ambient atmosphere through evaporative cooling;a pressure sensor configured to measure a pressure of the refrigerant in the evaporator of the dry heat rejection system;a valve of the dry heat rejection system configured to block a flow of the refrigerant to the evaporator when in a closed position; anda controller configured to control operation of the dry heat rejection system based at least on measures of water cost, electricity cost, or a combination thereof, wherein the controller is configured to adjust a position of the valve of the dry heat rejection system based at least on the pressure ...

Подробнее
01-12-2016 дата публикации

Corrosion Resistant Coaxial Heat Exchanger Assembly

Номер: US20160348988A1
Принадлежит:

A heat exchanger assembly is provided which includes a coaxial heat exchanger that is formed, at least in part, of a more corrosion resistant material such as, but not limited to stainless steel, titanium and/or alloys thereof. The assembly further includes a condenser tee connected at each end of the coaxial conduit or tubing defining the heat exchanger. The assembly allows for a non-brazed connection of the condenser tee to an inner tube of the coaxial heat exchanger. In some embodiments, the compression fitting may be connected directly to the heat exchanger without the use of a tee. 1. A coaxial heat exchanger assembly , comprising:a tee formed of one of copper, copper-alloy, brass, brass-alloy, a combination of copper and brass, a combination of copper-alloy and brass-alloy or a combination of any of the foregoing, said tee having a first port, a second port and a third port;one of said first port and second port tapers in diameter from a larger size to a smaller size, and wherein said one of said first port and second port comprises an interference fit compression fitting;said third port receives a refrigerant tube;the other of said first port and second port receives a coaxial heat exchanger including an inner conduit of a first material which is relatively more resistant to corrosion, and an outer jacket of a second material which is relatively less resistant to corrosion;wherein said refrigerant tube provides a refrigerant to flow on an outside of said inner conduit, and wherein said inner conduit is configured to receive a more corrosive fluid;wherein said inner conduit extends through said tee and said first port and said compression fitting eliminating a brazing of said inner tube to said tee, while said second port and said third port comprise at least one of brazing or a high temperature high pressure resin.2. The coaxial heat exchanger assembly of claim 1 , further wherein said assembly is capable of withstanding temperature above 150° F.3. The ...

Подробнее
08-12-2016 дата публикации

BLOOD PROCESSING UNIT WITH MODIFIED FLOW PATH

Номер: US20160354529A1
Принадлежит:

A blood processing apparatus may include a heat exchanger and a gas exchanger. At least one of the heat exchanger and the gas exchanger may be configured to impart a radial component to blow flow through the heat exchanger and/or gas exchanger. The heat exchanger may be configured to cause blood flow to follow a spiral flow path. 1. A blood processing apparatus comprising:a housing having a blood inlet and a blood outlet, the blood inlet extending into an interior of the housing;a heat exchanger core arranged within the housing and having a core aperture disposed near a first end of the housing such that blood passing from the blood inlet may flow through the core aperture to an exterior of the heat exchanger core;heat exchanger hollow fibers disposed about the heat exchanger core such that a heat exchanger fluid may flow through the heat exchanger hollow fibers and blood passing from the core aperture may flow across the heat exchanger hollow fibers;a cylindrical shell extending coaxially about the heat exchanger core and having an annular shell aperture disposed near a second end of the housing such that blood passing from the core aperture may flow to the annular shell aperture imparting a longitudinal blood flow component to the blood, the cylindrical shell configured to impart a shell radial flow component to the blood passing from the core aperture to the annular shell aperture; andgas exchanger hollow fibers disposed about the cylindrical shell such that gases may flow through the gas exchange hollow fibers and blood passing from the annular shell aperture may flow across the gas exchanger hollow fibers.2. The blood processing apparatus of claim 1 , wherein the cylindrical shell has an inner surface that includes one or more radially disposed shell ribs configured to impart the shell radial flow component to blood flow across the heat exchanger hollow fibers.3. The blood processing apparatus of claim 1 , wherein the cylindrical shell has an inner surface that ...

Подробнее
07-12-2017 дата публикации

FIBONACCI OPTIMIZED RADIAL HEAT TRANSFER

Номер: US20170350662A1
Принадлежит:

A heat transfer device for transferring heat energy to or from a gas or fluid flowing radially across a plurality of posts or tubes includes a plate having a plate surface. A plurality of posts or tubes are disposed on and protrude substantially perpendicular to the plate surface. At least about 50% of the plurality of posts or tubes are disposed according to a phyllotaxis layout. Each arc of a plurality of phyllotaxis spiral arcs of the phyllotaxis layout terminates at different locations along an arc radius on the plate at a phyllotaxis arc termination radius less than a perimeter radius. 1. A heat transfer device for transferring heat energy to or from a gas or fluid flowing radially across a plurality of posts or tubes comprising:a plate having a plate surface; anda plurality of posts or tubes disposed on and protruding substantially perpendicular to said plate surface, at least about 50% of said plurality of posts or tubes disposed according to a phyllotaxis layout; andeach arc of a plurality of phyllotaxis spiral arcs of said phyllotaxis layout terminates at different locations along an arc radius on said plate at a phyllotaxis arc termination radius less than a perimeter radius.2. The heat transfer device of claim 1 , wherein at least one or more posts or tubes of said plurality of posts or tubes comprises a heat pipe.3. The heat transfer device of claim 1 , wherein a surface of at least one or more posts or tubes of said plurality of posts or tubes comprises a nano texture or a semi-porous surface treatment or material deposit.4. The heat transfer device of claim 1 , wherein a surface of at least one or more posts or tubes of said plurality of posts or tubes comprises a surface treatment or a variable density surface treatment.5. The heat transfer device of claim 1 , wherein said phyllotaxis layout comprises a Fibonacci optimized radial heat transfer (FORHT) pattern claim 1 , and a plurality of phyllotaxis spiral arcs comprise a first number of clockwise ...

Подробнее
15-12-2016 дата публикации

THERMAL GRADIENT HYDROELECTRIC POWER SYSTEM AND METHOD

Номер: US20160363114A1
Принадлежит:

A thermal gradient hydroelectric power system and method is disclosed herein. Specifically, the method can comprise cycling through a submersed evaporator warm from a natural warm water source, said warm water source having a first temperature. The method also can comprise evaporating a working fluid using said evaporator, and routing the working fluid from the evaporator through a vapor line to a condenser above said evaporator. Finally, the method can also comprise cycling through a condenser cold water from a natural cold water source, the cold water source having a second temperature, and condensing the working fluid, the working fluid having a boiling point between said first temperature and said second temperature. 2. The system of wherein said natural warm water source comes from a first portion of a body of water claim 1 , and said natural cold water source comes from a second portion of said body of water.3. The system of wherein said first portion of said body of water is above said second portion of said body of water.4. The system of wherein said liquid line second end connects to said turbine system inlet by a flow control valve.5. The system of wherein said condenser is submersible.6. The system of further comprising a bio fouling protection system connected to said cold water inlet claim 1 , said bio fouling protection system connectable to said natural cold water source.7. The system of further wherein said bio-fouling protection system creates sodium hypochlorite from seawater.8. The system of further wherein said bio-fouling protection system further connects to said warm water inlet.9. The system of wherein said condenser is more than one hundred meters higher than said evaporator.10. The system of wherein said condenser is more than four hundred meters higher than said evaporator.11. The system of wherein said working fluid is 1 claim 1 ,1 claim 1 ,1 claim 1 ,2 claim 1 ,3 claim 1 ,3 claim 1 ,3-Heptafluoropropane CF3-CHF—CF3.12. A method of ...

Подробнее
15-12-2016 дата публикации

HEAT EXCHANGER

Номер: US20160363379A1
Принадлежит:

The invention relates to a heat exchanger, preferably for motor vehicles, comprising a heat exchanger body (), a first fluid channel (), which is flowed through by a first fluid (), and a second fluid channel (), which is flowed through by a second fluid (), wherein one of the fluids, either the first fluid () or the second fluid () is warmer than the other of the fluids, the first fluid () or the second fluid (), wherein, after entering a heat exchanging region, a heat transfer () from the warmer fluid () to the colder fluid () takes place in the heat exchanging region, wherein the first channel () and the second fluid channel () have in the heat exchanging region at least two shared co-current regions () and a shared counter-current region () arranged between the co-current regions (), or have at least two shared counter-current regions () and a shared co-current region () arranged between the counter-current regions (). 1. A heat exchanger , preferably for motor vehicles , said heat exchanger comprising:a heat exchanger bodya first fluid duct through which a first fluid can flow, and;a second fluid duct through which a second fluid can flow,wherein one of the first fluid and the second fluid is a relatively warm fluid and warmer than the other of the first fluid and the second fluid, which is a relatively cool fluid,wherein, during use of the heat exchanger with the first fluid and the second fluid, after said fluids enter a heat exchange region, heat transport from the relatively warm fluid to the relatively cool fluid takes place in the heat exchange region, andwherein the first fluid duct and the second fluid duct have, in the heat exchange region, at least two common codirectional-flow regions and one common counterdirectional-flow region arranged between the codirectional-flow regions, or at least two common counterdirectional-flow regions and one common codirectional-flow region arranged between the counterdirectional-flow regions.2. The heat exchanger as ...

Подробнее
14-12-2017 дата публикации

Finned Heat Exchanger

Номер: US20170356692A1
Принадлежит:

The present invention is directed to a finned heat exchanger comprising an inner annulus, an outer annulus, a plurality of fins, and an outer chamber. The plurality of fins extends radially outward from the outer surface of the inner annulus toward the inner surface of the outer annulus. The outer chamber is located between the inner annulus and the outer annulus. The plurality of fins is located within the outer chamber. A method of heating or cooling a fluid using the finned heat exchanger and a method of forming the finned heat exchanger are also disclosed. 1. A finned heat exchanger comprising:an inner annulus defining an inner chamber, the inner annulus having an inner surface and an outer surface;an outer annulus having an inner diameter larger than an outer diameter of the inner annulus, the outer annulus having an inner surface and an outer surface;a plurality of fins extending radially outward from the outer surface of the inner annulus toward the inner surface of the outer annulus; andan outer chamber between the inner annulus and the outer annulus, wherein the plurality of fins are located within the outer chamber.2. The finned heat exchanger according to claim 1 , wherein the fins do not contact the inner surface of the outer annulus.3. The finned heat exchanger according to claim 1 , wherein the fins extend 50% or more to less than 100% of the distance between the outer surface of the inner annulus and the inner surface of the outer annulus.4. The finned heat exchanger according to claim 1 , wherein the fins extend 60% or more to less than 90% of the distance between the outer surface of the inner annulus and the inner surface of the outer annulus.5. The finned heat exchanger according to claim 1 , wherein the finned heat exchanger further comprises a plurality of fins extending radially inward from the inner surface of the inner annulus.6. The finned heat exchanger according to claim 1 , wherein a plurality of channels are formed between the plurality ...

Подробнее
22-12-2016 дата публикации

HEAT EXCHANGER

Номер: US20160370131A1
Принадлежит:

The present disclosure relates to a heat exchanger with a particular crimped joint configuration between the manifold and the main body of the heat exchanger. To achieve the joint, the manifold comprises cavities distributed close to its perimetral edge, i.e., the edge that is coupled to the main body. The main body has a stepped seat on which the manifold is supported. Around the seat, the main body has a segment externally surrounding the manifold, at least in a band adjacent to its perimetral edge. This perimetral band has slots defining strips located between the slot and the free edge such that the strips, which are plastically deformed towards the inside of the cavities of the shell, establish a joint with a very rigid and strong coupling force. 2. The heat exchanger according to claim 1 , wherein the baffle of the main body extends claim 1 , around the perimeter thereof claim 1 , towards the manifold according to two consecutive segments:a first segment of the baffle being supported on the inner face of either the shell or of the main body, and a second segment of the baffle giving rise to the segment of the main body externally surrounding the manifold, extending at least by a band adjacent to its perimetral edge; and wherein, andbetween the first segment and the second segment, the baffle comprises a transition configured according to stepping, this stepping being the stepping of the main body establishing support for the perimetral edge of the manifold.3. The heat exchanger according to claim 1 , wherein the surface of the cavity of the manifold on which the strip is supported is inclined such that the greater the deformation of the strip towards the inside of the cavity claim 1 , the greater the compression between the manifold and the baffle.4. The heat exchanger according to claim 1 , whereinthe perimetral edge of the manifold is supported directly on the stepping; andthe perimetral edge of the manifold has a step giving rise to a housing which houses ...

Подробнее
21-11-2019 дата публикации

ANNULAR HEAT EXCHANGER

Номер: US20190353428A1
Автор: Sumera Pavel
Принадлежит:

An annular heat exchanger comprising at least two circumferentially enclosed tube profiles () arranged inside each other for media flow and having a thermal conductive structure () arranged inside. The thermal conductive structure () comprises a helically tightly wound pair of bands () lying on each other, the first band () being smooth, the other band () being corrugated transversally to the winding direction to create flow channels (). 1. An annular heat exchanger comprising of at least two circumferentially enclosed tube profiles arranged inside each other for media flow and having a thermal conductive structure arranged inside , wherein the thermal conductive structure comprises a helically tightly wound pair of bands comprising a first band and an other band lying on each other , the first band being smooth , and the other band being corrugated transversally to a winding direction to create flow channels.2. The annular heat exchanger according to claim 1 , wherein the tube profiles have a circular claim 1 , oval or rectangular cross-section.3. The annular heat exchanger according to claim 1 , wherein the thermal conductive structure completely fills the tube profiles.4. The annular heat exchanger according to claim 2 , wherein the thermal conductive structure completely fills the tube profiles. The invention relates to an annular heat exchanger comprising at least two circumferentially enclosed tube profiles arranged inside each other for media flow and having a thermal conductive structure arranged inside.Heat exchangers comprised of at least two tubes for media flow arranged inside each other are sometimes referred to as “tube-in-tube” exchangers. The tube in “tube-in-tube” exchangers has two principal functions—it separates the media and at the same time serves as a heat-exchange surface. Thermal convection from the media to the heat exchanger material is decisive for the exchange of heat, while thermal conduction is present to a minimal extent, just by the ...

Подробнее
17-12-2020 дата публикации

FLOW-GUIDING ROD, BUSHING AND CONVERTER TRANSFORMER SYSTEM

Номер: US20200395159A1
Принадлежит:

A flow-guiding rod includes a cooling channel provided in a rod portion of the flow-guiding rod, and a coolant inlet pipe and a coolant outlet pipe provided on end(s) of the flow-guiding rod. The coolant inlet pipe and the coolant outlet pipe are communicated with the cooling channel. 1. A flow-guiding rod , comprising:a rod portion including a cooling channel therein; anda coolant inlet pipe and a coolant outlet pipe provided at end(s) of the road portion, wherein the coolant inlet pipe and the coolant outlet pipe are communicated with the cooling channel.2. The flow-guiding rod according to claim 1 , wherein the coolant is cooling water claim 1 , the cooling channel is a water cooling channel claim 1 , the coolant inlet pipe is a water inlet pipe claim 1 , the coolant outlet pipe is a water outlet pipe claim 1 , and the water inlet pipe and the water outlet pipe are connected to a water cooling circulation loop of a converter valve tower.3. The flow-guiding rod according to claim 2 , wherein the rod portion of the flow-guiding rod is of a tubular shape claim 2 , and the water cooling channel is disposed in a tube hole of the rod portion and is configured to extend along a length direction of the rod portion.4. The flow-guiding rod according to claim 3 , wherein a joint of the water inlet pipe jointed with the water cooling circulation loop of the converter valve tower and a joint of the water outlet pipe jointed with the water cooling circulation loop of the converter valve tower are located on a same end of the flow-guiding rod; a water outlet of the water inlet pipe and a water inlet of the water outlet pipe are respectively located on two ends of the water cooling channel along an axial direction of the flow-guiding rod.5. The flow-guiding rod according to claim 2 , wherein the rod portion of the flow-guiding rod is of a tubular shape claim 2 , and the rod portion includes a tube wall which is hollow; the water cooling channel is disposed inside the tube wall ...

Подробнее
10-03-2009 дата публикации

Increased capacity sulfur recovery plant and process for recovering elemental sulfur

Номер: US7501111B2
Принадлежит: ConocoPhillips Co

Claus sulfur recovery plants that include one or more single-stage or multi-stage compact tubular Claus catalytic reactor-heat exchanger units are disclosed. In some instances, these new or improved Claus plants additionally include one or more compact heat exchanger containing cooling tubes that are filled with a heat transfer enhancement medium. The new compact tubular Claus catalytic reactor-heat exchanger units and HTEM-containing heat exchangers are also disclosed. A process for recovering sulfur from a hydrogen sulfide-containing gas stream, employing the new tubular Claus catalytic reactor-heat exchanger unit, and in some instances a HTEM-containing heat exchanger, are also disclosed.

Подробнее
01-12-2011 дата публикации

Thermosyphon coolers for cooling systems with cooling towers

Номер: US20110289951A1
Принадлежит: Johnson Controls Technology Co

In one embodiment, a cooling system may include a thermosyphon cooler that cools a cooling fluid through dry cooling and a cooling tower that cools a cooling fluid through evaporative cooling. The thermosyphon cooler may use natural convection to circulate a refrigerant between a shell and tube evaporator and an air cooled condenser. The thermosyphon cooler may be located in the cooling system upstream of, and in series with, the cooling tower, and may be operated when the thermosyphon cooler is more economically and/or resource efficient to operate than the cooling tower. According to certain embodiments, factors, such as the ambient temperature, the cost of electricity, and the cost of water, among others, may be used to determine whether to operate the thermosyphon cooler, the cooling tower, or both.

Подробнее
07-10-1975 дата публикации

Cooling apparatus and process

Номер: US3910347A
Автор: Herman N Woebcke
Принадлежит: Stone and Webster Engineering Corp

An apparatus and process for effecting heat exchange between hot effluent and a coolant. The heat exchange apparatus is substantially tubular in shape and is provided with a divergent inlet section having an angle of divergence less than 10*, and preferably 4* to 7*.

Подробнее
27-02-1906 дата публикации

Tubes, single or compound, with longitudinal ribs.

Номер: US813918A
Автор: Albert Schmitz
Принадлежит: Individual

Подробнее
30-08-1990 дата публикации

Double-pipe heat-exchanger

Номер: SU1589026A1

Изобретение относитс  к теплообменным устройствам и может использоватьс  дл  интенсификации теплообмена и повышени  эксплуатационной надежности при обработке в зких продуктов в технике нефтедобычи. Теплообменник типа "труба в трубе" содержит концентрично расположенные внутреннюю 1, промежуточную 2 и наружную 3 трубы и спиральную вставку 4 (СВ), размещенную в зазоре между трубами 1 и 2. СВ 4 выполнена в виде проволоки из упругого материала, диаметр которого составл ет 0,1-0,2 наружного диаметра трубы 1, а шаг СВ 4 - 4-6 диаметра проволоки. СВ 4 установлена в контакте с поверхностью трубы 1 с возможностью осевого и поперечного перемещени  под действием потока и с зазором относительно поверхности трубы 2, составл ющим 0,2-0,5 диаметра проволоки. Трубы 1-3 имеют патрубки 5-7 и 8-10 соотвественно дл  подвода и отвода теплообменивающихс  потоков. ВС 4 размещена между перегородками 11, имеющими отверсти  12 дл  прохода потока. При прохождении гор чего потока по трубам 1 и 3, а холодного (в зкого) - по трубам 2 за счет выполнени  СВ 4 из проволоки, размещенной с возможностью осевого и поперечного перемещений, движение нагреваемого потока происходит в турбулентном режиме, а проволока, вибриру  при этом, обеспечивает интенсивное перемешивание в зкого потока. 3 ил. The invention relates to heat exchangers and can be used to intensify heat exchange and increase operational reliability when processing viscous products in oil production techniques. The tube-in-tube heat exchanger contains concentrically arranged inner 1, intermediate 2 and outer 3 pipes and spiral insert 4 (CB) placed in the gap between pipes 1 and 2. CB 4 is made in the form of a wire made of an elastic material whose diameter is 0.1-0.2 outer diameter of the pipe 1, and the step CB 4 - 4-6 diameter of the wire. The CB 4 is installed in contact with the surface of the pipe 1 with the possibility of axial and lateral movement under the action of flow and with a gap relative to the surface of the pipe 2, ...

Подробнее
20-12-1996 дата публикации

Heat exchanger

Номер: RU2070700C1
Принадлежит: Сименс АГ

FIELD: heat engineering. SUBSTANCE: heat exchanger has outer shell 5 with primary chamber 2 for hot primary medium and secondary chamber 3 for secondary medium; these chambers are separated by gastight heat- conducting wall 4. Profiled partition 6 mounted in chamber 3 divides this chamber into inner section 3a and outer section 3b. Partition 6 may be mounted in direction of motion of flow of primary medium and may be profiled in plane perpendicular to it. EFFECT: enhanced reliability. 16 cl, 2 dwg 00210140Сс ПЧ ГЭ РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (19) ВИ "” 2 070 700 ' (51) МПК 13) СЛ Е 28 0 7/10, Е 28Е 9/22 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 5010829/06, 17.02.1992 (30) Приоритет: 18.02.1991 ОЕ Р 4104959.4 (46) Дата публикации: 20.12.1996 (56) Ссылки: Европейский патент М 0302310, кл. С 10 В $300, 1989. (71) Заявитель: Сименс АГ (0Е) (72) Изобретатель: Хартмут Херм[ОЕ], Карл Май[0Е] (73) Патентообладатель: Сименс АГ (ОЕ) (54) ТЕПЛООБМЕННИК (57) Реферат: Использование: в теплотехнике. Сущность изобретения: повышение надежности обеспечивается тем, что в теплообменнике, содержащем наружный корпус 5 с первичной камерой 2 для горячей первичной среды и вторичной камерой 3 для вторичной среды, отделенными друг ОТ друга газонепроницаемой теплопроводной стенкой 4, во вторичной камере З установлена профилированная перегородка 6, разделяющая последнюю на внутренний За и наружный ЗБ отсеки. Перегородка 6 может быть установлена в направлении движения потока первичной среды и профилирована в плоскости, перпендикулярной ему. 15 з.п. ф-лы, 2 ил. 2070700 С1 КО 00210140Сс ПЧ ГЭ КУЗЗАМ АСЕМСУ ГОК РАТЕМТ$ АМО ТКАОЕМАКК$ (19) ВИ "” 2 070 700 Сл (51) ПЕ С1.68 Е 28 р 7/10, Е 28 Е 9/22 12) АВЗТКАСТ ОЕ 1МУЕМТОМ (21), (22) АррИсаНоп: 5010829/06, 17.02.1992 (30) Рпогйу: 18.02.1991 ОЕ Р 4104959.4 (46) Бае ог ричбИсаНоп: 20.12.1996 (71) АррИсапе: Зтеп$ АС (0Е) (72) пуетщог. — Кпайти Кпегт[ОЕ], Кап МаОЕ] (73) Ргорпеюг: Зитеп$ АС (О0Е) (54 ...

Подробнее
18-12-2012 дата публикации

Energy conservation type silencer assembly and vacuum pump with the same for manufacturing of semiconductor and heat method of nitrogen gas

Номер: KR101213780B1
Автор: 이승룡

본 발명은 에너지 절약형 사일런서 어셈블리와 이를 구비한 반도체 제조용 진공펌프 및 질소가스의 가열방법에 관한 것으로 사일런서 자체 표면의 높은 온도를 이용하여 질소가스를 가열하고 이를 사일런서의 내부로 공급함으로써 반응부산물의 고형화로 인한 막힘문제를 해소하면서도 별도의 열원 사용에 따른 에너지 비용을 절감할 수 있는 것이다. 이러한 본 발명 중 에너지 절약형 사일런서 어셈블리의 경우, 진공펌프에서 반응부산물 가스를 펌핑하는 펌프부의 배출측에 연결되어 펌핑된 반응부산물 가스를 후단부로부터 선단부로 통과시키는 사일런서와, 사일런서의 외주면을 이격되게 둘러싸서 사일런서와의 사이에 가열공간을 마련하는 외관과, 가열공간으로 질소가스를 공급하는 질소가스 공급부와, 가열공간에서 사일런서의 외주면에 접촉하여 가열된 질소가스를 사일런서의 내부로 분사하는 질소가스 분사부를 포함하여 구성된다. The present invention relates to an energy-saving silencer assembly, a vacuum pump for semiconductor manufacturing and a method for heating nitrogen gas having the same, and heating nitrogen gas using a high temperature of the silencer's own surface and supplying it into the silencer to solidify the reaction by-product. It is possible to reduce the energy cost of using a separate heat source while eliminating the clogging problem. In the case of the energy-saving silencer assembly of the present invention, the silencer which is connected to the discharge side of the pump unit for pumping the reaction byproduct gas in the vacuum pump and passes the pumped reaction byproduct gas from the rear end to the distal end, and surrounds the outer peripheral surface of the silencer Wrap the outer space to provide a heating space between the silencer, nitrogen gas supply unit for supplying nitrogen gas to the heating space, and nitrogen gas injection for injecting heated nitrogen gas into the silencer in contact with the outer peripheral surface of the silencer in the heating space. It is configured to include a wealth.

Подробнее
10-11-2020 дата публикации

cooling system and method for operating the cooling system

Номер: BR112012030204B1
Принадлежит: Johnson Controls Technology Company

REFRIGERADORES DE TERMO-SIFÃO PARA SISTEMAS DE REFRIGERAÇÃO COM TORRE DE ESFRIAMENTO. Em uma modalidade, um sistema de esfriamento pode incluir um term-sifão refrigerador que refrigera um fluido de refrigeração através de refrigeração seca e uma torre de esfriamento que refrigera um fluido de refrigeração através de refrigeração evaporadora. O termo-sifão refrigerador pode usar convecção natural para circular um refrigerante entre um invólucro e o tubo evaporador e um condensador de ar refrigerado. O termo-sifão refrigerador pode estar localizado no sistema de esfriamento a montante de, e em série com, a torre de esfriamento, e pode ser operado quando o termo-sifão refrigerador é mais eficiente economicamente e/ou em recurso para operar do que a torre de esfriamento. De acordo com certas modalidades, fatores, como a temperatura ambiente, o custo da eletricidade e o custo da água, entre outros, podem ser usados para determinar se operar o termo-sifão refrigerador, a torre de esfriamento, ou ambos. THERMO-SIPHON REFRIGERATORS FOR COOLING SYSTEMS WITH COOLING TOWER. In one embodiment, a cooling system can include a cooler siphon that cools a cooling fluid through dry refrigeration and a cooling tower that cools a cooling fluid through evaporative cooling. The cooler siphon can use natural convection to circulate a refrigerant between an enclosure and the evaporator tube and a cooled air condenser. The cooler siphon can be located in the cooling system upstream of, and in series with, the cooling tower, and can be operated when the cooler siphon is more economically efficient and / or resource to operate than the cooling tower. According to certain modalities, factors, such as room temperature, the cost of electricity and the cost of water, among others, can be used to determine whether to operate the cooler siphon, the cooling tower, or both.

Подробнее
11-04-2017 дата публикации

Вихревой теплообменный элемент

Номер: RU2615878C1

Изобретение относится к теплотехнике и может быть использовано в теплообменниках, применяемых в различных областях техники. Вихревой теплообменный элемент содержит соосно расположенные одна в другой теплообменные цилиндрические трубы большего диаметра и внутреннюю трубу с цилиндрическими поверхностями, при этом труба большего диаметра разделена на участки, внутри каждой из труб установлены, по крайней мере, два завихрителя одинакового или разного типов, при этом каждый завихритель выполнен в виде суживающегося сопла, а внутренняя поверхность его покрыта нанообразной стеклоподобной пленкой из оксида тантала. Технический результат – устранение налипания загрязнений на внутренней поверхности завихрителей. 4 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 615 878 C1 (51) МПК F28D 7/10 (2006.01) B81C 1/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2016110870, 04.07.2016 (24) Дата начала отсчета срока действия патента: 04.07.2016 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 04.07.2016 (45) Опубликовано: 11.04.2017 Бюл. № 11 Адрес для переписки: 305040, Курская обл., г. Курск, ул. 50 Лет Октября, 94, кв. ЮЗГУ, УИР (56) Список документов, цитированных в отчете о поиске: RU 2376541 C1, 20.12.2009. RU 2456522 C1, 20.07.2012. US 6082116 A, 04.07.2000. 2 6 1 5 8 7 8 R U (57) Формула изобретения Вихревой теплообменный элемент, содержащий соосно расположенные одна в другой теплообменные цилиндрические трубы большего диаметра и внутреннюю трубу с цилиндрическими поверхностями, при этом труба большего диаметра разделена на участки, внутри каждой из труб установлены, по крайней мере, два завихрителя одинакового или разного типов, причем один завихритель - на входе в участок, а второй - на расстоянии между ними, определяемом полным затуханием вращательного движения закрученного потока при полной тепловой нагрузке, кроме того, вход теплоносителей в каждый из участков трубы большего ...

Подробнее
30-04-1985 дата публикации

Heat exchanger

Номер: SU1153221A1

ТЕПЛООБМЕННИК, содержащий корпус и коаксиально размещенные в нем щшиндры, образунище каналы дл  воздз ха и ЖИДКОСТИ) и устройство дл  очистки теплопередающей поверхности , вьтолненное в виде скребков, соединенных с приводом о .т л и ч аю щ и и с   тем, что, с целью интенсификации теплообмена и повышени  компактности,- цилиндры выполнены с двойными стенками и разомкнуты вдоль образующих с образованием в радиальном сечении щели в виде сектора , под которой дополнительно установлен лоток дл  сбора и удалени  загр знений, а привод скребков выполнен в виде водил, установленных с торцовых сторон цилиндров с возможностью возвратно-вращательного движени  и соединенных со скребками посредством штанг. (Л HEAT EXCHANGER, comprising a housing and coaxially placed shchindriks in it, the formation of channels for air and LIQUID) and a device for cleaning a heat transfer surface, made in the form of scrapers connected to the drive of the purpose of intensification of heat exchange and increase of compactness - the cylinders are made with double walls and are open along the generators with the formation in the radial section of the slit in the form of a sector, under which the tray for collecting and removing soils is additionally installed, and the drive is scraper It is formed as a driven, mounted sides with cylinders, with reciprocating rotary motion and connected with scrapers by means of rods. (L

Подробнее
10-01-2006 дата публикации

Method of treatment of fluocarbon raw

Номер: RU2267352C2

FIELD: methods of treatment of fluocarbon raw. SUBSTANCE: the invention is pertaining to the methods of treatment of fluocarbon raw. The method of treatment of fluocarbon raw provides for heating by means of high frequency induction of a heating zone of a reaction chamber up to the temperature of no more than 950°C, heating in the heating zone of fluocarbon raw, which contains at least one fluocarbon compound, so, that the fluocarbon compound dissociates with production of at least one predecessor of fluocarbon or its reactive kinds; and refrigerating of the predecessor of fluocarbon or its reactive kinds, in the result of which from the predecessor of fluocarbon or its reactive kinds forms at least one more desirable fluocarbon compound. The technical result is conversion of the fluocarbon raw into the useful products by the low-cost reliable non-polluting environment universal and easily controlled method. EFFECT: the invention ensures conversion of the fluocarbon raw into the useful products by the low-cost reliable non-polluting environment universal and easily controlled method. 12 cl, 10 dwg, 3 tbl, 2 ex ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2 267 352 (13) C2 (51) ÌÏÊ B01J 19/12 (2006.01) B01J 19/28 (2006.01) A62D 3/00 (2006.01) F28D 7/10 (2006.01) F28G 3/10 (2006.01) C07C 17/367 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2002122410/15, 09.02.2001 (72) Àâòîð(û): ÂÀÍ ÄÅÐ ÂÀËÜÒ Àéçåê ßêîáóñ (ZA) (24) Äàòà íà÷àëà äåéñòâè ïàòåíòà: 09.02.2001 (73) Ïàòåíòîîáëàäàòåëü(ëè): ÑÀÓÔ ÝÔÐÈÊÀÍ ÍÓÊËÅÀ ÝÍÅÐÄÆÈ ÊÎÐÏÎÐÅÉØÍ ËÈÌÈÒÅÄ (ZA) (30) Ïðèîðèòåò: 10.02.2000 ZA 2000/0636 R U (43) Äàòà ïóáëèêàöèè çà âêè: 27.03.2004 (45) Îïóáëèêîâàíî: 10.01.2006 Áþë. ¹ 01 2 2 6 7 3 5 2 (56) Ñïèñîê äîêóìåíòîâ, öèòèðîâàííûõ â îò÷åòå î ïîèñêå: ÅÐ 0648530 À, 19.04.1995. Õèìè÷åñêà ýíöèêëîïåäè . Ì.: Íàó÷íîå èçäàòåëüñòâî Áîëüøà Ðîññèéñêà Ýíöèêëîïåäè , 1999, ò.5, ñ.209. ÂÀÉÍÁÅÐà À.Ì. Èíäóêöèîííûå ...

Подробнее
23-06-2020 дата публикации

Heat exchanger

Номер: RU2724374C1

FIELD: heat exchange equipment.SUBSTANCE: invention can be used to create heat exchangers. Heat exchanging device housing consists of inlet, central and outlet parts. Central part is made in the form of a hollow cylinder with two bottoms, and inlet and outlet parts are made of several hollow cylindrical shell rings attached to each other. Shells have different diameters, increasing from inlet part to central part and decreasing from central part to outlet part. Number of shells of inlet part corresponds to number of shells of outlet part. Shells are installed in series on both sides of central part of housing so that alternating cavities of first and second components are formed. Heat exchange elements are made in the form of several coaxially installed pipes of different diameter and different length. Pipes of larger diameter and smaller length form peripheral part of heat exchange element, and pipes of smaller diameter and longer length form its central part.EFFECT: heat exchanger is proposed.1 cl, 3 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 724 374 C1 (51) МПК F28D 7/10 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ На основании пункта 1 статьи 1366 части четвертой Гражданского кодекса Российской Федерации патентообладатель обязуется заключить договор об отчуждении патента на условиях, соответствующих установившейся практике, с любым гражданином Российской Федерации или российским юридическим лицом, кто первым изъявил такое желание и уведомил об этом патентообладателя и федеральный орган исполнительной власти по интеллектуальной собственности. (52) СПК (21)(22) Заявка: 2018143023, 06.12.2018 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): Чернышов Валерий Александрович (RU) Дата регистрации: 23.06.2020 (56) Список документов, цитированных в отчете о поиске: SU 186906 A3, 03.10.1966. RU 54731 U1, 27.07.2006. RU 2036407 C1, 27.05.1995. RU 2671669 C1, 06.11.2018. SU 1298505 A1, 23.03. ...

Подробнее
05-03-1999 дата публикации

分離型極低温冷却装置

Номер: JPH1163697A
Принадлежит: Sumitomo Heavy Industries Ltd

(57)【要約】 【課題】 クライオスタット内の液体ヘリウム(LHe) タンク内へ液体ヘリウムを供給する冷却システムとし て、構造が簡単かつ高効率で、しかも機械的・磁気的ノ イズを低減でき、連続運転可能なシステムを実現するこ とを目的とする。 【解決手段】 極低温冷却装置を圧縮機ユニットAと冷 凍機ユニットBとクライオスタットCとで構成し、クラ イオスタットCを構成する第3段熱交換器18とJT弁 19を冷凍機ユニットBから分離してクライオスタット C内に配置し、該クライオスタットCと冷凍機ユニット Bを高圧側供給配管15と低圧側戻り配管16とを内包 する3重管フレキシブルトランスファ−チュ−ブ17で 接続し、冷凍機ユニットBとクライオスタットC間をG Heが移動する閉サイクル運転を可能にした。

Подробнее
16-08-2019 дата публикации

Counterflow recuperator for high-efficiency heat exchange

Номер: RU2697692C2

FIELD: heat exchange. SUBSTANCE: invention relates to heat engineering and can be used in recuperative heat exchangers. In the counterflow recuperator for high-efficiency heat exchange, consisting of inner(s) and external pipes of arbitrary cross-section, located one(s) in the other, as well as supply and discharge headers to them for hot and cold heat carriers, pipes consist of heat conducting pipe sections and heat-insulating spacers located between them, preventing heat propagation along pipes, wherein its outer pipe is either additionally heat-insulated from the outside, or completely made of heat-insulating material. EFFECT: technical result is higher efficiency of heat transfer. 1 cl, 3 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 697 692 C2 (51) МПК F28D 7/10 (2006.01) F28F 9/22 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК F28D 7/103 (2019.05); F28F 9/22 (2019.05) (21)(22) Заявка: 2015150541, 25.11.2015 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): Неница Николай Михайлович (RU) Дата регистрации: 16.08.2019 (43) Дата публикации заявки: 31.05.2017 Бюл. № 16 (45) Опубликовано: 16.08.2019 Бюл. № 23 2 6 9 7 6 9 2 R U (54) ПРОТИВОТОЧНЫЙ РЕКУПЕРАТОР ДЛЯ ВЫСОКОЭФФЕКТИВНОГО ТЕПЛООБМЕНА (57) Реферат: Изобретение относится к области трубы состоят из теплопроводящих трубных теплотехники и может быть использовано в отрезков и расположенных между ними рекуперативных теплообменных аппаратах. В теплоизолирующих прокладок, препятствующих противоточном рекуператоре для распространению тепла вдоль труб, причем его высокоэффективного теплообмена, состоящем внешняя труба либо дополнительно из внутренней(-их) и внешней труб произвольной теплоизолирована снаружи, либо полностью формы сечения, находящихся одна(-и) в другой, выполнена из теплоизолирующего материала. а также подводящих и отводящих коллекторов к Технический результат – повышение ним для горячего и холодного теплоносителей, ...

Подробнее
22-03-1989 дата публикации

Scraping type multicylinder type heat exchanger

Номер: JPS6475891A
Принадлежит: Ebara Corp

Подробнее
22-01-2020 дата публикации

Double tube for heat-exchange

Номер: KR102049353B1

열교환용 이중관이 개시된다. 열교환용 이중관은: 둘레면에 나선 궤적을 따라 교대로 형성된 산부와 골부를 가지고 제1 유체가 관통 유동하도록 안내하는 스파이럴 파이프; 축 방향으로 삽입되는 스파이럴 파이프를 수용하고 제2 유체가 제1 유체와 열교환되도록 제2 유체가 스파이럴 파이프의 둘레면을 따라 축 방향으로 유동하도록 안내하는 외부 파이프; 및 스파이럴 파이프의 둘레면에 형성된 골부에서 제2 유체의 잔류 시간을 증가시키고 이웃한 산부를 지지하기 위해 스파이럴 파이프 또는 골부에 돌출 형성되는 저항부재를 포함한다. 상기 열교환용 이중관은 통상적인 이중관과는 달리, 스파이럴 파이프의 스파이럴 형상 덕분에 외부 파이프 내측에 흐르는 제2 유체의 잔류시간을 증가시키기 위해, 외부 파이프의 내측을 유동하는 제2 유체와 외부 파이프에 축 방향으로 삽입되는 스파이럴 파이프의 내측을 유동하는 제1 유체 사이의 열교환 효율을 향상시킬 수 있고; 스파이럴 파이프의 골부에 상기 골부의 나선 궤적을 따라 그루브를 형성하여 제2 유체의 유동 방향성을 향상시킬 수 있고; 제2 유체의 압력을 감소시키기 위해, 내부 파이프 및 외부 파이프의 단부 조인트 사이에 형성된 공간을 확장시켜 유동을 야기하는 소음을 저감시킬 수 있고; 그리고 골부에 저항부재를 돌출시켜 제2 유체의 잔류 시간을 증가시킴으로써 열교환 효율을 더욱 향상시킬 수 있다. A double tube for heat exchange is disclosed. The double tube for heat exchange includes: a spiral pipe having a peak and a valley formed alternately along a spiral trajectory on a circumferential surface to guide the first fluid to flow therethrough; An outer pipe for receiving the spiral pipe inserted in the axial direction and for guiding the second fluid to flow axially along the circumferential surface of the spiral pipe such that the second fluid exchanges heat with the first fluid; And a resistance member protruding from the spiral pipe or the valley to increase the residence time of the second fluid in the valley formed on the circumferential surface of the spiral pipe and to support the neighboring hill. Unlike the conventional double pipe, the double pipe for heat exchange has a shaft on the outer pipe and the second fluid flowing inside the outer pipe to increase the residence time of the second fluid flowing inside the outer pipe due to the spiral shape of the spiral pipe. Heat exchange efficiency between the first fluid flowing in the inside of the spiral pipe inserted in the direction can be improved; Grooves along the spiral trajectory of the valleys in the valleys of the spiral pipe can improve flow direction of the second fluid; To reduce the pressure of the second fluid, the ...

Подробнее
19-02-2003 дата публикации

Heat exchanger and process for producing a heat exchanger

Номер: KR100353600B1

본 발명은, IC제조라인 등에서 사용되는 열교환기(11)에 관한 것이며, 유지반(retainer disk)(20)에 형성한 복수의 독립적인 튜브지지구멍(23)에 수지튜브(21)의 말단부를 배치하고, 각 수지튜브(21)의 소정의 길이 범위α를 튜브지지구멍(23)의 내부에서 유지반(20)에 융착시켜 일체화하고, 복수의 수지튜브(21)의 유지반(20)과의 융착부를 수지튜브(21)끼리 서로 비 접촉의 비 밀집구조로 하므로서, 융착부의 접합에 신뢰성을 높이고, 동시에 열교환효율을 높여서 열교환기의 소형화를 용이하게 한 것이며, 수지튜브(21)이나 유지반(20)등의 구성부재는 불소수지제의 것을 사용할 수가 있다. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger (11) used in an IC manufacturing line or the like, wherein the end portion of the resin tube (21) is formed in a plurality of independent tube support holes (23) formed in a retainer disk (20). It arrange | positions, the predetermined length range (alpha) of each resin tube 21 is integrated by fuse | melting to the holding board 20 inside the tube support hole 23, and is integrated with the holding board 20 of the some resin tube 21. The resin tube 21 or the holding plate are made easier by minimizing the heat exchanger by increasing the reliability of the welded portion and increasing the heat exchange efficiency at the same time by forming the non-contact structure of the non-contacting resin tubes 21 with each other. As the constituent members such as (20), those made of fluorine resin can be used.

Подробнее
10-06-2005 дата публикации

A heat exchanger of shell - tube type having silicon carbide tube

Номер: KR100494185B1
Автор: 박용묵
Принадлежит: 박용묵

본 발명은 화학공정에서 요구하는 기본 조건인 내압성, 내식성 및 열전도도가 우수할 뿐만 아니라, 성능대비 가격이 저렴한 실리콘 카바이드를 튜브로 제조하여 열교환을 수행함으로써 최적의 반응물 또는 추출물을 얻을 수 있고, 또한 쉘의 양측 커버 공간을 소정부분으로 구획하되, 상기 다수의 구획공간을 통해 열(냉)매체가 튜브 다발측으로 유,출입되도록 하여 쉘내부로 유입되는 반응물의 열교환 효율을 향상시킬 수 있는 실리콘 카바이드 튜브가 구비된 열교환기에 관한 것이다. The present invention not only has excellent pressure resistance, corrosion resistance and thermal conductivity, which are basic conditions required for chemical processes, but also obtains an optimal reactant or extract by performing heat exchange by producing silicon carbide in a tube, which is inexpensive for performance. The silicon carbide tube which partitions both cover spaces of the shell into a predetermined portion and improves the heat exchange efficiency of the reactants introduced into the shell by allowing the heat (cold) medium to flow into and out of the tube bundle through the plurality of partition spaces. It relates to a heat exchanger provided. 본 발명은, 상기 반응유체가 이동할 수 있는 내부공간을 가지되, 외주면 양측에 반응유체가 출입되기 위한 적어도 하나의 유입 노즐과 배출 노즐이 구비된 쉘; 상기 쉘의 양측단면에 구비되며, 대향하는 다수의 지지홀이 축방향으로 형성된 튜브시트; 상기 양측 튜브시트의 대향하는 다수의 지지홀에 각각 끼워져 지지되어 상기 쉘내에 흐르는 반응유체와 열교환을 수행하기 위한 열교환매체를 출입하며, 각각이 실리콘 카바이드 재질로 이루어진 튜브다발; 상기 튜브시트 외부의 쉘 양단부에 설치되며, 내부공간을 확보할 수 있도록 돔형상으로 형성된 쉘 커버; 및 상기 쉘커버의 내부공간을 소정공간으로 구획하여 열교환매체의 공급량 및 흐름방향을 제어하는 열교환매체 분배수단을 포함하는 실리콘 카바이드 튜브가 구비된 열교환기를 제공한다. The present invention includes a shell having an inner space through which the reaction fluid can move, at least one inlet nozzle and an outlet nozzle for allowing the reaction fluid to enter and exit both sides of an outer circumferential surface thereof; Tube sheets provided at both end surfaces of the shell and having a plurality of opposing support holes formed in an axial direction; A tube bundle inserted into and supported by a plurality of opposing support holes of the both side tube sheets to enter and exit a heat exchange medium for performing heat exchange with a reaction fluid flowing in the shell, each of which comprises a silicon carbide material; ...

Подробнее
20-04-2009 дата публикации

HEAT TRANSMISSION SYSTEM FOR COMBUSTION OF FUEL AND HEATING OF TECHNOLOGICAL FLUID AND METHOD OF ITS USE

Номер: RU2007137495A

1. Технологическая система, содержащая: ! первую теплопередающую систему для сгорания топлива и для нагревания технологической текучей среды, причем упомянутая теплопередающая система содержит: ! топливную трубу, имеющую длину и стенку трубы, образующие зону ввода топлива, в которой по упомянутой длине и внутри упомянутой зоны ввода топлива содержится зона предварительного нагревания топлива и зона сгорания; при этом упомянутая зона предварительного нагревания топлива содержит впуск топлива для ввода упомянутого топлива в упомянутую зону предварительного нагревания топлива и выпуск топлива для ввода предварительно нагретого топлива из упомянутой зоны предварительного нагревания топлива в упомянутую зону сгорания; и причем вдоль упомянутой зоны сгорания и в упомянутой стенке трубы выполнено множество отверстий; ! трубу окислителя, которая является наружной по отношению к упомянутой топливной трубе и окружающей ее, и тем самым образующей зону ввода окислителя по упомянутой длине упомянутой топливной трубы; при этом упомянутая зона ввода окислителя включает в себя зону предварительного нагревания окислителя и зону сгорания топлива; причем упомянутая зона предварительного нагревания окислителя имеет впуск окислителя для ввода окислителя в упомянутую зону предварительного нагревания окислителя и выпуск окислителя для ввода предварительно нагретого окислителя из упомянутой зоны предварительного нагревания окислителя в упомянутую зону сгорания топлива; и при этом упомянутое множество отверстий обеспечивает сообщение по текучей среде между упомянутой зоной сгорания и упомянутой зоной сгорания т РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2007 137 495 (13) A (51) МПК F23C 99/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21), (22) Заявка: 2007137495/06, 09.03.2006 (71) Заявитель(и): ШЕЛЛ ИНТЕРНЭШНЛ РИСЕРЧ МААТСХАППИЙ Б.В. (NL) (30) Конвенционный приоритет: 10.03.2005 US 60/660,446 (43) Дата публикации заявки: ...

Подробнее
25-08-2004 дата публикации

Heat exchanger using engine waste heat

Номер: KR200360189Y1
Автор: 가원로
Принадлежит: 가원로

본 고안은, 입출수관(11)(12)을 통하여 유동되는 용수가 엔진의 폐열에 의해 가열되도록 하는 열교환기에 있어서: 전후방이 개방되는 통형의 내부공간이 다수의 배플(26)에 의해 구획되고, 상기 내부공간의 상하류를 연통하는 입출수관(11)(12)을 구비하는 본체(10); 상기 본체(10)의 양단에서 독립된 상부공간과 하부공간을 형성하도록 결합되고, 상부공간으로 배기입출구관(13)(14)과 하부공간으로 냉각수입출구관(15)(16)을 구비하는 커버(20); 상기 양측 커버(20)의 상부공간을 서로 연통하도록 본체(10)를 통과하여 설치되는 상부관체(23); 및 상기 양측 커버(20)의 하부공간을 서로 연통하도록 본체(10)를 통과하여 설치되는 하부관체(25);를 포함하여 이루어진다. The present invention provides a heat exchanger in which water flowing through the inlet and outlet pipes 11 and 12 is heated by waste heat of an engine: a cylindrical inner space in which front and rear sides are opened is partitioned by a plurality of baffles 26, A main body 10 having inlet and outlet pipes 11 and 12 communicating up and down the inner space; Covers provided at both ends of the main body 10 to form independent upper and lower spaces, and having exhaust inlet and outlet pipes 13 and 14 as upper spaces and cooling water inlet and outlet pipes 15 and 16 as lower spaces ( 20); An upper tube body 23 installed through the main body 10 so as to communicate the upper spaces of the both side covers 20; And a lower tube 25 installed through the main body 10 so as to communicate the lower spaces of the both side covers 20 with each other. 효과에 있어서, 산업용으로나 가정용으로 폭넓게 활용함에 따라 연간 전국적으로 소비되는 온수용 보일러의 기름 사용을 크게 절감할 수 있다. In effect, it is possible to greatly reduce the oil use of hot water boilers consumed nationwide annually as it is widely used for industrial or home use.

Подробнее
28-11-1972 дата публикации

Dialysis apparatus with capillary exchanger

Номер: US3704223A
Принадлежит: Dietzsch Hans Joachim GmbH

MEMBRANE CAPILLARY EXCHANGERS INCLUDING MULTIPLE COUNTERCURRENT EXCHANGERS AND THE PROCESS FOR MAKING AND USING THEM ARE DISCLOSED IN THE PRESENT APPLICATION. THE MEMBRANE CAPILLARY IS PRODUCED BY DEPOSITION ONTO AN AUXILIARY CORE FOLLOWED BY BUNDLING A PLURALITY OF THE CAPILLARIES, INTRODUCING A MEANS FOR HOLDING INTO THE ENDS OF THE CORES, CASTING AND HARDENING THE MEANS FOR HOLDING TO THE ENDS OF THE CAPILLARIES, REMOVING THE MOLD AND THEN REMOVING THE AUXILIARY CORES FROM THE INTERIOR OF THE MEMBRANES. THE EXCHANGER IS OPERABLE IN THE CHAMBER FOR DIALYSIS LIQUID TREATMENT.

Подробнее
26-11-2019 дата публикации

Heat exchanger

Номер: RU2707446C1

FIELD: heating equipment. SUBSTANCE: invention relates to heat exchange technology and can be used to create heat exchangers. Heat exchanging device housing consists of inlet, central and outlet parts. Central part is made in the form of a hollow cylinder with two bottoms, and inlet and outlet parts are made of several hollow cylindrical shell rings attached to each other. Shell rings have different diameters, increasing from inlet part to central part and decreasing from central part to outlet part. Number of shell rings of inlet part corresponds to number of shell rings of outlet part. Shell rings are installed in series on both sides of central part of housing so that alternating cavities of first and second components are formed. Heat exchange elements are made in the form of several coaxially installed pipes of different diameter and different length. Pipes of larger diameter and smaller length form peripheral part of heat exchange element, and pipes of smaller diameter and longer length form its central part. EFFECT: heat exchanger is proposed. 1 cl, 3 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 707 446 C1 (51) МПК F28D 7/10 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ На основании пункта 1 статьи 1366 части четвертой Гражданского кодекса Российской Федерации патентообладатель обязуется заключить договор об отчуждении патента на условиях, соответствующих установившейся практике, с любым гражданином Российской Федерации или российским юридическим лицом, кто первым изъявил такое желание и уведомил об этом патентообладателя и федеральный орган исполнительной власти по интеллектуальной собственности. (52) СПК (21)(22) Заявка: 2018143024, 06.12.2018 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): Чернышов Валерий Александрович (RU) Дата регистрации: 26.11.2019 (56) Список документов, цитированных в отчете о поиске: SU 1298505 A1, 23.03.1987. RU 2671669 C1, 06.11.2018. SU 1802292 A1, ...

Подробнее