РАЗБОРНЫЙ КОНДЕНСАТОР АКВАДИСТИЛЛЯТОРА

Устройство для получения дистиллированной воды содержит конденсатор, отличающееся разъемной конструкцией, позволяющий при необходимости удалять образовавшуюся накипь.

Выпарной аппарат

Изобретение относится к технологическим процессам для приготовления продуктов в пищевой промышленности, например для приготовления соусов и паст, и позволяет повысить производительность и экономичность аппарата. Выпарной аппарат содержит вертикальный корпус на опорах, крышку и перемешивающее устройство. Нижняя и верхняя рубашки соединены с помощью трубки для отвода конденсата, нижний конец которой закреплен в нижней части нижней рубашки, а верхний - в нижней части верхней рубашки. Верхняя рубашка обогревается конденсатом, поступающим из нижней, при постоянном контроле температуры з верхней рубашке и ее регулировании в ней путем открытия и закрытия клапана на трубопроводе слива конденсата из верхней рубашки, обеспечивая этим более полное использование тепла пара для нагрева продукта. 1 з.п. ф-лы, 1 ил.

Способ автоматического управления процессом выпаривания

Распределительное устройство для пленочного выпарного аппарата

Изобретение относится к выпарной технике, может быть использовано в пищевой и химической промышленности и позволяет повысить эффективность путем увеличения степени равномерности орошения теплообменных трубок. Распределительное устройство содержит приемную камеру, в днище которой выполнены отверстия для генерации струй жидкости. Под днищем расположены последовательно промежуточный перфорированный лист, имеющий в местах падения струй площадки без перфорации, полностью перфорированный лист и экранный лист, имеющий отверстия над коническими углублениями в виде воронок в трубной решетке. 1 з.п.ф-лы, 3 ил.

Способ автоматического управления многокорпусной выпарной установкой

Изобретение относится к системам автоматического управления вакуум-выпарными установками, применяемыми в пищевой, химической промышленности, биохимических производствах, и позволяет снизить энергозатраты на процесс и повысить эффективность работы системы. Система содержит регуляторы 1, 5 давления греющего пара в первом и сокового пара в последнем корпусах, регулятор 4 концентрации упаренного раствора на выходе выпарной установ ...

Выпарной аппарат со встроенной внутри него вертикально установленной испарительной камерой

Способ управления процессом упаривания растворов в многокорпусной установке

Способ автоматического регулирования процесса уваривания сахарных сиропов

Способ автоматического управления многоступенчатой выпарной установкой "асу мву опи-9

Способ определения оптимального времени остановки выпарной установки на чистку

УСТРОЙСТВО В ВЫПАРИТЕЛЯХ ДЛЯ ОТДЕЛЕНИЯ УВЛЕКАЕМЫХ ПАРОМ КАПЕЛЬ ЖИДКОСТИ

KOMБИHИPOBAHHAЯ ЛOПACTЬ POTOPHOГO ПЛEHOЧHOГO AППAPATA

Способ автоматического управления процессом выпаривания

СПОСОБ АВТОМАТИЧЕСКОГО УПРАВЛЕНИЯ ПРОЦЕССОМ ВЫПАРИВАНИЯ в производстве аммофоса путем /регулирований подачи греющего пара в зависимости от расхода исходного раствора с коррекцией по его плотности, регулирования уровня в annapaie в зависимности от расхода исходного раствора и отвода вторичного пара из аппарата, отличающийся тем, что, с целью снижения себестоимости продукта и увеличения его выхода путём повыше ния точности регулирования, отвод втори: чного пара регулируют в зависимости от температуры в аппарате с коррекцией по плотности исходного раствора.

Узел вакуумного уплотнения

Изобретение относится к лабораторной технике, в частности к ротационным испарителям , используемым для проведения различных тепло- и массообменных процессов, и позволяет повысить герметичность узла за счет возможности самоустановки вкладышей в месте контакта. Для этого во вращающиеся вкладыше выполнены внешняя и внутренняя кольцевые проточки треугольного сечения, смещенные одна относительно другой на толщину стенки вращающегося вкладыша и расположенные от места контакта вращающегося и невращающегося вкладышей на расстоянии не более наружного диаметра и не менее двух толщин стенки вращающегося вкладыша, причем упругость стенки, образованной проточками , не должна быть больше упругости пру-- жины невращающегося вкладыша. 1 ил.

Способ автоматического управления процессом выпаривания в многокорпусной установке

Выпарной аппарат

Изобретение относится к аппаратурному оформлению процессов упаривания, может быть использовано в химической и смежных с ней отраслях промышленности для осуществления упаривания с подводом тепла через теплообменные поверхности и позволяет интенсифицировать процесс упаривания путем повышения удельного теплосъема за счет создания высокоскоростного пристеночного знакопеременного движения раствора и устранения зарастаний теплообменной поверхности. Выпарной аппарат содержит вертикальный цилиндрический корпус 1 с установленными в нем трубными решетками, теплообменные трубы 6, горизонтальную стержневую раму 10, размещенную над верхней трубной решеткой, штоки 12, закрепленные на раме и расположенные соосно и внутри труб, цилиндрические поршни 13, штуцера для подвода-отвода материальных потоков и теплоносителя. На штоках последовательно размещены поршни и перфорированные в центральной части скребки 14, причем поршни расположены с зазором по отношению к внутренним стенкам трубы, а скребки контактируют ...

Узел вакуумного уплотнения в приводе ратационного испарителя

Использование изобретения: изобретение относится к лабораторному оборудованию , в частности к ротационным испарителям. Сущность изобретения: узел снабжен оправкой 2, установленной между шпинделем 5 (Ш) и запрессованным в нее вращающимся вкладышем 1, который контактирует с имеющим кольцевую канавку в месте контакта невращающимся вкладышем 4 (НВ). Оправка 2 соединяется со Ш 5 с помощью резьбы, направление которой противоположно направлению вращения Ш 5, НВ 4 выполнен в виде шайбы, жестко и перпендикулярно закрепленной относительно закругленного конца вращающегося вкладыша 1. 1 ил.

Устройство для охлаждения кристаллизующихся растворов

Аппарат для дегазации суспензий

FLÜSSIGKEITSVERTEILER FÜR VERDAMPFER

Positive drive coupling for rotating evaporator - has elastic coupling element to minimise stress on glass evaporator

A coupling element made of an elastic material is provided in a detachable drive coupling for connecting the vapour tube of a rotary evaporator to a driven tubular sleeve which holds the vapour tube. The vapour tube and coupling each have at least one drive dog for positive transmission. Danger of damage to the glass evaporator and vapour pipe due to assembly/disassembly by unskilled personnel and to the take-up of play in the coupling on start up is minimised. The coupling element is easily replaced by inskilled personnel.

Appts. for concentrating and processing waste liq.

An appts. comprises a steam flow generator for concentrating the waste liq. and a mist separator. The mist separator has a porous film which transmits gas but not liq.; the waste liq. in the form of a steam flow is brought into contact with this film. The steam flow generator can be plumbed into the mist separator or it can be situated in the same container as the mist separator. In the latter case, a baffle plate is placed in a wall between the steam generator and the mist separator. The porous film can be a hollow film. The appts. also comprises a recycling system by which steam, not transmitted by the film, is redirected back to the mist separator. This recycling section contains a system that concentrates the mist steam. The pressure difference across the porous film is changeable. The appts. has tanks in which to store the sepd. clean water and the conc. waste water. Waste liq. from a nuclear power plant has a high electric conductivity, and in this application the appts. requires ...

FLUESSIGKEITSVERTEILEREINRICHTUNG MIT DAMPFABFUEHRUNGSSEKTION FUER GEGENSTROMFALLFILTERVERDAMPFER

WATER EVAPORATION PROCESS

Verfahren und Vorrichtung zum Trennen eines aus einem Extraktor kommenden Stoffgemisches.

Verfahren und Vorrichtung zum Abscheiden der festen Bestandteile aus den Abzugsgasen von Verdampfern

Rotor in einem dünnschichtigen Verdampfer

Rotor in einem Dünnschichtverdampfer mit drehenden Elementen zur Lagerung einer Vielzahl von Schaufeln, dadurch gekennzeichnet, daß die Lagerelemente übereinander angeordnete Ringe (6) umfassen, in denen sowohl bewegliche abschabende Schaufeln (9) als auch gezahnte feststehende abschabende Schaufeln (1) verankert sind, wobei die gezahnten feststehenden abschabenden Schaufeln (1) lösbar an den Ringen (6) verankert sind.

Verdampferrohr für eine Meerwasserentsalzungsanlage

Die Erfindung betrifft ein Verdampferrohr für eine Meerwasserentsalzungsanlage, mittels welcher insbesondere in Gebieten mit geringen Süßwasserreserven Trink- bzw. Brauchwasser aus dem Meer gewonnen wird. Das erfindungsgemäße Verdampferrohr zeichnet sich dabei dadurch aus, daß es aus einem gegen Meerwasser beständigen und zugleich säurefesten Stahl ausgebildet ist und daß es eine Wandstärke zwischen 0,1 mm und 0,5 mm aufweist. Das erfindungsgemäße Verdampferrohr läßt sich wirtschaftlich bereitstellen und einsetzen und zeichnet sich insbesondere durch eine hohe Korrosionsfestigkeit bei gutem Wärmedurchgang aufgrund der dünnen Wandung sowie durch eine gute Beständigkeit gegenüber niedrigen pH-Werten aus. Zudem kann eine Belagsbildung auf den Verdampferrohren zuverlässig verhindert werden. Es ist daher auch für einen wirtschaftlichen Betrieb in nicht kontinuierlich betriebenen Meerwasserentsalzungsanlagen wie z. B. windkraftgetriebenen Meerwasserentsalzungsanlagen geeignet.

FLUESSIGKEITSVERDAMPFER UND BETRIEBSVERFAHREN FUER DIESEN

BATH PANEL

... 1459542 Bath panels; towel rails OMEGA PLASTICS Ltd 22 May 1975 [12 July 1974] 31013/74 Headings A4N and A4U A moulded thermoplastics bath panel comprises a side wall I, an end-wall 9 and a towel rail 6 located in a recessed central portion 5 of the wall 1, the rail 6 being easily accessible to a person using the bath. Each wall is provided with longitudinally extending ribs adjacent its base, the ribs being spaced apart by approximately one inch so that the panel may be parted along the joins between ribs for adjustment. The panel is preferably of polystyrene and the rail may be a plastics rod or a rod or tube of anodized aluminium or chromium plated steel. The panel has flanges 2 which are rounded off at the corners 3, 4.

Means permitting of evaporating or of de-gasifying in vacuo continuously a liquid contained in any vessel or apparatus

Liquids are evaporated or degasified by drawing the liquid from a tank 20 up through a pipe 4 into an evacuated vessel 1 so that the liquid passes through a heater element 7 and then impinges on a baffle 9, finally falling downwardly over perforated plates 8. The vapour and gases evolved are drawn through a pipe 3 and air condenser 10 by a pump 21. Residual liquid passes in heat exchange with the cold liquid through a vessel 19 and is pumped by a pump 16 to a receiver 22, the action of the pump being increased by recirculating part of the liquid through an injector 17. Liquid level in the vessel 1 is maintained constant by a float 6 actuating a clack valve 5.

VACUUM-BRAZING ALUMINIUM CLADDING MATERIAL.

A vacuum-brazing aluminum cladding material consisting of a core member and a first and a second clad which cover at least one surface of the core member. The first clad consists of 6-14% by weight of Si, 0-0.6% by weight of Mg and the balance being at least Al, and the second clad formed on the first clad consists of 0-14% by weight of Si, 0.8-2.5% by weight of Mg and the balancing being at least Al. The second clad has a thickness of at least 5"m, and this thickness and a content of Si determined so as to satisfy a formula t Подробнее

DESALINATION DEVICE

Fluid purifier

The disclosure describes a device for separating a volatile contaminant from a contaminated fluid. The device comprises a vacuum chamber (10) having an internal space (I) that may be at least partially evacuated, a rotating plate arrangement (30) disposed within the vacuum chamber (10), means (25) for introducing the contaminated fluid on to the surface of the plate arrangement, whereby small droplets (36) of the contaminated fluid are centrifugally dispersed from the edge of the rotating plate arrangement (30), said droplets (36) having sufficient residence time within the evacuated space (I) to permit at least a portion of the contaminant to be released, and means (39) for coalescing the small droplets.

A new or improved flash evaporator

... 174,572. Griscom-Russell Co., (Assignees of Sebald, L. E.). Jan. 27, 1921, CG'onvention date]. Generating by reduction of pressures of heated water.-In an apparatus for vaporizing liquids, particularly for evaporating brine or other impure water in producing distilled water for boilerfeed &c., a heating-agent such as steam or flue gases is passed through an inlet 2 on to the outside of a group of tubes 3 through which the liquid to be evaporated is forced by a pump 8. The heated liquid is sprayed through a pipe 11 above the surface of the liquid in the chamber 12. The vapour formed rises through baffles 13 to an outlet 14. A regulating-valve 4 on the pipe 11 retains sufficient pressure in the tubes 3 to prevent evaporation and consequent formation of scale therein. Residual liquid is withdrawn from the chamber 12 by a pipe 15 and recirculated by the pump 8. A continuous supply of fresh liquid and withdrawal of concentrated residual liquid in suitable proportions are maintained by pumps ...

WATER PURIFICATION DEVICE

An apparatus for purifying a fluid

An apparatus for purifying a fluid comprises a receptacle 4a with an inlet 3a for receiving a liquid with one or more contaminants therein, e.g. seawater, the receptacle being configured to be heated to evaporate the liquid, and the receptacle has a vapour outlet 8a through which the fluid in gaseous form may pass with at least part of the contaminant(s) remaining in the receptacle. A pump 2 may deliver the liquid from a reservoir 5 to the inlet. The pump can be powered by wave energy and/or by wind energy. The liquid may be filtered 7 before delivery to the inlet, e.g. to remove material such as seaweed, fish etc. The receptacle may be heated by solar energy, e.g. by direct sunlight. An outer surface of the receptacle may be of a light absorbent material with high thermal conductivity, e.g. formed of a polymer, silicone or glass. The outer surface may be of a light absorbent dark colour, e.g. a matt black colour. The receptacle may be hemispherical in shape. The apparatus may comprise ...

Device for cleaning a fluid in the form of a vapour from a circuit

Device for cleaning a fluid in the form of a vapour from a circuit.

Device for cleaning a fluid in the form of a vapour from a circuit

Device for cleaning a fluid in the form of a vaporfrom a circuit.

Device for cleaning a fluid in the form of a vapour from a circuit

PROCEDURE AND A DEVICE FOR PREVENTING WATER HAMMER AND CONDENSATION SHOCK IN AN EVAPORATOR

PURE STEAM GENERATOR

PROCEDURE AND DEVICE FOR PREHEATING THE LIQUID IN THE DEAERATOR OF EVAPORATION PLANTS

PROCEDURE AND PLANT FOR CATCHING LIQUID

PROCEDURE AND DEVICE FOR PREHEATING THE LIQUID IN THE DEAERATOR OF EVAPORATION PLANTS

INLET ARRANGEMENT FUER A DISK EVAPORATION DEVICE.

AFTER THE WAERMEKOMPRESSORPRINZIP WORKING DISTILLATION DEVICE.

DEMINERALIZATION EQUIPMENT AND - PROCEDURES.

LIQUID CLEANING APPARATUS.

PROCEDURE AND DEVICE FOR THE QUANTITATIVE ENRICHMENT OF VOLATILE CONNECTIONS BY CAPILLARY DISTILLATION

PROCEDURE AND DEVICE FOR THE ENTSALZEN OF SEA WATER

EVAPORATOR PIPE FOR A SEA WATER DESALINATION PLANT

PROCEDURE AND DEVICE FOR THE PROCESSING OF A WASTE LIQUID

Device for cleaning a fluid in the form of a vapor from a circuit

Solar-powered continuous distillation assembly having efficient heat recovery

The invention relates to a distillation assembly (1) which, with the aid of solar energy (2), continuously evaporates a feed liquor (4). Said distillation assembly (1) comprises: a container (3) which contains the feed liquor (4), a container (5) in which the distillate (6) is collected, these containers (3, 5) being in thermal contact, and a compressor (7). The compressor (7) compresses the vapour which is produced by boiling the feed liquor (4) using the concentration of solar energy (2) and/or using negative pressure, into the distillate container (5) such that the vapour condenses there, and the evaporation enthalpy and thermal energy is returned to the feed liquor (4) by the thermal contact.

PLANT AND PROCESS FOR CONCENTRATING TARTARIC ACID

The present invention relates to a plant for concentrating a tartaric acid solution comprising: - a first and a second evaporation unit, in which said first and second evaporation units are arranged in series; - a pump for feeding a diluted tartaric acid solution into said first evaporation unit; - a barometric condenser placed downstream of said second evaporation unit, - a system for feeding a first low-temperature vapor into said first evaporation unit. The present invention also relates to a process for concentrating tartaric acid comprising the steps of: - providing a plant according to the above description; - performing a first concentration, by evaporation, of the diluted tartaric acid solution, inside the first evaporation unit; - performing a second concentration, by evaporation, of the partially concentrated tartaric acid solution from the first evaporation unit, inside the second evaporation unit. The plant and process for concentrating tartaric acid according to the present ...

Vessel for treating liquids

Heat transfer apparatus with positive drive orbital whip rod

Bar confluence rod for concentrates preparation device

Bar confluence rod for concentrates preparation device Abstract The invention relates to a bar confluence rod for the concentrates preparation device using low pressure and low boiling point. The bar confluence rod comprises a rod body; the bar confluence rod is provided with an abutment surface corresponding to the interior 5 crow surface of the cover body, a first arcuate surface opposed invagination is symmetrically arranged to the two side surfaces vertical to the abutment surface, a second arcuate surface opposed invagination is arranged to the top surface parallel to the abutment surface, an overflow prevention edge is formed between the first and 10 second arcuate surface. The first and second arcuate surfaces enlarge the interface between hot and cool so as to incarese the condensing efficiency. The overflow prevention edge makes condensed water drop slide along the first and second arcuate surfaces into the confluence chamber so as to prevent condensed water drop directly 15 from ...

Boiler for concentrates preparation device

Boiler for concentrates preparation device Abstract The invention relates to a boiler for concentrates preparation device using low pressure and low boiling point. The boiler comprises a sealing structure and at the bottom portion thereof is provided with a feeding opening, a discharging opening and a heating unit; the 5 sidewall of the boiler near to the bottom portion is provided with a sampling unit, the upper cover of the boiler is provided with a condensing unit; the collecting portion includes a bar confluence rod fitting well with the interior crow surface of the cover body and a confluence ring fitting well with the interior circumferential surface of 10 the cover body, the confluence ring and the cover body forms a confluence chamber, the cooling portion includes a plurality of coaxial ring like sheets, a water letin duct is arranged to the top ring, a water outlet duct is arranged to the bottom ring. The device of the invention has good reliablility and high efficiency. Fig.2 ...

METHOD AND APPARATUS FOR CLOSING THE VENT OF AN EVAPORATOR

Device for superheating steam

PROCESS AND APPARATUS FOR REGENERATING SULPHURIC ACID

AEROSOL GENERATOR HAVING HEATER IN MULTILAYERED COMPOSITE AND METHOD OF USE THEREOF

An aerosol generator (100) includes a fluid passage (130) arranged between a first (110) and a second layer (120) wherein the first (110) and second (120) layers at least partially define the fluid passage (130). A liquid supply (150) is arranged to provide a fluid in liquid phase to the fluid passage (130). The aerosol generator (130) also includes a heater (180) arranged to volatilize the fluid in the fluid passage (130). An outlet (140) of the aerosol generator (100) is arranged to receive the volatilized fluid and direct the volatilized fluid out of the fluid passage (130). The aerosol generator (100) can be used to generate aerosols containing medicated materials.

PURE DISTILLATE RECOVERY SYSTEM

In the condensing operation of a waste concentration system, water vapor is condensed, by cooling, into liquid condensate which is reboiled so as to drive off and strip gas that has been redissolved into such condensate. The stripped and driven off gas is directly recombined with the undissolved gas without being mixed with the main body of vapors. The resulting mixture is further cooled to remove the remaining portion of water vapor after which the noncondensible gas stream is filtered and cooled.

DESALINATION DEVICE AND PROCESS

DESALINATION DEVICE AND PROCESS A membrane distillation module is provided with a thin, flexible microporous membrane (16) positioned against an impermeable condensor sheet (12) that is stiffer in bending than the membrane. Distillate vapour diffuses through the membrane from a hot feed flowing rapidly past the membrane, and condenses and collects between, and in intimate contact with, the membrane and the condensor sheet. The condensed distillate is stripped by forces exerted by the hot feed acting on the distillate across the membrane, and flows toward a distillate outlet (40) located in the downstream direction of the hot feed flow. Cold feed flows past the condensor sheet in the counter direction to that of the hot feed for absorbing the latent heat of condensation, and is subsequently additionally heated and introduced into the hot feed channel. Expanded microporous polytetrafluorethylene (PTFE) is the preferred membrane material, and a spiral-wound assembly is the preferred configuration ...

WATER PROCESSING DEVICE

A water processing device for removing contaminants from water for consumption, including a heat exchanger (8), a heater (15), a boiler chamber (21), a liquid level control device (24), a demister (23), a degasser (26), and a self-cleaning component (6). A water seal (30) to prevent steam from leaking from the device is also provided.

DESALINIZATION BY EVAPORATION FROM CAPILLARY MATERIAL

A method and an apparatus for desalinizing raw water are disclosed. The method can include wicking the raw water into a porous material by capillary action and heating the raw water in the porous material with a heating element to form water vapor. The water vapor then can be condensed to form purified water. The apparatus can include a chamber (20) for holding raw water, a heating element (24), a sheet of porous material (42) and a chamber (22) for collecting water vapor evaporated from the raw water in the porous material.

MOVEMENT MODIFICATION OF FEED STREAMS IN SEPARATION APPARATUS

A swirl generator is described for use in a cyclonic evaporator to receive fluid axially and discharge the fluid tangentially through one or more outlets (114). The swirl generator is moveable so as to be separated from the evaporation tube so as to facilitate clean in place practices overcoming the need to remove the evaporation tube which can in some instances be up to twelve meters long. Movement of the head (102) allows relatively fast and efficient cleaning of the cyclonic evaporator.

PLANT FOR SEAWATER DESALINIZING USING SOLAR ENERGY PREFERABLY ACCOMPANIED BY ELECTRIC POWER GENERATION

... 2112573 9300299 PCTABS00019 An equipment for desalination of sea water by the utilization of solar energy, advantageously accompanied by electric power generation, containing the heat caption unit (1) serving as a heat source, the sea water collecting tank (10), the pre-heating tank (11), the heat receiver (20), and the condensers (2, 3, 4) connected in line, and the distilled water storage tanks (13). The sea water collecting tank (10) and the pre-heating tank (11) that pre-heats the sea water and cools the distilled steam are situated beside each other by level difference and that the adjoining walls of the two tanks have an opening for through-flow (11a) or a through-flow tube; the discharge duct (8) of the pre-heating tank (11) is led into the condensers where the first condenser (2) is provided with a heater (72) heated by the heating agent, the second and the subsequent evaporators (3) are provided with a heating system consisting of pipe rings (73a) utilizing hot vapour and pipes ...

PROCESS AND DEVICE FOR SEPARATING A MIXTURE OF INGREDIENT SUBSTANCES FROM THE EXTRACTING AGENT

The invention relates to a process and a device for separating a mixture obtained in an extractor and consisting of solvents and ingredient substances, the extraction pressure of the mixture being reduced. The aim of the invention is to design an unsophisticated and rapid separation process particularly suitable for substances of high viscosity. The invention provides for a process wherein the mixture is directly injected into a large chamber via a relief valve.

Heizkörper für Flüssigkeitsverdampfer.

Flüssigkeitsverdampfer.

Ringheizkörper für Flüssigkeitsverdampfer.

Verfahren zur Trennung der Komponenten eines Gemisches von Flüssigkeiten.

Gefäss zur Durchführung von chemischen Reaktionen, Verdampfungsvorgängen und dergleichen.

Heizanlage zur Übertragung von Wärme mit Hilfe eines flüssigen Wärmeträgers

Kessel von Destillationsanlage.

Eindampfungsanlage

Umlaufverdampfer

Verdampfanlage

Verfahren zum Verdampfen von Flüssigkeiten und Einrichtung zur Durchführung des Verfahrens

Verdampfer mit Flüssigkeitsabscheider.

Heizmantel für Rührwerkskessel, Destillierblasen und dergleichen Behälter.

Mehrstufiger konischer Wärmeaustauscher

Flüssigkeitsabscheider für Dünnschichtapparate

Dünnschichtverdampfer

EINSPRITZKUEHLER ZUM KUEHLEN VON WASSER.

Konischer Wärmeaustauscher

Konischer Wärmeaustauscher

Wärmeaustauscher

Verfahren zur Vernichtung von Ölemulsionen

Verfahren und Vorrichtung zur Entgasung flüssiger Suspensionen

PROCEDURE AND DEVICE FOR SEPARATING SOLIDS FROM DREDGING.

Distillation appliance for water

The distillation appliance is constructed in such a way that all moisture fractions in the crude steam supplied thereto are removed, pyrogens, minerals and other contaminants being largely eliminated at the same time, so that the distilled water thus obtained is suitable for medical purposes, e.g. for the preparation of sterile solutions such as injections and the like. The appliance has a steam-drying cylinder (I) and a steam condenser (III), the steam-drying cylinder (I) having the shape of a tubular body (10) arranged vertically or at an angle, which is made of corrosion-resistant material and is packed with corrosion-resistant bodies such as spheres, rings or short tube sections (16). Crude steam enters the tubular body (10) in the region of the bottom part, rises into the top part and leaves this to pass into the steam condenser (III), while contaminated water leaves the steam-drying cylinder (I) through an outlet (14) which is provided on the bottom part thereof and is equipped with ...

DUENNSCHICHT MORE WISCHBLATTVERDAMPFER.

Methods and Apparatuses for Water Purification

An apparatus for generating purified liquid from an input liquid, comprises, an evaporation chamber, wherein the evaporation chamber is flooded with the input liquid; and a condensation chamber having channels, wherein the channels are disposed in the input liquid, wherein liquid-saturated gases are generated from the input liquid in the evaporation chamber, wherein the liquid-saturated gases are guided into a first end of the channels, and wherein the purified liquid is outputted at a second end of the channels.

Settling Chamber for Separation of Large, Plugging Particles Upstream of A Hydroclone

Evaporation technology is commonly used to to treat process waters that contain low solubility salts. The technology typically used is a brine boncentrator which uses seeded slurry techniques internal to the falling film evaporator which allows these scaling salts to co-precipitate with the seed crystals instead of scaling on the heat transfer surface. Such systems often employ hydroclones to recover and recycle seed crystals that would otherwise leave the process with the brine blowdown stream. These hydroclones (or other separation devices) often have regions of tight clearance that are susceptible to plugging which can lead to suboptimal process availability and greater maintenance obligations. The inventors have developed an apparatus called a “settling chamber” for separating large solid particles from the feed stream to the hydroclone to eliminate plugging, improve availability and reduce maintenance requirements. 1. An apparatus for removing large solid particles from an evaporator stream being fed to a hydroclone downstream of said evaporator , comprising:a circulating slurry comprising a brine-concentrating seed bed, anda settling region downstream of said brine-concentrating seed bed, wherein said settling region decreases a fluid flow velocity between an evaporator and a hydroclone downstream of said evaporator, thereby removing, by gravity separation, at least a portion of solid particles flowing from said brine-concentrating seed bed to said hydroclone.2. The apparatus of claim 1 , wherein said settling region prevents said particles from being fed to the hydroclone.3. The process of claim 2 , wherein said hydroclone has an underflow claim 2 , and wherein said underflow of the hydroclone is directed back to a recirculating water to maintain a circulating slurry seed bed sufficient to retard scaling of a heat transfer surface in an evaporator.4. The process of wherein hydroclone has an overflow claim 2 , and wherein said overflow is either discharged or ...

Falling film evaporator

A falling film evaporator, includes an outer shell formed by a cylindrical shell and convex ends, at least one tube bundle formed of vertical tubes arranged inside the outer shell, whereby a heat-releasing, condensable vapour can be fed into the vertical tubes from below upwards, and a heat-receiving, vaporizable liquid can be fed to the upper end of the tube bundle to flow downwards along the outer surface of the vertical tubes as a thin liquid layer, whereby an element for discharging non-condensable gases contained in the heat-releasing vapour has been arranged in the tube bundle. The evaporator includes two or more tube bundles each being provided with a tube plate of its own, whereby the vertical tubes of each tube bundle are at their lower ends attached to the tube plate of the corresponding tube bundle and at their upper ends to collecting manifolds of the corresponding tube bundle.

Alcohol Beverage and Spirits Nosing, Tasting, Drinking, and Sampling Vessel, Procedure or Method for Using Same, and a Process to Separate Ethanol Vapors from Sampling Vapors Prior to Nosing

This application is for a device and article of manufacture for the purpose of drinking, tasting, sampling, and nosing and evaluating alcohol beverages without alcohol nose burn and numbing; a procedure or method to manipulate said vapors for the same purpose; and a process to separate and dissipate ethanol vapors to accomplish the same purpose. The device is one embodiment of a vessel which collects vapors in a chamber with curved sides and large surface area to promote evaporation, which chamber's top opening orifice concentrates same vapors prior to passing into an expansion chamber releasing and dissipating fast moving ethanol prior to nosing, providing improved aroma detection and enhancing nosing, tasting, and sampling experiences for all spirits, wines and liqueurs, distilled, fermented, and fortified.

Method and apparatus for reduction of contaminants in evaporator distillate

A method and apparatus for producing high purity distillate in evaporators is useful for evaporation of waters where volatile silica or organic compounds are encountered such as in production of hydrocarbons from geological formations. An evaporator having a contaminant reduction system is provided. The contaminant reduction system includes an upflow first mist eliminator portion to remove entrained liquid droplets and produce an intermediate purity water vapor stream. A continuous spray system provides a spray of dilute caustic solution in a selected spray configuration for mass transfer contact with the passing intermediate purity water vapor stream, to remove volatile silica compounds therefrom, and produce a partially decontaminated steam stream having mist particles therein. An upflow second mist eliminator portion is provided to remove the residual mist particles, and produce a high purity water vapor stream. The high purity water vapor stream is condensed to provide a high purity distillate stream.

Water Purifying Apparatus

A water purifying apparatus comprising a casing having a circulation path. A splitter device is disposed within the casing and adapted to split raw water into droplets and create a carrier airflow capable of circulating along the circulation path and carrying water vapor evaporated from the droplets. A demister is disposed within the casing at a position downstream of the splitter device in a direction of the carrier airflow and adapted to remove the droplets while permitting the water vapor to pass therethrough. A condenser is disposed within the casing at a position downstream of the demister in the direction of the carrier airflow and adapted to condense the water vapor flowing out of the demister to create purified water. The demister comprises a plurality of demister plates arranged at intervals of a predetermined distance to define a flow passage therebetween. 1. A water purifying apparatus comprising:a casing having a circulation path;a splitter device disposed within the casing and adapted to split raw water into droplets and create a carrier airflow capable of circulating along the circulation path and carrying water vapor evaporated from the droplets;a demister disposed within the casing at a position downstream of the splitter device in a direction of the carrier airflow and adapted to remove the droplets while permitting the water vapor to pass therethrough; anda condenser disposed within the casing at a position downstream of the demister in the direction of the carrier airflow and adapted to condense the water vapor flowing out of the demister to create purified water,wherein the demister comprises a plurality of demister plates arranged at intervals of a predetermined distance to define a flow passage therebetween.2. The water purifying apparatus as defined in claim 1 , wherein each of the demister plates is bent.3. The water purifying apparatus as defined in claim 1 , wherein each of the demister plates is curved.4. The water purifying apparatus as ...

Evaporation device

An evaporation device including an agitation vessel to which raw material liquid is supplied. The agitation vessel has a volatile component outlet and a concentrate outlet, a jacket provided on an outer circumference and configured to heat an inner wall, and a liquid-distributing portion configured to cause the raw material liquid to flow down the inner wall. The agitation vessel includes storage portion surrounded by a bottom, the inner wall, and a partition wall portion configured to temporarily store the raw material liquid that flows down, the liquid-distributing portion is constituted by a rotating shaft and at least one channel part having a flow passage which, as the rotating shaft rotates, the raw material liquid temporarily stored in the storage portion flows upward from a lower side of the agitation vessel. The channel part is mounted to the rotating shaft, and the concentrate outlet is provided in the bottom.

MOBILE MECHANICAL VAPOR RECOMPRESSION EVAPORATOR

A mobile mechanical vapor recompression evaporator system including a horizontal vapor separator and a horizontal forced circulation heat exchanger. The horizontal vapor separator can include a generally cylindrical housing configured in a generally horizontal orientation. The housing can include at least one product chamber having at least one product passage configured to receive at least one product. The housing further includes at least one vapor chamber having at least one vapor passage and at least one vapor window located between the at least one product chamber and the at least one vapor chamber, wherein a portion of the at least one product evaporates in the product chamber to produce a vapor that passes through the at least one vapor window into the at least one vapor chamber, and is discharged through the at least one vapor passage. 1. A vapor separator comprising: at least one product chamber having at least one product passage configured to receive at least one product;', 'at least one vapor chamber having at least one vapor passage; and', 'at least one vapor window located between the at least one product chamber and the at least one vapor chamber;', 'wherein a portion of the at least one product evaporates in the product chamber to produce a vapor that passes through the at least one vapor window into the at least one vapor chamber, and is discharged through the at least one vapor passage., 'a generally cylindrical housing configured in a generally horizontal orientation comprising2. A vapor separator comprising:a generally cylindrical housing configured in a generally horizontal orientation comprising:a first product chamber having a first product passage configured to receive a first product;a second product chamber having a second product passage configured to receive a second product;a vapor chamber positioned between the first product chamber and the second product chamber, the vapor chamber having a vapor passage;a first vapor window located ...

COMPACT EVAPORATOR SYSTEM

A compact evaporator system is provided having a horizontal vapor separator and a horizontal forced circulation heat exchanger utilizing mechanical vapor recompression. The vapor separator has at least one product chamber having at least one product passage configured to receive at least one product. The vapor separator can also have at least one vapor chamber in fluid communication with the at least one product chamber having at least one vapor passage, wherein the at least one vapor chamber has a substantially horizontal orientation. The vapor separate can be configured such that a portion of the at least one product evaporates in the product chamber to produce a vapor that travels into the at least one vapor chamber, residual entrained droplets are removed from the vapor as it flows laterally through the vapor chamber, and the vapor is then discharged through the at least one vapor passage. 1. A vapor separator comprising:at least one product chamber having at least one product passage configured to receive at least one product; and 'wherein a portion of the at least one product evaporates in the product chamber to produce a vapor that travels into the at least one vapor chamber, residual entrained droplets are removed from the vapor as it flows laterally through the vapor chamber, and the vapor is then discharged through the at least one vapor passage.', 'at least one vapor chamber in fluid communication with the at least one product chamber having at least one vapor passage, wherein the at least one vapor chamber has a substantially horizontal orientation;'}2. The vapor separator of claim 1 , further comprising a housing wherein the at least one product passage is configured to enter the housing near the end claim 1 , at the top portion of the housing claim 1 , and direct the product toward a product inlet distributor.3. The vapor separator of claim 1 , wherein the housing further comprises at least one product sump located in the lower section of the at least ...

FRESH WATER GENERATOR

There is provided a combined evaporator and condenser for a fresh water generator. The generator comprises an evaporation unit into which is introduced water to be treated (typically seawater) heated to at least a saturation temperature for the pressure in the evaporation unit for generating vapor by evaporating water from the seawater, and the condenser unit for condensing the evaporated fresh water. Moreover the generator comprises circulation means for returning the brine, after being evaporated in the evaporation part. The generator utilizes specially designed stacked evaporator and condenser plates having a circular form with a flat peripheral portion and a cone like central portion with an aperture in the centre of the plates providing. 2. Fresh water generator according to claim 1 , wherein the evaporator and/or condenser plates are fully or partially made from a material selected from stainless steel claim 1 , aluminium claim 1 , and a polymer claim 1 , such as polycarbonate.3. Fresh water generator according to claim 1 , wherein ultrasound modules are provided on the housing for reducing the accumulation of scaling and the like.4. Fresh water generator according to claim 1 , wherein ultrasound modules are provided in the evaporator unit.5. Condenser or evaporator plate having a circular form with a flat peripheral portion and a cone like central portion with an aperture in the centre of the plate claim 1 , wherein the plate is provided with openings in the flat peripheral portion claim 1 , wherein 2-4 claim 1 , preferably 2 claim 1 , openings are provided claim 1 , whereby the openings constitute 5-30% of the area of the flat peripheral portion.6. Condenser or evaporator plate according to claim 5 , wherein the plate is made from a material selected from stainless steel claim 5 , aluminium claim 5 , and a polymer claim 5 , such as polycarbonate. The present invention relates to a single stage vacuum evaporator, in particular for fresh water generators with ...

Microfluidic System And Method For Performing A Flash Separation Of A Reservoir Fluid Sample

A system for performing a flash separation of a reservoir fluid includes a sample chamber configured to hold the reservoir fluid and a flash apparatus in fluid communication with the sample chamber. The flash apparatus includes a microfluidic device configured to flash the reservoir fluid in fluid communication with the sample chamber, and a separation chamber configured to separate the flashed reservoir fluid into a liquid phase and a gaseous phase in fluid communication with the microfluidic device. The system further includes a gas receptacle configured to store the gaseous phase. A method for performing a flash separation of a reservoir fluid includes providing a reservoir fluid to a microfluidic device, urging the reservoir fluid through the microfluidic device such that the reservoir fluid is lashed within the microfluidic device, and separating a liquid phase and a gaseous phase from the flashed reservoir fluid. 1. A system for performing a flash separation of a reservoir fluid , comprising:a sample chamber configured to hold the reservoir fluid; a microfluidic device configured to flash the reservoir fluid in fluid communication with the sample chamber; and', 'a separation chamber configured to separate the flashed reservoir fluid into a liquid phase and a gaseous phase in fluid communication with the microfluidic device; and, 'a flash apparatus, comprisinga gas receptacle configured to store the gaseous phase in fluid communication with the separation chamber.2. The system of claim 1 , further comprising an adjustment valve between and in fluid communication with the sample chamber and the microfluidic device.3. The system of claim 1 , further comprising a pump for urging the reservoir fluid from the sample chamber.4. The system of claim 3 , wherein:the sample chamber comprises a floating piston dividing the separation chamber into a first chamber and a second chamber;the reservoir fluid is disposed in the second chamber; andthe pump is in fluid ...

Treatment of produced water using indirect heat

Systems and methods utilize heated waste flue gas to indirectly heat untreated water. The heated waste flue gas, which may come from a steam generator, passes through one or more heating coils in a vessel to vaporize untreated water and separate out solids and other contaminants before subsequent condensing. The steam generator may receive resulting treated water to produce steam for injection.

SILICON REFINING EQUIPMENT AND METHOD FOR REFINING SILICON

In this method for refining silicon by vacuum melting, the falling of impurity condensate from an impurity trap located above a crucible and contamination of the molten silicon are prevented. A crucible for housing molten silicon, and a heating means for heating the crucible are located inside a treatment chamber equipped with a vacuum pump; further provided are: an impurity trap having an impurity condensation unit for cooling and condensing the vapor of impurities evaporating from the liquid surface of the molten silicon; and a contamination prevention device for preventing contamination of the molten silicon, having an impurity catch unit for catching impurities when impurities trapped by the impurity trap fall. 1. A silicon purification device for separating and removing the evaporated impurities from the silicon melt generated by the heating and fusion of silicon at reduced pressure , which is provided with a processing chamber at a reduced pressure which is reduced to below a specific pressure by a pressure reduction means , and a crucible containing the silicon which is provided disposed in this processing chamber , and a heating means heating the silicon in this crucible ,characterized in that it is provided with a contamination prevention device preventing contamination of the silicon melt, equipped with an impurities capture device having an impurities condensation means cooling and condensing the vapour of impurities evaporating from the liquid surface of the silicon melt that, as well as an impurities reception means receiving and containing the impurities, when dropping down impurities captured by the impurities capture device,and on the occasion of silicon purification processing, the impurities reception and containment means of the contamination prevention device is located in the standby position, and the vapour of the impurities is condensed by the impurities condensation means of the impurities capture device, and moreover, when the silicon ...

Water Treatment Device

A water treatment system ( 220 ) heats raw water, gasifies a portion thereof by an evaporator ( 34 ), and condenses the gasified steam at a condensation area ( 240 ) to obtain condensed water. The water treatment system ( 220 ) includes a heater ( 32 ) for heating raw water, a steam conducting part ( 35, 36 ) for conducting, to the condensation area ( 240 ), steam gasified from the raw water heated by the heater ( 32 ), and a pipe ( 221 ) for conducting circulating water from the condensation area ( 240 ) to the evaporator ( 34 ), causing heat exchange between the steam conducted to the condensation area ( 240 ) by the steam conducting part ( 35, 36 ) and the circulating water, as well as causing heat exchange between the raw water and the circulating water at the evaporator ( 34 ).

Drum Trap Capable of Condensing/Circulating Vapor and Food Waste Treatment Apparatus Using the Same

Disclosed are a drum trap and a food waste treatment apparatus using the same. In the drum trap according to the present invention and the food waste treatment apparatus using the same, the fetid vapor generated when drying food waste in the drying unit is introduced into the drum trap, condensed, and then discharged to the drain pipe side. In addition, the fetid vapor remaining without being condensed is re-introduced into the drying unit. That is, since the fetid vapor generated when drying the food waste does not leak out to the outside, no separate filter for removing the fetid smell contained in the vapor is required. Accordingly, production costs may be reduced. 1. A drum trap comprising:a housing including an opened top surface and one side surface in which a discharge unit is formed to discharge water, the discharge unit being configured to store water in a bottom side inner portion thereof; anda cooling plate module coupled to the housing to condense vapor introduced into the housing, a first cooling plate coupled to the opened top surface of the housing;', 'a second cooling plate formed to extend downwardly from a bottom surface of the first cooling plate and positioned inside of the housing, a bottom side portion of the second cooling plate being positioned below the discharge unit to be submerged in the water stored in the housing; and', 'an introduction pipe formed to extend downwardly from a central portion of the first cooling plate so as to introduce water into the inside of the housing therethrough,', 'wherein an inlet hole and an outlet hole are formed in one side portion and the other side portion, respectively, so that vapor is introduced into the inside of the housing through the inlet hole, and non-condensed vapor in the vapor introduced into the inside of the housing through the inlet hole is discharged through the outlet hole., 'wherein the cooling plate module comprises2. The drum trap of claim 1 , wherein the cooling plate module is made of ...

DESALINATION SYSTEMS AND ASSOCIATED METHODS

Systems and methods related to the desalination of aqueous solutions containing one or more dissolved salts are generally described. 12-. (canceled)3. A method for desalinating water , comprising:removing, within an ion-removal apparatus, at least a portion of at least one scale-forming ion from an aqueous feed stream comprising the scale-forming ion and at least one dissolved monovalent salt to produce an ion-diminished stream containing less of the scale-forming ion relative to the aqueous feed stream;removing, within a desalination apparatus, water from the ion-diminished stream to produce a concentrated saline stream enriched in the dissolved monovalent salt relative to the ion-diminished stream; andprecipitating, within a precipitation apparatus, at least a portion of the dissolved monovalent salt from the concentrated saline stream to produce a product stream containing less of the dissolved monovalent salt relative to the concentrated saline stream.46-. (canceled)7. The method of claim 3 , comprising recycling at least a portion of the product stream to the desalination apparatus.8. The method of claim 3 , wherein a concentration of the dissolved monovalent salt within the concentrated saline stream differs from a concentration of the dissolved monovalent salt within the ion-diminished stream by no more than about 20%.915-. (canceled)16. A method for desalinating water claim 3 , comprising:removing, within a desalination apparatus, water from an aqueous feed stream comprising at least one dissolved monovalent salt to produce a concentrated saline stream enriched in the dissolved monovalent salt relative to the aqueous feed stream; andprecipitating, within a precipitation apparatus, at least a portion of the dissolved monovalent salt from the concentrated saline stream to produce a product stream containing less of the dissolved monovalent salt relative to the concentrated saline stream,wherein substantially no precipitation of the dissolved monovalent salt ...

SEAWATER DESALINATION DEVICE AND SEAWATER DESALINATION METHOD

Embodiments of the invention provide a seawater desalination device, including a steam re-compressor configured to pressurize steam by pressurizing a steam; a first heat exchanger configured to exchange an amount of sensible heat of seawater to be desalinated with an amount of liquid sensible heat after pressurized steam is condensed, and an amount of sensible heat of a concentrated liquid after seawater is concentrated; a second heat exchanger configured to exchange an amount of heat of pressurized steam, an amount of latent heat of vaporization of seawater, and an amount of sensible heat when seawater is evaporated, and configured to concentrate seawater; a seawater supply means; a steam supply means; a first discharge means; a second discharge means; and a water-droplet separation means. 1. A seawater desalination device for seawater desalination , the device comprising:a steam re-compressor configured to generate pressurized steam by pressurizing a steam;a first heat exchanger configured to exchange an amount of liquid sensible heat of seawater to be desalinated with an amount of liquid sensible heat after the pressurized steam is condensed, and an amount of sensible heat of a concentrated liquid after the seawater is concentrated;a second heat exchanger configured to exchange an amount of heat of the pressurized steam, latent heat of vaporization of the seawater, and an amount of steam sensible heat when the seawater is evaporated, and further configured to concentrate the seawater;a seawater supplier configured to supply the seawater to the first heat exchanger, and further to supply the seawater from the first heat exchanger to the second heat exchanger;a steam supplier configured to supply steam evaporated from the seawater to the second heat exchanger;a first discharger configured to discharge externally either of the concentrated seawater liquid after the seawater is concentrated or salt extracted from the seawater, or both of the concentrated seawater ...

APPARATUS FOR EVAPORATIVE CONCENTRATION OF WATER TO BE TREATED, WHICH USES HOT LIME SOFTENING, AND METHOD FOR EVAPORATIVE CONCENTRATION OF WATER USING THE SAME

An apparatus for evaporative concentration of water, containing hardness-causing substances, to be treated using hot lime softening, includes: a first evaporator configured to form first concentrated water from the water to be treated by evaporatively concentrating the water by first heat exchange with hot steam; a hot lime softener configured to precipitate and to separate hardness-causing substances contained in the first concentrated water from at least a portion of the first concentrated water from the first evaporator by reaction with lime and configured to remove the hardness-causing substances from the first concentrated water; and a second evaporator configured to form second concentrated water by further evaporatively concentrating at least a portion of the first concentrated water that passed through the hot lime softener by second heat exchange with hot steam. 1. An apparatus for evaporative concentration of water , containing hardness-causing substances , to be treated using hot lime softening , the apparatus comprising:a first evaporator configured to form first concentrated water from the water to be treated by evaporatively concentrating the water by first heat exchange with hot steam;a hot lime softener configured to precipitate and to separate hardness-causing substances contained in the first concentrated water from at least a portion of the first concentrated water from the first evaporator by reaction with lime and configured to remove the hardness-causing substances from the first concentrated water; anda second evaporator configured to form second concentrated water by further evaporatively concentrating at least a portion of the first concentrated water that passed through the hot lime softener by second heat exchange with hot steam.2. The apparatus of claim 1 , wherein a temperature of the first concentrated water that is introduced into the hot lime softener is approximately 90° C. to 110° C.3. The apparatus of claim 1 , wherein the first ...

Method of Cleaning a Compact Wastewater Concentrator

A method of cleaning compact wastewater concentrator cleans accreted salts from inner surfaces of a compact wastewater concentrator having a demister including mist eliminators. The method of cleaning is simple and quick and eliminates a majority of accreted salts by re-dissolving the salts in relatively dilute process water. 1. A method of cleaning a compact wastewater concentrator having an evaporator assembly defining a mixing corridor including a mixing chamber arranged to receive wastewater and gas and an evaporator section connected with the mixing chamber arranged to mix the wastewater with the gas and evaporate liquids from the wastewater; a demister operatively connected with the evaporator section and arranged to receive the mixed wastewater and gas and to separate the gas and the evaporated liquids from solids and the wastewater; and a conduit arranged to transfer the wastewater separated in the demister to a liquid inlet opening into the mixing chamber , the method comprising:turning off a blower and an infeed pump of the concentrator;opening a thickener inlet valve to a thickening tank to allow fluid to flow from a sump of the demister to the thickening tank;closing a thickener return valve to prevent fluid from flowing from the thickening tank back to the sump;turning on a sump pump to pump liquid from the sump to the thickening tank;turning off the sump pump when the sump is empty;closing the thickener inlet valve to fluidly isolate the sump from the thickening tank;opening a service water valve of the concentrator;opening a sump make-up valve of the concentrator to allow fresh unconcentrated wastewater to flow into the sump through a make-up water line;closing the sump make-up valve when the sump is full of unconcentrated wastewater;starting a flare and a blower fan of the concentrator;operating the concentrator for a predetermined period of time;checking a saturation level of the wastewater in the sump;returning to the step of turning off the blower ...

PLASMA GAS WATER IONIZATION PURIFICATION SYSTEM

A plasma gas water ionization purification system that purifies waste water into clean water by removing inert waste solids from the waste water. The plasma gas water ionization purification system includes an ionization chamber and a plasma emitting device. The ionization chamber receives the waste water. The plasma emitting device is operatively connected to the ionization chamber and generates a stream of plasma to heat the waste water in the ionization chamber to generate purified steam from the waste water, thereby resulting in separation of the purified steam from the inert waste solids in the waste water, with the purified steam then being condensed into liquid form forming the clean water, which is collected for later use. 1. A plasma gas water ionization purification system for purifying waste water into clean water by removing inert waste solids from the waste water , comprising:a) an ionization chamber; andb) a plasma emitting device;wherein said ionization chamber is for receiving the waste water;wherein said plasma emitting device is operatively connected to said ionization chamber; andwherein said plasma emitting device is for generating a stream of plasma to heat the waste water in said ionization chamber to generate purified steam from the waste water, thereby resulting in separation of the purified steam from the inert waste solids in the waste water, with the purified steam then being condensed into liquid form forming the clean water, which is collected for later use.2. The plasma gas water ionization purification system of claim 1 , further comprising a collection chamber;wherein said collection chamber is in fluid communication with said ionization chamber;wherein said collection chamber is for condensing the purified steam into the clean water; andwherein said collection chamber is for collecting the clean water.3. The plasma gas water ionization purification system of claim 2 , further comprising a waste chamber;wherein said waste chamber is ...

System for Extending Turndown in A Gas-Liquid Separator

An apparatus for extending turndown in a gas-liquid separator is presented. The apparatus includes a first mist extractor with a first operating range and a second mist extractor with a second operating range. The mist extractors are generally of the same type, with the second operating range being different than the first operating range. A gas stream containing entrained liquid droplets flows through the first mist extractor and then through the second mist extractor. Each mist extractor coalesces and captures the liquid droplets within its own operating range, expanding the overall operating range of the separator. Additional mist extractors may be added to cover any gap between the first and second operating ranges.

LIQUID PURIFICATION METHODS AND APPARATUS

Liquid purification methods and apparatus are disclosed. An example apparatus includes a frame to define an interior space, the frame having an inner surface in contact with air of the interior space; a barrier positioned between a body of liquid and the interior space; and an absorber suspended from the frame to transfer liquid from the body of liquid into the interior space via an opening in the barrier. 1. An apparatus , comprising:a frame to define an interior space, the frame having an inner surface in contact with air of the interior space;a bather positioned between a body of liquid and the interior space; andan absorber suspended from the frame to transfer liquid from the body of liquid into the interior space via an opening in the barrier.2. The apparatus of claim 1 , wherein the barrier comprises insulation material.3. The apparatus of claim 1 , wherein the absorber comprises:a wicking section to be placed in the body of liquid; andan evaporation section to be placed in the interior space.4. The apparatus of claim 3 , wherein the absorber is to transfer the liquid from the wicking section to the evaporation section via capillary action.5. The apparatus of claim 1 , further comprising a controller to control movement of the absorber into the body of liquid in response to an indication that the absorber is to be cleaned.6. The apparatus of claim 1 , further comprising a reservoir to store condensation formed on the inner surface of the frame.7. The apparatus of claim 1 , further comprising a controller to convey a message to an extraction entity in response to an indication that a reservoir is to be emptied claim 1 , wherein the reservoir is to collect condensation from the inner surface.8. The apparatus of claim 1 , further comprising a flotation structure.9. A method claim 1 , comprising:positioning a first section of an absorber within an interior space of a structure, the interior space defined by a frame of the structure and a barrier positioned above a ...

A method for recovery of ethylene oxide

Ethylene oxide purification by quenching and washing ethylene oxide reactor effluent prior to passing the gaseous ethylene oxide-containing stream to an ethylene oxide absorber to form a dilute aqueous ethylene oxide and carbon dioxide solution and thereafter stripping that solution in an EO stripper to produce a gaseous ethylene oxide and carbon dioxide-containing overhead vapor which is then passed to a reabsorber wherein the ethylene oxide and part of the carbon dioxide vapors are absorbed to form an aqueous reabsorbate solution from which carbon dioxide is removed to produce an ethylene oxide-containing solution is improved by passing an impurities-containing liquid bleed stream obtained from the quench wash to a second, small quench bleed stripper where steam and carbon dioxide are added and gaseous overhead from that quench bleed stripper is passed to the reabsorber for recovery of the EO and removal of formaldehyde and other impurities.

MECHANICAL VAPOR RECOMPRESSION SYSTEM AND METHOD THEREOF

A mechanical vapor recompression system and method thereof. The system comprises: an evaporator (), a first cavity (), a first fluid collection area (), a second cavity () and a blowing type pump (), the evaporator () having a high temperature fluid reception channel () and a low temperature fluid reception channel (); the method comprises: enabling a first fluid to flow from a vapor source () to the high temperature fluid reception channel () of the evaporator (), enabling liquid water collected from a first fluid supply to flow to the low temperature reception channel (), and transferring heat of vaporous water in the high temperature reception channel () to the liquid water collected in the low temperature reception channel (); converting at least a part of the liquid water collected in the low temperature reception channel () to vaporous water, and returning the further heated vaporous water to the vapor source (). 1. A mechanical vapor recompression system , comprising:{'b': 20', '20', '20', '20', '20', '20', '20', '21', '20', '20', '21', '21', '21, 'i': a', 'b', 'c', 'd', 'a', 'c', 'a', 'b', 'd', 'b', 'a', 'b, 'an evaporator (), comprising a first inlet (), a second inlet (), a first outlet () and a second outlet (), the first inlet () and the first outlet () forming opposing ends of a high temperature fluid reception channel (), the second inlet () and the second outlet () forming opposing ends of a low temperature fluid reception channel (), and no opening communicating the high temperature fluid reception channel () and the low temperature fluid reception channel () existing between the two;'}{'b': 30', '30', '30', '20', '20', '20, 'i': a', 'a', 'c', 'c, 'a first cavity (), comprising a gap space and having an inlet () leading to the gap space, and the inlet () being in fluid communication with the first outlet () in the fluid reception direction of the first outlet () of the evaporator ();'}{'b': 31', '30', '30', '30', '31', '31', '31', '31', '31', '20', ' ...

METHOD AND APPARATUS FOR ISOLATION OF POTENTIALLY HARMFUL MATERIAL

A method and an apparatus for isolating potentially harmful medical substances, such as antibiotics, is disclosed. An aqueous composition, such as blackwater, contains potentially harmful medical substances present in dissolved state in bodily waste. The aqueous composition is temporarily stored in a buffer tank and is then transferred in batches to a vaporization unit comprising one or more vaporization chambers for producing a water-reduced waste material containing said potentially harmful medical substances. The waste material is subjected to a destructive treatment, such as a high-temperature incineration process. 1. A method for isolating potentially harmful medical substances , such as antibiotics , present in dissolved state in bodily waste , said method comprising:{'b': '22', 'in at least one buffer tank (), receiving an aqueous composition containing potentially harmful medical substances present in dissolved state in bodily waste;'}{'b': '22', 'temporarily storing the aqueous composition in the buffer tank ();'}{'b': 22', '24', '26', '28, 'transferring the aqueous composition in batches from the buffer tank () to a vaporization unit () comprising one or more vaporization chambers (, );'}{'b': 26', '28, 'in said one or more vaporization chambers (, ), vaporizing water from the aqueous composition for producing a water-reduced waste material containing said potentially harmful medical substances;'}{'b': 59', '79, 'passing the vaporized water through one or more protective structures (, ), such as one or more demisters, arranged to prevent aerosols or droplets to pass through;'}{'b': '24', 'transferring the waste material from the vaporization unit (); and'}subjecting the waste material to a destructive treatment, such as a high-temperature incineration process.224. The method as claimed in claim 1 , wherein claim 1 , the water content of the aqueous composition is reduced in the vaporization unit () by 30-95% claim 1 , preferably 50-95% and most preferably ...

VACUUM DEVOLATILIZER

Provided is a vacuum devolatilizer for use in a polymer manufacturing or processing plant. The devolatilizer comprises a vacuum chamber having an inlet for a polymer melt, an outlet for a polymer melt, a vacuum port through which volatiles may be removed and a stirrer shaft port for the entry of a stirrer shaft. The stirrer shaft passes through the at least one stirrer shaft port and extends into the vacuum chamber and carries an agitation means. The stirrer shaft seal is associated with each stirrer shaft port for sealing against the stirrer shaft and each stirrer shaft seal has an external portion outside the vacuum chamber. The devolatilizer is provided with a motor located outside of the vacuum chamber for rotating shaft and comprises means for blanketing the external portion of the stirrer shaft seal with a low oxygen content gas or vapor, e.g., nitrogen, helium, steam, or carbon dioxide. 125.-. (canceled)26. A vacuum devolatilizer for polymer manufacturing or processing , the devolatilizer comprising:a vacuum chamber having an inlet, an outlet, at least one vacuum port, and at least one stirrer shaft port configured to accept a stirrer shaft;a stirrer shaft passing through the at least one stirrer shaft port and extending into the vacuum chamber, the stirrer shaft includes an agitator;a stirrer shaft seal associated with each stirrer shaft port for sealing against the stirrer shaft, each stirrer shaft seal having an external portion outside of the vacuum chamber;at least one motor located outside the vacuum chamber for rotating the shaft; andan enclosure for blanketing the external portion of at least one stirrer shaft seal with a low oxygen content gas or vapor.27. The devolatilizer of claim 26 , wherein the agitator comprises one or more paddles.28. The devolatilizer of claim 26 , wherein the vacuum chamber includes two stirrer shaft ports claim 26 , and the stirrer shaft extends through each of those two stirrer shaft ports.29. The devolatilizer of claim 26 ...

Liquid de-entrainment in heat exchange equipment

A kettle reboiler includes a shell, a liquid reservoir defined within the shell to contain a first process fluid, and a tube bundle positioned within the liquid reservoir and at least partially submergible in the first process fluid, the tube bundle being configured to circulate a second process fluid that causes the first process fluid to boil and discharge a vapor-liquid mixture. A liquid-vapor separation assembly is positioned in the shell and includes a separation deck, and a plurality of separation devices mounted to the separation deck, each separation device being operable to de-entrain liquid from the vapor-liquid mixture and discharge a vapor. A vapor outlet nozzle is coupled to the shell to receive the vapor discharged from the plurality of separation devices.

WASTEWATER CONCENTRATION SYSTEM

A wastewater concentrator system is portable and scalable to effectively process up to forty thousand gallons of wastewater per day and more. The system has a portable assembly including a liquid evaporator assembly, gas-liquid separator, and exhaust assembly carried by a skid, which can be carried as a single unit on a mobile platform. The liquid evaporator assembly includes wastewater injection nozzles arranged to minimize buildup of material inside a mixing chamber. The gas-liquid separator has top access doors for installing and removing demister panels through a top wall and a sump adapted to provide scalability of the system to larger processing capacities while maintaining the portability. The system is adapted for connection to a plurality of heated gas sources and includes a control system designed to maintain a selected operating condition regardless of variations in the amount of heated gases supplied. 1. A portable wastewater concentrator assembly comprising: a liquid evaporator assembly,', 'a gas-liquid separator connected with the liquid evaporator assembly,', 'an exhaust assembly having a fan connected with the gas-liquid separator, and', 'a power plant assembly connected with the exhaust assembly and arranged to drive the fan;, 'a wastewater concentrator including'}a skid, wherein the wastewater concentrator is attached to and carried by the skid; anda mobile hauling platform;wherein the skid is removably carried by the mobile hauling platform, whereby the wastewater concentrator may be hauled as a single unit on the mobile hauling platform for transportation on roads and to remote operating locations.2. The portable wastewater concentrator assembly of claim 1 , wherein the skid further comprises a support frame disposed below the liquid evaporator assembly claim 1 , gas-liquid separator claim 1 , exhaust assembly claim 1 , and power plant assembly claim 1 , wherein the wastewater concentrator may be removed from the mobile hauling platform as a ...

LIQUID CONCENTRATOR

A liquid concentrator having an evaporator assembly and a cyclonic separator includes features designed to improve the performance of the liquid concentrator. A settling chamber is separated from a sump of the cyclonic separator. A liquid inlet opening into a mixing chamber of the evaporator injects wastewater at low pressures. Features to aid in the cleaning of the liquid concentrator include easy open doors and clean water injection ports for cleaning interior portions of the liquid concentrator. 112-. (canceled)13. A liquid concentrator comprising:an evaporator assembly defining a mixing corridor having a mixing chamber arranged to receive wastewater and gas and an evaporator section connected with the mixing chamber arranged to mix the wastewater with the gas and evaporate liquids from the wastewater;a cyclonic separator operatively connected with the evaporator section and arranged to receive the mixed wastewater and gas and to separate the gas and the evaporated liquids from solids and the wastewater; anda conduit arranged to transfer the wastewater separated in the cyclonic separator to a liquid inlet opening into the mixing chamber, wherein the liquid inlet comprises a low-pressure injection port, wherein the low-pressure injection port injects wastewater at a pressure of about ten psig or less.14. The liquid concentrator of claim 13 , wherein the low-pressure injection port injects the wastewater at a pressure of about five psig or less.15. The liquid concentrator of claim 14 , wherein the low-pressure injection port injects the wastewater at a pressure of about two psig.16. The liquid concentrator of claim 13 , wherein the low-pressure injection port includes a spray nozzle.17. The liquid concentrator of claim 13 , wherein the low-pressure injection port does not have a spray nozzle.18. The liquid concentrator of claim 17 , comprising a baffle arranged to deflect wastewater entering the mixing chamber through the low-pressure injection port.19. A liquid ...

SYSTEM AND METHOD FOR WATER PURIFICATION

An apparatus for use in water purification including a cylindrical vessel comprising, within the cylindrical vessel, a first set of hydrocyclones, at least one intermediate set of hydrocyclones, and a final set of hydrocyclones, the sets of hydrocyclones arranged in series. In one embodiment, the hydrocyclones within each set of hydrocyclones are arranged in a parallel configuration, wherein each set of hydrocyclones is defined by a divider which causes the hydrocyclones in each set to operate in parallel. In one embodiment each hydrocyclone has a tangential inlet disposed within an inlet chamber of the cylindrical vessel and in fluid communication with an inlet connected to the inlet chamber, an overflow disposed within an overflow chamber of the cylindrical vessel, and an underflow disposed within an underflow chamber of the cylindrical vessel. In one embodiment, the cylindrical vessel comprises a first set of hydrocyclones and a second, final set of hydrocyclones. 1. An apparatus for use in water purification comprising:a cylindrical vessel comprising, within the cylindrical vessel, a first set of hydrocyclones, at least one intermediate set of hydrocyclones, and a final set of hydrocyclones, the sets of hydrocyclones arranged in series, wherein the hydrocyclones within each set of hydrocyclones are arranged in a parallel configuration, wherein each set of hydrocyclones is defined by a divider which causes the hydrocyclones in each set to operate in parallel,and wherein each hydrocyclone hasa tangential inlet disposed within an inlet chamber of the cylindrical vessel and in fluid communication with an inlet connected to the inlet chamber,an overflow disposed within an overflow chamber of the cylindrical vessel, andan underflow disposed within an underflow chamber of the cylindrical vessel.2. The apparatus as recited in wherein the cylindrical vessel is disposed within a high temperature water tank having a first water inlet claim 1 , a second water inlet claim 1 ...

METHOD FOR WATER PURIFICATION

A method for water purification utilizing a cylindrical vessel containing a hydrocyclone nest. The heated contaminated water is fed into the nest, which includes a first set of hydrocyclones, at least one intermediate set of hydrocyclones, and a final set of hydrocyclones, the hydrocyclones in each set arranged in parallel, and each set arranged in series. The heated contaminated water is pumped into the cylindrical vessel such that the heated contaminated water enters a tangential inlet of each of the hydrocyclones, the hydrocyclones separate the heated contaminated water into steam and solids/concentrate, the steam exits through an overflow of the hydrocyclones and a first outlet of the cylindrical vessel, the solids/concentrate exit through an underflow of the hydrocyclones and into the subsequent ser of hydrocyclones until the final set of hydrocyclones, and then out through a second outlet of the cylindrical vessel. The steam is condensed into purified water. 1. A method for purifying a contaminated water comprising the steps of:heating the contaminated water within a high temperature water tank to a specified temperature, wherein the heated contaminated water heats a cylindrical vessel disposed within the high temperature water tank and, disposed within the cylindrical vessel, a first set of hydrocyclones, at least one intermediate set of hydrocyclones, and a final set of hydrocyclones, the sets of hydrocyclones arranged in series, wherein the hydrocyclones within each set of hydrocyclones are arranged in a parallel configuration, wherein each set of hydrocyclones is defined by a divider which causes the hydrocyclones in each set to operate in parallel;pumping the heated contaminated water into an inlet of the cylindrical vessel such that the heated contaminated water enters tangential inlets of each hydrocyclone within each set of the hydrocyclones in series, the hydrocyclones separate the heated contaminated water into a steam and a concentrate, the steam ...

METHOD OF ACCELERATING EVAPORATION OF WATER AND DEVICE FOR ITS IMPLEMENTATION

The invention relates to a method and device for accelerating the evaporation of liquids, in particular water, using solar energy. The device is made of a polymer material with a density of 0.8-0.95 g/cmand contains a flat base, on the upper and lower surfaces of which there are ribs to ensure that the surface of the base is immersed under the surface of water, while the ratio the mass of the upper, lower ribs and base is 1:1:1. The efficiency of water evaporation is increased due to solar energy absorption into the thin surface layer of water having a thickness from 1 to 10 mm. The method uses the fact that the thin surface layer of water is isolated while the device under the surface of water. As the surface layer evaporates the device is steadily positioned at a given depth below the water surface. 1. A method of accelerating an evaporation of water , wherein a surface layer of water is isolated by placing a device for accelerating the evaporation of water under the surface layer of water , while a heat absorbed by a base of the device is transferred to the surface water layer to stimulate evaporation , and as the surface water layer evaporates , the device is stably placed at a predetermined level below a surface of the water , wherein the base of the device has ribs on an upper and a lower surfaces; the base being made of a polymer material with a density of 0.8-0.95 g/cm , wherein a mass ratio of the upper , the lower ribs and the base is 1:1:1.2. The method according to claim 1 , wherein the surface layer of water has a thickness of 1-10 mm.3. A device for accelerating evaporation of water claim 1 , comprising:{'sup': '3', 'a flat base, having ribs on an upper and a lower surfaces, the base being made of a polymer material with a density of 0.8-0.95 g/cm, wherein a mass ratio of the upper, the lower ribs and the base is 1:1:1.'}4. The device according to claim 3 , wherein the base has a developed texture.5. The device according to claim 4 , wherein the ...

A PLATE HEAT EXCHANGER, A HEAT EXCHANGING PLATE AND A METHOD OF TREATING A FEED SUCH AS SEA WATER

The present invention relates to a plate heat exchanger for treatment of a feed. The plate heat exchanger includes a plate package comprising a plurality of heat exchanging plates and defining a heating volume, a cooling volume and a plurality of process volumes. Each of the process volumes includes an evaporation section for evaporation of a part of the feed, a separation section for separating a non-evaporated part from an evaporated part of the feed, and a condensation section being arranged to condense the evaporated part of the feed. Each heat exchanging plate defines a first thermal interface between the heating volume and the evaporation section of a first process volume, a second thermal interface between the cooling volume and the condensation section of a second process volume, and at least one further thermal interface between an evaporation section and a condensation section of two adjacent process volumes. 1. A plate heat exchanger for treatment of a feed such as sea water , the plate heat exchanger including a plate package comprising a plurality of heat exchanging plates arranged in a successive order , the plate package defines a heating volume for receiving a heating medium , a cooling volume for receiving a cooling medium and a plurality of process volumes , each of the volumes being fluidly separated from each other in the plate package , each of the process volumes includes:an evaporation section being arranged to permit evaporation of at least a part of the feed,a separation section being arranged to separate a non-evaporated part of the feed from an evaporated part of the feed, anda condensation section being arranged to condense the evaporated part of the feed,wherein each heat exchanging plate defines a first thermal interface between the heating volume and the evaporation section of a first process volume of the plurality of process volumes, a second thermal interface between the cooling volume and the condensation section of a second ...

Salt Removal And Transport System And Method For Use In A Mono Ethylene Glycol Reclamation Process

A system for removing salt from a process stream being fed into a flash separator introduces a swirling motive fluid into the fluid column of the separator. The swirling motive fluid comes into contact with salt components residing in the fluid of the column to create a salt slurry. Means to limit the upward movement of the swirling motive fluid can be provided. The salt slurry is then removed and can be sent to a brine generation vessel. Saturated brine from the vessel is transported back to the fluid column to replace the motive fluid in the column. 1. A system for removing salt from a rich MEG stream being fed into a flash separator , the system comprising:a solids fluidization device located at a bottom end of a fluid column of the flash separator and arranged to introduce a swirling motive fluid within the fluid columna salt removal device located above the solids fluidization device and arranged to remove a salt slurry created by the swirling motive fluid.2. A system according to further comprising means for limiting an upward movement of the swirling motive fluid in the fluid column.3. A system according to wherein the means for limiting the upward movement is a valve located between a top and a bottom end of the fluid column.4. A system according to wherein the solids fluidization device includes a plurality of spaced-apart vertical slots arranged tangential to claim 1 , surrounding claim 1 , and in communication with a central inner bore of the solids fluidization device.5. A system according to further comprising a brine generation vessel arranged to receive the salt slurry from the fluid column.6. A system according to further comprising means for transporting a saturated brine from the brine generation vessel into the fluid column.7. A system according to wherein a source of the swirling motive fluid is at least one of a produced water stream and a condensate water stream.8. A method of fluidizing salts to aid their removal claim 1 , the method ...

Apparatus For Concentrating Wastewater And For Creating Brines

A liquid concentrator system includes a concentrator section having a gas inlet, a gas outlet, and a mixing corridor disposed between the gas inlet and the gas outlet. A liquid inlet is disposed in the mixing corridor between the gas inlet and a narrowed portion. A demister is disposed downstream of the concentrator section. The demister includes a liquid collector to remove liquid from gas flowing through the demister, and a reservoir that collects the removed liquid. A re-circulating circuit is disposed between reservoir and the mixing corridor to transport liquid within the reservoir to the mixing corridor, and a secondary re-circulating circuit includes a settling tank to separate saturated liquid and suspended solids. A custom brine mixing device is operatively coupled to the settling tank. 1. A liquid concentrator system , comprising: a gas inlet,', 'a gas outlet,', 'a mixing corridor disposed between the gas inlet and the gas outlet, the mixing corridor having a narrowed portion in which gas flow within the mixing corridor accelerates when traveling from the gas inlet to the gas outlet; and', 'a liquid inlet through which liquid to be concentrated is injected into the mixing corridor, the liquid inlet disposed in the mixing corridor between the gas inlet and the narrowed portion;, 'a concentrator section including;'} a demister gas flow passage coupled to the gas outlet of the concentrator section,', 'a liquid collector disposed in the demister gas flow passage to remove liquid from gas flowing in the demister gas flow passage, and', 'a reservoir that collects the liquid removed from the gas flowing in the demister gas flow passage by the liquid collector;, 'a demister disposed downstream of the concentrator section, the demister including;'}a re-circulating circuit disposed between reservoir and the mixing corridor to transport liquid within the reservoir to the mixing corridor;a secondary re-circulating circuit including a settling tank to separate ...

VAPOR TRAP

A method of capturing a vaporized component or components, and apparatus for same is provided. The method involves vaporization of desired components, and capture of the vaporized components in a material using a vapor trap device. Once captured, the material with the component stored therein may be used for any number of purposes including ingestion, topical administration, and/or aromatization. 1. A device for capturing volatile components from plant material comprising:a vaporizer, a quantity of plant material loaded into the vaporizer; a reservoir containing a quantity of vapor trapping media, a vapor inlet providing an inlet path to the reservoir, and a vapor outlet providing an outlet path from the reservoir, the vapor inlet and vapor outlet being on opposite sides of the vapor trap, the reservoir being between the vapor inlet and vapor outlet;', 'a first container positioned just downstream of the vapor inlet, the first container configured to allow a vapor inlet flow and prevent escape of the vapor trapping media through the vapor inlet;', 'a second container positioned just upstream of the vapor outlet, configured to allow a vapor outlet flow and to prevent escape of the vapor trapping media through the vapor outlet;, 'a vapor trap attached to the vaporizer, the vapor trap comprisingwherein the vaporizer is configured to heat a quantity of air and pass the heated air past the plant material within the vaporizer, the heated air configured to vaporize a volatile component of the plant material forming a vapor flow, the vaporizer configured to allow the vapor flow to pass into the vapor inlet of the vapor trap, into the vapor trap reservoir and through and in contact with the vapor trapping media, and exiting the vapor trap from the vapor outlet;wherein the vapor trapping media is configured to capture a portion of the volatile component of the vapor flow by at least one of condensation, absorption, and adsorption of the volatile component.2. The device for ...

SYSTEM FOR DESALINATING SALTWATER

A system for separating salt and/or minerals from ocean, sea, brackish, or brine water collected in a water enclosure. The water enclosure is heated with solar radiation to increase a rate of evaporation of the saline water and produce humidity or moisture within the water enclosure for conversion to desalinated water. Due to condensation, water collects as droplets on cold surfaces of cooling coils when the humidity or moisture comes in contact with the cold surfaces of the cooling coils. The water droplets, which are desalinated, are gathered by condensation capture pans. Output lines channel the collected desalinated water out of the pans for consumption and/or storage. Re-saturation units increase a rate of condensation within the water enclosure, thereby, increasing a collection of the desalinated water. 1. A system comprising: a suction filter with a screen enclosure configured to prevent water source debris or sediment from being drawn into the water supply line;', 'a pump being configured to be operable to draw saline water from the at least one or more water sources, and', 'a particle filter being configured to filter particles or minerals out of the saline water traveling through the water supply line;, 'a water supply line, said water supply line being configured to siphon saline water from at least one or more water sources, the water supply comprises;'}a water enclosure being configured to receive the saline water from the water supply line, the water enclosure being further configured to be operable for desalination of the saline water, wherein the water enclosure is configured to be heated by solar radiation to at least increase a rate of evaporation of the saline water to produce humidity or moisture within the water enclosure for collection;a cooling coil having an outer surface being configured to at least accumulate liquid or water droplets when the humidity or moisture within the water enclosure comes in contact with the outer surface of the ...

High Pressure Separator Cleaning Methods and Apparatus

A process and system for cleaning a high pressure separator vessel in a polymerization reactor without removing the top cover and its associated bolts by providing a cleaning hole in a fluid fitting above and adjacent to the top cover, through which a cord or cable is fed and affixed to a rotatable cleaning nozzle. The cleaning nozzle is gradually raised, lowered and rotated to direct a high pressure liquid onto the interior walls of the vessel to remove accumulated waste material. 1. A process for cleaning a high pressure separator vessel in a polymerization reactor , comprising:opening an outlet at a bottom of the high pressure separator vessel;removing a flush plug from a fluid fitting above and adjacent to a top cover of the high pressure separator vessel, thus, exposing a cleaning hole in the fluid fitting;feeding a cord or cable through the cleaning hole into an interior of the high pressure separator vessel and down to the outlet;affixing a rotatable cleaning nozzle to the cord or cable at the outlet;supplying a pressurized liquid to the cleaning nozzle; andgradually raising and/or lowering and rotating the cleaning nozzle through the inside of the high pressure separator vessel from the bottom to a top thereof,such that the pressurized liquid is directed into contact with an inner wall of the high pressure separator vessel and removes accumulated waste material.2. The process according to claim 1 , further comprising threading a cleaning hose connection nut having a central aperture into the cleaning hole to protect threads in the cleaning hole.3. The process according to claim 1 , further comprising gradually lowering and rotating the cleaning nozzle from the top to the bottom of the interior of the high pressure separator while the pressurized liquid is supplied to the cleaning nozzle and directed into contact with the inner wall of the high pressure separator vessel.4. The process according to claim 1 , wherein the top cover of the high pressure separator ...

METHOD, APPARATUS AND SYSTEM FOR CONCENTRATING SOLUTIONS USING EVAPORATION

A system, apparatus and method for concentrating a solution. The system includes a humidification device and a solution flow path for flow of a solution to be concentrated to the humidification device. The humidification device includes humidification media to facilitate evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution. The method includes flowing a solution to be concentrated along a flow path to a humidification device including humidification media, flowing a gas through the humidification media, and flowing the solution to be concentrated through the humidification media. There is evaporation of liquid from the solution to the gas as the solution passes through the humidification media thereby concentrating the solution and producing a humidified gas. The solution to be concentrated may be salt water and the gas may be air. 1. A system for concentrating a solution comprising:a humidification device comprising humidification media;a solution flow path for flow of a solution to be concentrated to the humidification device, the humidification media facilitating evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution; and a cleaning solution container for cleaning solution; and', 'a closable outlet flow path fluidly connecting the cleaning solution container with the solution flow path, for controllable flow of cleaning solution from the cleaning solution container through at least part of the solution flow path., 'a cleaning circuit comprising2. The system of claim 1 , wherein the outlet flow path is closable by a one way valve.3. The system of claim 1 , wherein the cleaning circuit further comprises a closable return flow path fluidly connecting the solution flow path with the cleaning solution container for return flow ...

METHOD AND COMPOSITION FOR PULSE DOSE CLEANING OF PROCESS STREAMS

Pulse dosing is used to administer a cleaning formulation into a fluid process stream flowing through structural components of a processing facility. The fluid process stream may contain corn, corn-derived products, or a combination thereof, or the fluid process stream may contain a process condensate, a rinse fluid, a cleaning fluid or any combination thereof. The processing facility may be an ethanol processing plant, a protein processing plant, a corn oil processing plant, an ethanol and corn oil processing plant, an ethanol and protein processing plant, or an ethanol, corn oil and protein processing plant. Pulse dosing may include administering the cleaning formulation into the fluid process stream for a period of x seconds every y minutes, with no administration of the cleaning formulation between the periods of x seconds. 1. A method , comprising using pulse dosing to administer a cleaning formulation into a fluid process stream flowing through structural components of a processing facility , the fluid process stream comprising (i) corn , corn-derived products , or a combination thereof , or (ii) a process condensate , a rinse fluid , a cleaning fluid , or any combination thereof.2. The method of claim 1 , wherein pulse dosing comprises administering the cleaning formulation into the fluid process stream for a period of x seconds every y minutes claim 1 , with no administration of the cleaning formulation between the periods of x seconds claim 1 , wherein x and y independently are from 1 to 500.3. The method of claim 2 , wherein x and y independently are from 15 to 90.4. The method of claim 2 , wherein x=y.5. The method of claim 1 , wherein an amount of the cleaning formulation is administered into the fluid process stream to provide a concentration of 10 ppm to 50 claim 1 ,000 ppm of the cleaning formulation in the fluid process stream during the period of x seconds.6. The method of claim 1 , wherein the processing facility is an ethanol processing plant ...

FLUID EVAPORATOR FOR AN OPEN FLUID RESERVOIR

A reservoir evaporation system for evaporating fluid from an open reservoir of effluent containing a contaminant includes a fluid evaporator, an air pump, and an air supply conduit functionally connecting the fluid evaporator with the air pump. The fluid evaporator includes a vessel adapted to be positioned in an operative position partially submerged on the top surface of the effluent in the reservoir with a lower chamber submerged in the effluent and an upper chamber extending above the top surface of the effluent. In operation, air from the air pump mixes with the effluent inside the fluid evaporator and subsequently is discharged through exhaust openings. A fluid discharge pipe can also simultaneously discharge aerated effluent back down into the reservoir. Fluid is thereby separated from the effluent in the lower chamber by evaporation in a controlled manner that minimizes spread of contaminants to surrounding environments by wind. 133-. (canceled)34. A reservoir evaporation system for evaporating fluid from an open reservoir of effluent containing a fluid and a contaminant , the system comprising:a fluid evaporator comprising a vessel with an upper chamber and a lower chamber, the vessel adapted to float in an operative position partially submerged on the top surface of the effluent in the reservoir with the lower chamber submerged in the effluent and the upper chamber extending above a top surface of the effluent, a first opening into a lower portion of the lower chamber to allow the effluent to enter the chamber, and an exhaust opening into the upper chamber disposed to be above the top surface of the effluent and in communication with the lower chamber;an air pump; andan air supply conduit functionally connecting the fluid evaporator with the air pump, the air supply conduit having an outlet arranged to discharge forced air into the lower portion of the chamber;wherein when the fluid evaporator is in the operative position, air from the air pump can be ...

Salt Removal And Transport System And Method For Use In A Mono Ethylene Glycol Reclamation Process

Systems and methods for removing solids from a process stream being fed into a flash separator include a solids fluidization device and a solids removal device. The solids fluidization device at the bottom end of the fluid column of the flash separator introduces a swirling motive fluid within the fluid column, while the solids removal device located above the solids fluidization device removes the slurry created by the swirling motive fluid. Systems and methods for fluidizing solids in the fluid column of a flash separator include a solids fluidization device that introduces a swirling motive fluid within the fluid column, means to limit the upward movement of the swirling motive fluid, such as a valve, and removing the solid slurry produced by the swirling motive fluid. 1. A system for removing solids from a process stream being fed into a flash separator , the system comprising:a solids fluidization device located at a bottom end of a fluid column of the flash separator and arranged to introduce a swirling motive fluid within the fluid column; anda solids removal device located above the solids fluidization device and arranged to remove a slurry created by the swirling motive fluid.2. A system according to further comprising means for limiting an upward movement of the swirling motive fluid in the fluid column.3. A system according to wherein the means for limiting the upward movement of the swirling motive fluid in the fluid column is a valve located between a top end and a bottom end of the fluid column.4. A system according to wherein the solids fluidization device includes a plurality of spaced-apart vertical slots arranged tangential to claim 1 , surrounding claim 1 , and in communication with a central inner bore of the solids fluidization device.5. A system according to further comprising a brine generation vessel arranged to receive the slurry from the fluid column.6. A system according to further comprising means for transporting a saturated brine from ...

Concentrated Wastewater Slurry Thickening and Storage System and Stabilization Batch Treatment Plant

A wastewater concentrator a liquid evaporator assembly, a gas-liquid separator, an exhaust assembly, and a slurry thickening and storage system. The slurry thickening and storage system includes a slurry thickening tank fluidly connected to the gas-liquid separator and a thickened slurry storage tank fluidly connected to the slurry thickening tank. 139-. (canceled)40. A batch treatment and stabilization plant for treating and stabilizing slurry formed from concentrating a wastewater stream , the batch treatment and stabilization plant comprising:a central batch processing plant, the central batch processing plant including a slurry inlet, a slurry outlet, an additive, and a stabilizer.41. The batch treatment and stabilization plant of claim 40 , further comprising sulfate as one additive.42. The batch treatment and stabilization plant of claim 40 , further comprising Portland cement as one stabilizer.43. The batch treatment and stabilization plant of claim 40 , further comprising a plurality of slurry storage tanks that are operatively connected to the central batch processing plant.44. The batch treatment and stabilization plant of claim 43 , wherein each slurry storage tank in the plurality of storage tanks is fluidly connected to a wastewater concentrator.45. The batch treatment and stabilization plant of claim 44 , wherein at least one of the concentrators is operatively connected to a source of produced water from a natural gas well.46. The batch treatment and stabilization plant of claim 40 , further comprising a plurality of storage containers for storing slurry after being mixed with an additive or a stabilizer in the central batch plant. Field of the DisclosureThe present disclosure generally relates to systems and apparatuses for concentrating wastewater by separating and removing a water constituent from the wastewater and more specifically to wastewater concentrators having a concentrated slurry thickening and storage system and/or a stabilization batch ...

VAPOR TRAP

A method of capturing a vaporized component or components, and apparatus for same is provided. The method involves vaporization of desired components, and capture of the vaporized components in a material using a vapor trap device. Once captured, the material with the component stored therein may be used for any number of purposes including ingestion, topical administration, and/or aromatization. 1. A device for capturing volatile components from plant material comprising:a vaporizer, a quantity of plant material loaded into the vaporizer; a reservoir, a vapor inlet, and a vapor outlet, the vapor inlet and vapor outlet being on opposite sides of the vapor trap, the reservoir being in between the vapor inlet and vapor outlet, the reservoir being in communication with both the vapor inlet and the vapor outlet;', 'a quantity of vapor trapping media positioned in the reservoir;', 'a first container positioned just downstream of the vapor inlet, configured to allow a vapor flow into the reservoir and prevent escape of the vapor trapping media through the vapor inlet;', 'an outlet adapter of the vaporizer being attached to the vapor inlet;, 'a vapor trap removably attached to the vaporizer, the vapor trap comprisingwherein the vaporizer is configured to heat a quantity of air and pass the heated air past the plant material within the vaporizer, the heated air configured to vaporize a volatile component of the plant material forming a vapor flow, the vaporizer configured to allow the vapor flow to pass into the vapor inlet of the vapor trap, into the vapor trap reservoir and through and in contact with the vapor trapping media, and exiting the vapor trap from the vapor outlet;wherein the vapor trapping media is configured to capture a portion of the volatile component of the vapor flow by at least one of condensation, absorption, and adsorption of the volatile component; anda chiller connected to the vapor trap reservoir, the chiller configured to decrease a temperature of ...

Apparatus for Concentrating Wastewater and for Creating Brines

A liquid concentrator system includes a concentrator section having a gas inlet, a gas outlet, and a mixing corridor disposed between the gas inlet and the gas outlet. A liquid inlet is disposed in the mixing corridor between the gas inlet and a narrowed portion. A demister is disposed downstream of the concentrator section. The demister includes a liquid collector to remove liquid from gas flowing through the demister, and a reservoir that collects the removed liquid. A re-circulating circuit is disposed between reservoir and the mixing corridor to transport liquid within the reservoir to the mixing corridor, and a secondary re-circulating circuit includes a settling tank to separate saturated liquid and suspended solids. A custom brine mixing device is operatively coupled to the settling tank. 1. A liquid concentrator system , comprising:a concentrator section including;a gas inlet,a gas outlet,a mixing corridor disposed between the gas inlet and the gas outlet;a liquid inlet through which liquid to be concentrated is injected into the mixing corridor;a demister disposed downstream of the concentrator section, the demister including a demister gas flow passage coupled to the gas outlet of the concentrator section, a liquid collector disposed in the demister gas flow passage to remove liquid from gas flowing in the demister gas flow passage, and a reservoir that collects the liquid removed from the gas flowing in the demister gas flow passage by the liquid collector;a re-circulating circuit disposed between reservoir and the mixing corridor to transport liquid within the reservoir to the mixing corridor;a settling tank to separate saturated liquid and suspended solids; anda custom brine mixing device operatively coupled to the settling tank.2. The liquid concentrator system of claim 1 , wherein the custom brine mixing device includes a saturated liquid extraction port claim 1 , a saturated liquid valve operatively coupled to the saturated liquid extraction port ...

EVAPORATOR

The invention relates to an evaporator comprising an evaporator body () surrounded by an evaporator housing (), wherein the evaporator housing () is provided with a feed line () for feeding a liquid into the evaporator housing () and with an outlet () for emitting any vapour produced, 1. An evaporator comprising an evaporator body surrounded by an evaporator housing , wherein the evaporator housing is provided with a feed line for feeding a liquid into the evaporator housing and with an outlet for emitting any vapour produced ,wherein the evaporator body comprises a multiplicity of plates which are arranged in a planar manner one above another, wherein at least one void is formed in each case between adjacent plates, wherein each of the voids is fluidically connected to the outlet,wherein a liquid distributor is interconnected between the feed line and the evaporator body, wherein the liquid distributor branches off from the feed line in the direction of the evaporator body in at least two distributor lines (VR), andwherein each distributor line (VR) is connected to at least one void,wherein a cross-sectional area of the feed line corresponds substantially to the sum of the cross-sectional areas of the distributor lines (VR).2. The evaporator according to claim 1 , wherein a pressure loss between an end claim 1 , facing the evaporator body claim 1 , of the feed line and an end claim 1 , facing the evaporator body claim 1 , of each distributor line (VR) is substantially the same.3. The evaporator according to claim 1 , wherein the distributor lines (VR) are substantially the same length and have the same cross section.4. The evaporator according to claim 1 , wherein a pre-distributor structure is connected between the feed line and the distributor lines (VR) claim 1 , the feed line splitting up in a tree-like manner into a multiplicity of feed end lines in said pre-distributor structure claim 1 , wherein each of the feed end lines is divided into at least two ...

LIQUID PURIFICATION METHODS AND APPARATUS

Liquid purification methods and apparatus are disclosed. An example apparatus includes a frame to define an interior space, the frame having an inner surface in contact with air of the interior space; a barrier positioned between a body of liquid and the interior space; and an absorber suspended from the frame to transfer liquid from the body of liquid into the interior space via an opening in the barrier. 1. A method , comprising:positioning a first section of an absorber within an interior space of a structure, the interior space defined by a frame of the structure and a barrier positioned above a body of liquid, the structure to float on the body of liquid;positioning a second section of the absorber in the body of liquid below the barrier to transfer liquid of the body of liquid to the first section of the absorber via capillary action; andcollecting, in a reservoir, condensation formed on the frame from evaporation of the liquid.2. The method of claim 1 , further including temporarily submerging of the first section of the absorber into the body of liquid.3. The method of claim 2 , further including determining whether the absorber is scheduled for a cleaning claim 2 , wherein the temporarily submerging of the first section of the absorber is in response to determining that the absorber is scheduled for the cleaning.4. The method of claim 2 , further including determining whether an amount of sediment accumulation on the first section of the absorber is greater than a threshold claim 2 , and wherein the temporarily submerging of the first section of the absorber into the body of liquid is in response to determining that the sediment accumulation is greater than the threshold.5. The method of claim 1 , further including sending a message to an extraction entity to initiate extraction of the liquid from the reservoir.6. The method of claim 5 , further including determining a water level in the reservoir claim 5 , and wherein the sending of the message to the ...

Liquid Separator And Concentrator

A liquid separator and concentrator is disclosed. An example liquid separator and concentrator includes a separator column. A spray chamber has a sprayer nozzle to spray an influent within the spray chamber and create a falling film in the separator column. A heating jacket surrounds the separator column, wherein the heating jacket heats the falling film to evaporate at least one portion of the falling film and leaves a concentrate. A concentrate collection vessel receives the concentrate from the separator column. 1. A liquid separator and concentrator system , comprising:a separator column;a spray chamber having a sprayer nozzle to spray an influent within the spray chamber and create a falling film in the separator column;a heating jacket surrounding the separator column, wherein the heating jacket heats the falling film to evaporate at least one portion and leave a concentrate; anda concentrate collection vessel to receive the concentrate from the separator column.2. The system of claim 1 , further comprising a first condenser column to cool the evaporated portion.3. The system of claim 2 , further comprising a first evaporate collection vessel to collect condensate.4. The system of claim 3 , further comprising a second condenser column connected to the first condenser column through the first evaporate collection vessel to further cool a remaining evaporated portion.5. The system of claim 4 , wherein the second condenser column feeds back to the first evaporate collection vessel.6. The system of claim 5 , further comprising a second evaporate collection vessel to collect condensate from the first evaporate collection vessel.7. The system of claim 6 , further comprising a vacuum to draw vapor through the first condenser.8. The system of claim 7 , wherein the vacuum is connected to the second condenser.9. The system of claim 7 , further comprising a valve connected between the first condenser and the second condenser.10. The system of claim 1 , further comprising ...

An evaporator and a method for vaporizing a substance in an evaporator

An evaporator ( 1 ) for vaporizing a substance into its gaseous form, which comprises a cylindrical outer shell ( 2 ) and a plate pack ( 4 ) arranged inside the cylindrical shell in its lower part and a droplet separator ( 9 ) arranged above the plate pack. A recirculation of a substance to be vaporized is carried out by using flow guides ( 10 a, 10 b ) arranged tightly between the plate pack and the outer shell and by an ejector pipe ( 13 ) arrangement comprising a collection pipe ( 11 ) arranged inside the outer shell.

Salt Water Desalination Assembly

A salt water desalination assembly includes a tank for containing salt water. The tank has an inverted cone therein that is positioned above the salt water thereby facilitating water vapor from the salt water to condense on the inverted cone. An input pipe extends into the tank to fill the tank with the salt water. A condensate pipe extends upwardly into the tank and the condensate pipe is aligned with the inverted cone to collect the condensed water vapor for subsequent use. A stand is vertically oriented and is positioned adjacent to the tank. A reflector is pivotally coupled to the stand and the reflector is exposed to sunlight. The reflector focuses the reflected sunlight onto the tank for heating the tank and thereby facilitate the salt water in the tank to be heated for producing the water vapor. 1. A salt water desalination assembly being configured to desalinate salt water with sun driven condensation , said assembly comprising:a tank for containing salt water, said tank having an inverted cone therein wherein said inverted cone is configured to be positioned above the salt water thereby facilitating water vapor from the salt water to condense on said inverted cone, said inverted cone being an inverted rectangular pyramid shape having four planar triangular faces, said tank being comprised of a thermally conductive material wherein said tank is configured to be in thermal communication with the salt water, said tank has a bottom wall, a top wall and an outer wall extending therebetween, said top wall sloping downwardly from said outer wall toward a center point of said tank such that said top wall defines said inverted cone, said inverted cone having a lower facing surface that faces an interior of said tank wherein said lower facing surface is configured to have the water vapor condense thereupon thereby facilitating the condensed water vapor to run downwardly along said lower facing surface toward a point of said inverted cone;an input pipe extending into ...

System for Energy Regeneration Using Mechanical Vapor Recompression in Combined Chemical Process

The present disclosure provides a system for energy recycling using mechanical vapor recompression in combined chemical process, the system including a heat exchange reactor for generating an intermediate material by means of an exothermic reaction and discharging the generated intermediate material, and heat-exchanging heat generated in the exothermic reaction with water supplied from outside so as to generate water vapor; an absorption tank for receiving the intermediate material, and mixing the intermediate material with water, so as to generate an intermediate material aqueous solution; a stripper for receiving the intermediate material aqueous solution, and separating the intermediate material into an intermediate material gas and an intermediate material water-rich aqueous solution; an endothermic reactor for receiving the intermediate material water-rich aqueous solution, and reacting the intermediate material with water, so as to generate a final product aqueous solution; an evaporation concentrator for receiving the final product aqueous solution, and heat-exchanging heat of the water vapor from the heat exchange reactor with the final product aqueous solution so as to generate steam; a dehydrating distillation tower for receiving, dehydrating, and purifying the final product aqueous solution discharged from the evaporation concentrator; and a mechanical vapor recompressor for compressing the steam from the evaporation concentrator, and providing the compressed steam as a source of heat or a source of steam supply. 1. A system for energy recycling using mechanical vapor recompression in combined chemical process , characterized in that the system comprises:{'b': '10', 'a heat exchange reactor () for generating an intermediate material by means of an exothermic reaction and discharging the generated intermediate material, and heat-exchanging heat generated in the exothermic reaction with water supplied from outside so as to generate water vapor;'}{'b': '20', ...

VAPOR-LIQUID CONTACTING APPARATUS AND PROCESS WITH CROSS CONTACTING

A high capacity and high efficiency co-current and cross-flow vapor-liquid contacting apparatus and process is useful in distillation columns and other vapor-liquid contacting processes. The apparatus is characterized by an arrangement of contacting modules and perforated receiving pans in horizontal stages. The modules define a co-current contacting volume and in an exemplary configuration the modules include a liquid distributor and a demister. Liquid dispensed from the modules on a perforated receiving pan are contacted with upflowing vapor through perforations therein. 1. An apparatus for performing co-current and cross-flow vapor-liquid contacting , comprising:a plurality of stages each having at least one contacting module and at least one receiving pan;said contacting module comprising a liquid distributor having an outlet proximate to a contacting volume and a demister having an inlet surface proximate to the contacting volume and an outlet surface superior to said receiving pan; andsaid receiving pan having a perforated base, said receiving pan inferior to said outlet surface of the demister.2. The apparatus of further comprising at least one duct in fluid communication with the receiving pan and with an inferior liquid distributor.3. The apparatus of wherein the duct is separate from the liquid distributor and said duct having an upper end in fluid communication with the receiving pan claim 2 , and a lower end claim 2 , wherein the lower end of each duct is in fluid communication with a separate inferior liquid distributor.4. The apparatus of further comprising a contacting volume between the demister and the liquid distributor and the liquid distributor has an outlet in fluid communication with the contacting volume and the inlet surface of the demister is in fluid communication with the contacting volume.5. The apparatus of wherein vapor enters the receiving pan through perforations in the base and liquid exits the receiving pan though the duct.6. The ...

VAPOR-LIQUID CONTACTING APPARATUS AND PROCESS WITH OFFSET CONTACTING MODULES

A high capacity and high efficiency co-current and cross-flow vapor-liquid contacting apparatus and process is useful in distillation columns and other vapor-liquid contacting processes. The apparatus is characterized by an arrangement of offset contacting modules in horizontal stages. The modules define a co-current contacting volume and in an exemplary configuration the modules include a liquid distributor and a demister. Half modules comprise downcomers against the shell of the vessel for transporting liquid to the subjacent stage. 1. An apparatus for performing vapor-liquid contacting , comprising:a plurality of stages having a contacting module;said contacting module comprising a liquid distributor having an outlet proximate to a contacting volume and a demister having an inlet surface proximate to the contacting volume; andcontacting modules on adjacent stages being horizontally offset.2. The apparatus of further comprising a deck in each stage and said deck inferior to an outlet surface of said demister.3. The apparatus of further comprising a half module which shares a wall with the shell of the vessel.4. The apparatus of wherein said deck is perforated.5. The apparatus of further comprising a full contacting module comprising liquid distributor between two demisters.6. The apparatus of further comprising a receiving deck inferior to said demisters and a half module inferior to said receiving deck.7. The apparatus of further comprising a transport deck inferior to said half module and a contact module inferior to said transport deck.8. The apparatus of wherein said half module comprises a downcomer comprising an outlet in said downcomer proximate to a contacting volume claim 7 , a demister having an inlet surface proximate to the contacting volume and an outlet surface superior to said transport deck.9. The apparatus of wherein said contacting modules in every other stage are vertically aligned.10. The apparatus of further comprising a weir adjacent to the ...

VAPOR-LIQUID CONTACTING APPARATUS AND PROCESS WITH DOWNCOMER AT SHELL

A high capacity and high efficiency vapor-liquid contacting apparatus and process is useful in distillation columns and other vapor-liquid contacting processes. The apparatus is characterized by a half module comprising a downcomer against a shell of a vessel for transporting liquid to a subjacent stage which utilizes a demister to effect vapor-liquid separation at the downcomer outlet. 1. An apparatus for performing vapor-liquid contacting , comprising:a vessel comprising a shell;a first contact module comprising a downcomer, said downcomer is adjacent to a shell of the vessel and comprises an outlet proximate to a contacting volume; anda demister having an inlet surface proximate to the contacting volume.2. The apparatus of further comprising a transport deck inferior to an outlet of said demister.3. The apparatus of wherein said downcomer shares a wall with the shell.4. The apparatus of wherein a wall of said downcomer has an edge that is in contact with said shell.5. The apparatus of wherein said wall is curved.6. The apparatus of wherein said wall is sloped.7. The apparatus of wherein said deck is perforated.8. The apparatus of wherein said downcomer is between said shell and said demister.9. The apparatus of wherein said downcomer is inferior to a receiving deck.10. The apparatus of wherein said receiving deck is perforated.11. The apparatus of wherein said receiving deck is imperforate adjacent said downcomer.12. The apparatus of further comprising a weir adjacent to the downcomer extending above a base of the receiving deck for holding up liquid on the receiving deck.13. The apparatus of further comprising a full contact module inferior to said transport deck claim 1 , said contact module comprising a liquid distributor between two demisters.14. The apparatus of wherein said first contact module and said full contact module are offset from each other.15. The apparatus of further comprising at least one of:a processor;a memory storing computer-executable ...

Water purification device

The disclosure provides systems methods and apparatus for purifying water. A purification device includes a heating vessel adapted to receive impure water and output water or water vapor. The device further includes at least one heating element arranged outside and in thermal contact with the heating vessel, configured to provide heat to the impure water. The device also includes at least one heat exchanger to exchange heat between the impure water and the water vapor to raise the temperature of the impure water. In some example implementations, the at least one heating element can include a Peltier cell.

Method to remove solids in contaminated water

The world suffers from a refugee crisis. There are millions of people homeless and displaced by war, poverty, terrorism and the world economy. Hunger and thirst are rampant. Millions of people live in refugee camps. I knew that I could not help the hunger problem except by donations to charities. So, I thought about the lack of water problem. Millions of people live by the sea and ocean. People have access to salt water. People have been removing salt from the sea and ocean from hundreds of years, if not more, by evaporation. The solution to provide people with salt free water was to collect salt water, sea water or ocean water in a container. Evaporate the salt water and in the evaporation process, transfer the purer water, (salt(NaCl) free) to another container. I developed a method to accomplish this task. A process to transfer salt(NaCl) water or contaminated water to another container, purer than before. During this process of providing salt(NaCl) free water to people, I realized that this method not only works for salt removal but also works for feces removal and other contaminated water, such as dirty water from rivers, canals, swamps, streams, lakes, etc. 1. A method to remove solids in contaminated water to purer water by using two containers, an energy source, evaporation, a vapor/water passage, the force of gravity, a truncated cone and a pressure plate. This method is works by transferring the purer water to another container and leaving the solid in the contaminated container. Originally, This was thought to remove salt(NaCl) from saltwater or ocean water. This method, not only works for salt(NaCl) removal, but other solids, such as feces removal, dirt removal, sand removal, etc. My patent is a way to transfer contaminated water salt(NaCl) water) to purer water by using two containers, an energy source, evaporation, a vapor/water passage, a truncated cone and a pressure plate.Obtain two containers. Container A is filled with salt(NaCl) water, i.e., sea ...

Apparatus for Concentrating Wastewater and for Creating Brines

A liquid concentrator system includes a concentrator section having a gas inlet, a gas outlet, and a mixing corridor disposed between the gas inlet and the gas outlet. A liquid inlet is disposed in the mixing corridor between the gas inlet and a narrowed portion. A demister is disposed downstream of the concentrator section. The demister includes a liquid collector to remove liquid from gas flowing through the demister, and a reservoir that collects the removed liquid. A re-circulating circuit is disposed between reservoir and the mixing corridor to transport liquid within the reservoir to the mixing corridor, and a secondary re-circulating circuit includes a settling tank to separate saturated liquid and suspended solids. A custom brine mixing device is operatively coupled to the settling tank. 2. The liquid concentrator system of claim 1 , wherein the custom brine mixing device includes a saturated liquid extraction port claim 1 , a saturated liquid valve operatively coupled to the saturated liquid extraction port claim 1 , a settled solids extraction port claim 1 , a settled solids valve operatively coupled to the settled solids extraction port claim 1 , and a controller operatively coupled to the saturated liquid valve and to the settled solids valve.3. The liquid concentrator system of claim 2 , wherein the custom brine mixing device includes a source of lubricant that is fluidly connected to a mixture line downstream of a point at which the saturated liquids and settled solids are mixed.4. The liquid concentrator system of claim 3 , wherein the controller is operatively coupled to a mixture weight sensor claim 3 , to a saturated liquid weight sensor claim 3 , and to a settled solids weight sensor.5. The liquid concentrator system of claim 1 , wherein the concentrator section includes an adjustable flow restriction disposed in the narrowed portion of the mixing corridor claim 1 , the flow restriction adjustable to alter gas flow through the mixing corridor.6. ...

EVAPORATOR AND BAFFLE THEREOF

An evaporator and a baffle structure thereof are disclosed by the present application. The baffle structure is configured to block liquid droplets in a gas, and includes: a bottom portion extending in a first direction and side portions extending from the bottom portion in a direction intersecting the first direction; and a liquid blocking region provided on the side portions, the liquid blocking region being provided therein with a plurality of holes penetrating the side portions to allow gas to pass through the holes. 1. A baffle structure configured to block liquid droplets in a gas , comprising:{'b': 22', '24', '26, 'a body () comprising a bottom portion () extending in a first direction and side portions () extending from the bottom portion in a direction intersecting the first direction; and'}{'b': 42', '441, 'a liquid blocking region () provided on the side portions, the liquid blocking region being provided therein with a plurality of holes () penetrating the side portions to allow gas to pass through the holes.'}23234. The baffle structure according to claim 1 , wherein the bottom portion has opposite first end portion () and second end portion () in the first direction claim 1 , and the liquid blocking region is further provided at at least one of the first end portion and the second end portion.3. The baffle structure according to claim 2 , wherein the liquid blocking region is provided throughout the side portions and/or the first end portion and the second end portion.4. The baffle structure according to claim 1 , wherein the body has a substantially U-shaped cross-sectional shape.5. The baffle structure according to claim 4 , wherein an angle between the side portion and the bottom portion is 90° or greater than 90° claim 4 , and the bottom portion is planar or the bottom portion is configured into a funnel shape.6. The baffle structure according to claim 1 , wherein the holes in the liquid blocking region have a shape of circle claim 1 , triangle ...

IMPROVEMENTS IN METHODS OF DISTILLATION

In an improved method of distilling fluids, some or all of the fluid is recovered as distillate and the fluid is situated in the shell side of a first shell and tube heat exchanger. The fluid to be recovered as distillate is successively boiled, demisted, compressed and then introduced into upper ends of the tubes. A second shell and tube heat exchanger is located below the first heat exchanger, and distillate from upper ends of the tubes in the second heat exchanger are arranged to receive distillate liquid and/or vapor from the lower ends of tubes of the first heat exchanger. The fluid is located in the shell of the second heat exchanger and that fluid is heated but is not boiled. A mechanism is provided to supply at least some of the heated fluid to the shell of the first heat exchanger.

Salt Removal and Transport System and Method For Use In A Mono Ethylene Glycol Reclamation Process

A system for removing salt from a rich mono ethylene glycol (MEG) stream being fed into a flash separator isolates the fluid residing in the brine column of the separator from the MEG and introduces a swirling motive fluid into the column. The swirling motive fluid comes into contact with salt components residing in the isolated fluid of the column to create a salt slurry. The salt slurry is then removed and sent to a brine generation vessel. Saturated brine from the vessel is transported back to the column to replace the motive fluid in the column. 1. A system for removing salt from a rich MEG stream being fed into a flash separator , the system comprising:means for isolating a fluid residing in a brine column of the flash separator from MEG residing toward an upper end of the flash separator;means for introducing a swirling motive fluid into the isolated fluid; andmeans for removing a salt slurry created by the swirling motive fluid2. A system according to wherein the isolating means is an on-off valve located between a top and a bottom end of the brine column of the flash separator.3. A system according to wherein the introducing means is a solids fluidization device having a plurality of spaced-apart vertical slots arranged tangential to claim 1 , surrounding claim 1 , and in communication with a central inner bore of the device.4. A system according to wherein the removal means is a slurry discharge head located in the brine column and directly above the introducing means.5. A system according to further comprising a brine generation vessel arranged to receive the salt slurry from the brine column.6. A system according to further comprising means for transporting a saturated brine from the brine generation vessel into the brine column.7. A system according to wherein a source of the swirling motive fluid is at least one of a produced water stream and a condensate water stream.8. A method of removing salt from a rich MEG stream claim 1 , the method comprising ...

Energy efficient water purification and desalination

A desalination system that can comprise an inlet, an optional preheating stage, multiple evaporation chambers and optional demisters, product condensers, a waste outlet, one or more product outlets, a nested configuration that facilitates heat transfer and recovery and a control system. The control system can permit operation of the purification system continuously with minimal user intervention or cleaning. The desalination system can operate with any number of pre-treatment methods for descaling, and with degassing systems to eliminate or reduce hydrocarbons and dissolved gases. The system is capable of removing, from a contaminated water sample, a plurality of contaminant types including microbiological contaminants, radiological contaminants, metals, and salts.

HEAT TRANSFER TUBE AND METHOD FOR MANUFACTURING A HEAT TRANSFER TUBE

The invention relates to a heat transfer tube () for falling film evaporation having a heating medium surface () to be heated by a heating medium, a falling film surface () to have spent liquor passing over it, and being made from an iron based high alloy stainless steel material with an alloy content above 16.00% for Chromium and above 1% for Nickel. The falling film surface of the heat transfer tube is equipped with at least one weld ridge (WR; WR, WR), said weld ridge having a height (h; h) in the range 0.3 to 5.0 mm, a width (w; w) in the range 0.5-15 mm, and an inclination angle (α; α, α) versus a plane orthogonal to a longitudinal axis (CC) of the heat transfer tube in a range of 0-70 degrees so that each weld ridge is inclined and extends helically along at least a portion of the heat transfer tube or extend within a plane orthogonal to the longitudinal axis of the heat transfer tube and forms well ridge portions on the falling film surface such that the distance along the longitudinal axis of the heat transfer tube between adjacent weld ridge portions is within the range of 0 to 250 mm. The invention also relates to a method for manufacturing said heat transfer tube. 199. A heat transfer tube () for falling film evaporation of spent liquor , the heat transfer tube () having:{'b': '21', 'a heating medium surface () arranged to be heated by a heating medium; and'}{'b': 20', '21', '20, 'claim-text': {'b': 20', '9', '9, 'sub': 1', '2', '1', '2', '2', '1', '2', '2', '1', '2', '1', '2, 'the falling film surface () of the heat transfer tube () is equipped with one or several welds forming a multitude of weld ridges (WR; WR, WR) spaced apart along the longitudinal axis (CC) of the heat transfer tube such that the distance along the longitudinal axis of the heat transfer tube between adjacent weld ridges is within the range of 0-250 mm; said weld ridges (WR; WR, WR) having a height (h; h) in the range of 0.3-5.0 mm; said weld ridges (WR; WR, WR) having a width (w; w) ...

HARMFUL SUBSTANCE REMOVAL SYSTEM AND METHOD

A harmful substance removal system and method include a direct contact liquid concentrator having a gas inlet, a gas outlet, a mixing chamber disposed between the gas inlet and the gas outlet, and a liquid inlet for importing liquid into the mixing chamber. Gas and liquid mixing in the are mixed chamber and a portion of the liquid is vaporized. A demister is disposed downstream of the mixing chamber. The demister includes at least one stage of mist elimination having a first filter that removes particles greater than 9 microns. A fan is coupled to the demister to assist gas flow through the mixing chamber. 1. A harmful substance removal system , comprising:a direct contact liquid concentrator including a gas inlet, a gas outlet, a mixing chamber disposed between the gas inlet and the gas outlet, and a liquid inlet for importing liquid into the mixing chamber, gas and liquid mixing in the mixing chamber to vaporize a portion of the liquid;a demister disposed downstream of the mixing chamber, the demister including at least one stage of mist elimination comprising a first filter that removes particles greater than 9 microns; anda fan coupled to the demister to assist gas flow through the mixing chamber.2. The harmful substance removal system of claim 1 , wherein the filter is located downstream of the fan.3. The harmful substance removal system of claim 1 , further comprising a second filter in the demister claim 1 , the second filter removing particles greater than 15 microns claim 1 , the second filter being located upstream of the first filter.4. The harmful substance removal system of claim 1 , further comprising a third filter in the demister claim 1 , the third filter being a coarse filter claim 1 , the third filter being located upstream of the second filter.5. The harmful substance removal system of claim 1 , wherein the first filter removes particles greater than 5 microns and preferably greater than 1 micron.6. (canceled)7. (canceled)8. The harmful substance ...

Liquid purifying/distillation device

Multi-phase separation system

A multi-phase separation system utilized to remove contaminants from fluids includes a pre-filtering module for filtering a contaminated fluid to provide a filtered contaminated fluid. A condenser module receives the filtered contaminated fluid and a contaminated gas phase for condensing the contaminated gas phase to a contaminated liquid. A phase reaction chamber converts the filtered contaminated fluid to a contaminated mist wherein the mist is subjected to a low energy, high vacuum environment for providing a first change of phase by separating into a contaminated gas phase and a liquid mist phase. The contaminated gas phase is carried out of the phase reaction chamber by a carrier air. A vacuum pump provides the low energy, high vacuum environment in the phase reaction chamber and delivers the contaminated gas phase to the condenser module for condensation providing a second change of phase.

Multi-phase separation system

A multi-phase separation system utilized to remove contaminants from fluids includes a pre-filtering module for filtering a contaminated fluid to provide a filtered contaminated fluid. A condenser module receives the filtered contaminated fluid and a contaminated gas phase for condensing the contaminated gas phase to a contaminated liquid. A phase reaction chamber converts the filtered contaminated fluid to a contaminated mist wherein the mist is subjected to a low energy, high vacuum environment for providing a first change of phase by separating into a contaminated gas phase and a liquid mist phase. The contaminated gas phase is carried out of the phase reaction chamber by a carrier air. A vacuum pump provides the low energy, high vacuum environment in the phase reaction chamber and delivers the contaminated gas phase to the condenser module for condensation providing a second change of phase.

Multi-phase separation system

A multiphase separation system utilized to remove contaminants from fluids includes a pre-filtering module for filtering a contaminated fluid to provide a filtered contaminated fluid. A condenser module receives the filtered contaminated fluid and a contaminated gas phase for condensing the contaminated gas phase to a contaminated liquid. A phase reaction chamber converts the filtered contaminated fluid to a contaminated mist wherein the mist is subjected to a low energy, high vacuum environment for providing a first change of phase by separating into a contaminated gas phase and a liquid mist phase. The contaminated gas phase is carried out of the phase reaction chamber by a carrier air. A vacuum pump provides the low energy, high vacuum environment in the phase reaction chamber and delivers the contaminated gas phase to the condenser module for condensation providing a second change of phase.

Multi-phase separation method

A multiphase separation system utilized to remove contaminants from fluids includes a pre-filtering module for filtering a contaminated fluid to provide a filtered contaminated fluid. A condenser module receives the filtered contaminated fluid and a contaminated gas phase for condensing the contaminated gas phase to a contaminated liquid. A phase reaction chamber converts the filtered contaminated fluid to a contaminated mist wherein the mist is subjected to a low energy, high vacuum environment for providing a first change of phase by separating into a contaminated gas phase and a liquid mist phase. The contaminated gas phase is carried out of the phase reaction chamber by a carrier air. A vacuum pump provides the low energy, high vacuum environment in the phase reaction chamber and delivers the contaminated gas phase to the condenser module for condensation providing a second change of phase.

Система многофазного разделения

1. Система разделения для удаления загрязнений из жидкости, содержащая:камеру фазовой реакции;распределительную головку и ряд атомизирующих распылительных сопел для преобразования отфильтрованной загрязненной жидкости в загрязненный туман;вакуумный насос, создающий в упомянутой камере фазовой реакции низко энергетическую сильно разреженную среду;причем упомянутая низко энергетическая сильно разреженная среда обеспечивает изменение фазы путем разделения упомянутого загрязненного тумана на загрязненный газ и на фазу жидкостного тумана.2. Система разделения по п. 1, содержащая непрерывный источник воздуха-носителя для транспортировки упомянутого загрязненного газа из упомянутой камеры фазовой реакции.3. Система разделения по п. 1, далее содержащая бак пониженного давления выхода жидкости, соединенный с упомянутой камерой фазовой реакции для сбора упомянутого жидкостного тумана.4. Система разделения по п. 1, в которой упомянутая камера фазовой реакции сообщается с упомянутым баком пониженного давления выхода жидкости через трехходовой управляющий вентиль.5. Система разделения по п. 1, в которой упомянутый трехходовой управляющий клапан приводится в действие переключателем высокого уровня и плавающим переключателем низкого уровня, помещенными внутри упомянутого бака пониженного давления выхода жидкости.6. Система разделения по п. 1, далее содержащая модуль предварительной фильтрации, принимающий и фильтрующий загрязненную жидкость и создающий упомянутую отфильтрованную загрязненную жидкость.7. Система разделения для удаления загрязнения из жидкости, содержащая:камеру фазовой реакции;средство дл� РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2006 103 675 A (51) МПК B01D 5/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2006103675/15, 09.07.2004 (71) Заявитель(и): Ликвид Сепарейшн Технолоджиз энд Эквипмэнт, ЛЛС (US) Приоритет(ы): (30) Конвенционный приоритет: 12.07.2003 US 10/619.071 (85) Дата начала рассмотрения ...

一种赤泥提碱用碱液多级高效浓缩系统

一种涉及赤泥无害化处理技术领域的赤泥提碱用碱液多级高效浓缩系统，包含一级蒸发器、二级蒸发器、预热换热器、缓冲分离器、汽水分离器、蒸气压缩机和电加热炉；原碱液经过预热换热器和缓冲分离器预热后，进入一级蒸发器和二级蒸发器加热蒸发浓缩，加热产生的蒸汽经过蒸气压缩机压缩升温后，进入一级蒸发器、二级蒸发器和预热换热器换热；该浓缩系统结构简单便于操作维护，能够提高浓缩效果和效率，减少带出浓碱蒸汽，降低噪音。

Sistema e processo de destilaçao e purificaçao

一种可扩展的节能蒸发器

本专利提供一种有较大的产能扩展能力、兼容性强、可以去除原液中的内毒素、节能降耗的可扩展的节能蒸发器。其从下到上依次包括缓存室、主蒸发部件、升膜蒸发部件、挡板分离器、重力分离室；缓存室侧壁上开有原液入口，缓存室底部开有废液出口；主蒸发部件包括主蒸发室、毛细管，毛细管上、下端分别与升膜蒸发部件、缓存室相通；升膜蒸发部件包括升膜蒸发室、穿过升膜蒸发室的升膜管，升膜蒸发室侧壁上下部分别连接有与升膜蒸发室相通的二次蒸汽入管、二次出水管，升膜管上、下端分别与挡板分离器、毛细管上端相通；挡板分离器内部具有弯折的气体流道；重力分离室的上端出口通过蒸汽回收管与二次蒸汽入管相通。

一种闪蒸耦合旋流汽液分离装置及其余热回收工艺

本公开涉及一种闪蒸耦合旋流汽液分离装置及其余热回收工艺，属于余热回收领域，该系统包括括同轴线、且竖直设置的内部芯管和外部直筒体，内部芯管的长度小于外部直筒体的长度，外部直筒体的底部连接锥斗，内部芯管和外部直筒体之间形成环形通道；环形通道的顶部封闭，且顶部设有倾斜的通道管，通道管的轴线与外部直筒体的轴线之间设有夹角，且为锐角，通道管的内部设有雾化器，内部芯管的顶部通过管路与冷凝换热器相连通，所述冷凝换热器内设有换热管。

증발기

본 발명은 공급되는 액상 제품을 필름화하는 동시에 이를 가열하여 증발시킴으로써 액상 제품을 정제 또는 농축하기 위한 증발기의 제품 공급부에 관한 것이다. 그 구성은; 하우징(1); 상기 하우징(1) 상부에 횡으로 고정 설치되는 상부플레이트(7); 상단이 상기 상부플레이트(7)를 수직으로 관통하도록 직립되게 설치되는 다수의 증발튜브(9)를 포함하는 증발기에 있어서; 상기 각각의 증발튜브(9)의 상단에는; 튜브결합부(23), 걸림대(25) 및 액분배부(27)로 구성되는 어댑터본체(19)와; 상기 어댑터본체(19)에 결합되며 원통형의 채움공간(S4)을 마련하는 어댑터커버(21)로 구성되는 관체로 된 어댑터(17)가 결합되는 것을 특징으로 한다.

用于工艺流的蒸发系统

本发明涉及一种用于工艺流的蒸发系统。用于从工艺流移除重有机杂质的工艺和系统包括提供具有水和大约0.5至大约1.5重量百分数的重有机杂质的工艺流。该工艺包括在具有一个或更多个蒸发级的蒸发器系统中将水与重有机杂质分离以提供含水冷凝物和液体残余物。含水冷凝物具有大约0.1重量百分数或更少的重有机杂质而液体残余物具有大约3至大约10重量百分数的重有机杂质。

[UNK]

Co-current contacting separation tray design and methods for using same

공급류를 증류하거나 분류하기 위한 분리 컬럼(2)에 사용하는 트레이 구조가 제공된다. 트레이(6)상에 복수의 병류 증기 및 액체 접촉 섹션(16)이 위치한다. 또한 트레이상에 증기류로부터 연행된 액체를 분리하기 위한 복수의 탈연행 장치(8)가 위치하며, 탈연행 장치는 내부 측면(25) 및 외부(27) 측면이 있고, 내부 측면(25)은 병류 접촉 섹션에 인접해 있다. 트레이 구조는 추가로상부와 하부가 있는 복수의 액체 하강관(14)을 합체하고 있으며, 상부는 제일 트레이의 탈연행 장치의 외부 측면(27)으로부터 액체를 수용할 수 있고, 하부는 제이 트레이의 병류 접촉 섹션내에 위치한다. A tray structure for use in the separation column 2 for distilling or fractionating the feed stream is provided. A plurality of cocurrent vapor and liquid contact sections 16 is located on the tray 6. Also on the tray is a plurality of decarburizing devices 8 for separating entrained liquid from the vapor stream, the decarburizing device having an inner side 25 and an outer 27 side, and the inner side 25 being Adjacent to the cocurrent contact section. The tray structure further incorporates a plurality of liquid downcomers 14 having an upper portion and a lower portion, the upper portion of which can receive liquid from the outer side 27 of the de-drawing unit of the first tray, and the lower portion of the J-tray. Located in the cocurrent contact section.

Method and device for cleaning contaminated and used oil

본 발명은 오염되고 사용된 오일을 세정하기 위한 방법 및 디바이스에 관한 것으로, 여기서 시작 재료는 기상으로 가열되며, 그리고 결과적인 증기는 정류되고, 정제된 오일은 정류 컬럼의 배수구로부터 응축물로서 제거된다. 본 발명에 의해 해결되는 문제는, 오염되고 사용된 오일을 정제하기 위한 방법 및 디바이스를 제공하는 것이며, 이 방법은, 심지어 시스템들 중 가장 작은 시스템에서 효과적인 작동을 가능하게 하여, 밀집한 시스템 구성 및 이에 따른 특히 컨테이너 구조에 의한 이동 사용이 가능하게 된다. 본 발명은 또한, 정비를 위해 요구되는 비용을 감소시키는 문제를 해결한다. 본 발명에 따른 문제는, 사용된 오일이 적어도 간접적으로 용융 배스와 접촉하게 시작 재료를 배치함으로써 증발 프로세스를 겪음으로 해결된다.

Evaporators and Methods for Evaporating Materials in Evaporators

가스 형태로 물질을 증발시키기 위한 증발기(1)는 원통형 외부 쉘(2) 및 원통형 쉘 내부에, 원통형 쉘의 하부에 배치된 플레이트 팩(4) 및 플레이트 팩 위에 배열된 액적 분리기(9)를 포함한다. 증발될 물질의 재순환은 플레이트 팩과 외부 쉘 사이에 단단히 배열된 유동 가이드(10a, 10b) 및 외부 쉘 내부에 배열된 수집 파이프(11)를 포함하는 배출기 파이프(13) 배열에 의해 수행된다.

Three phase vapor distributor

질량 및/또는 열 전달 탑은 탑의 내주 둘레에 증기 스트림을 분배하는 다상 증기 분배기를 구비한다. The mass and / or heat transfer tower has a poly-phase vapor distributor that distributes the vapor stream around the inner circumference of the tower. 다상 증기 분배기, 탑, 섬프, 챔버, 증기 유입 노즐, 천장, 연통, 바닥 Multipurpose steam distributor, tower, sump, chamber, vapor inflow nozzle, ceiling, communication, floor

High efficiency vaporizer and separating method for aldehyde and catalyst using the same

본 발명은 고효율 기화기 및 이를 이용한 알데히드 및 촉매의 분리방법에 관한 것으로, 본 발명에 따른 기화기는 복수의 유량 조절 플레이트 및 열 교환 튜브와 1:1로 매칭되는 가스관에 의하여 액상 및 기상 혼합물을 열 교환 튜브에 균일하게 주입하고, 이에 따라 기화기의 열전달 효율이 향상된다. 올레핀의 하이드로포밀화 공정에 이러한 기화기를 이용하여 알데히드 및 촉매 혼합 용액을 분리하는 경우 촉매의 활성을 저하시키지 않고, 전이금속 및 리간드의 분해를 방지할 수 있어 하이드로포밀화 반응의 효율이 향상된다. The present invention relates to a high-efficiency vaporizer and a method for separating aldehyde and catalyst using the same, wherein the vaporizer according to the present invention heat exchanges a liquid and gaseous mixture by a gas pipe that is matched 1: 1 with a plurality of flow control plates and a heat exchange tube. Evenly injected into the tube, thereby improving the heat transfer efficiency of the vaporizer. When the aldehyde and the catalyst mixed solution are separated by using such a vaporizer in the hydroformylation process of the olefin, the decomposition of transition metals and ligands can be prevented without lowering the activity of the catalyst, thereby improving the efficiency of the hydroformylation reaction. 하이드로포밀화, 올레핀, 합성가스, 알데히드, 촉매, 유량 조절 플레이트, 가스관, 기화기(vaporizer). Hydroformylation, olefins, syngas, aldehydes, catalysts, flow control plates, gas lines, vaporizers.

EVAPORATION UNIT FOR TECHNOLOGICAL FLOW

РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2017 114 572 A (51) МПК B01D 1/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2017114572, 01.09.2015 (71) Заявитель(и): ИНЕОС ЮРОП АГ (CH) Приоритет(ы): (30) Конвенционный приоритет: 29.09.2014 CN 201410511193.7 31 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 02.05.2017 US 2015/047907 (01.09.2015) (87) Публикация заявки PCT: A WO 2016/053551 (07.04.2016) Адрес для переписки: 119019, Москва, Гоголевский б-р, 11, этаж 3, "Гоулинг ВЛГ (Интернэшнл) Инк.", Лыу Татьяна Нгоковна R U (57) Формула изобретения 1. Способ удаления тяжелых органических примесей из технологического потока, причем способ содержит: подачу технологического потока, который содержит воду и тяжелые органические примеси; и разделение воды и тяжелых органических примесей в испарительной установке, содержащей одну или более ступеней испарения, для получения водного конденсата и жидкого остатка; причем водный конденсат содержит около 0,1 масс. % или менее тяжелых органических примесей, а жидкий остаток содержит от около 3 до около 10 масс. % тяжелых органических примесей. 2. Способ по п. 1, в котором технологический поток содержит от около 0,5 до около 1,5 масс. % тяжелых органических примесей. 3. Способ по п. 1, в котором тяжелые органические примеси включают полимерные материалы, полученные в процессе реакции аммоксидирования. 4. Способ по п. 1, в котором испарительная установка содержит от 1 до около 6 ступеней испарения. 5. Способ по п. 1, в котором испарительная установка содержит от 2 до около 6 ступеней испарения. Стр.: 1 A 2 0 1 7 1 1 4 5 7 2 (54) ИСПАРИТЕЛЬНАЯ УСТАНОВКА ДЛЯ ТЕХНОЛОГИЧЕСКОГО ПОТОКА 2 0 1 7 1 1 4 5 7 2 (86) Заявка PCT: R U (43) Дата публикации заявки: 09.11.2018 Бюл. № (72) Автор(ы): МАКДОНЕЛ Тимоти Роберт (US), КОУЧ Джей Роберт (US), ВАГНЕР Дэвид Рудольф (US), ВАЧТЕНДОРФ Пол Тригг (US) A 2 0 1 7 1 1 4 5 7 2 A R U 2 0 1 7 1 1 4 5 7 2 Стр.: 2 R U 6. Способ по п. 1, ...

Method and device for sea water desalination

FIELD: methods and devices for sea water desalination. SUBSTANCE: method of sea water desalination includes evaporation of sea water and condensation inside the primary circuit, and evaporation and condensation of the secondary medium, preferably, in form of raw water inside secondary circuit closed to itself and having compressor and separated from the primary circuit. Sea water is evaporated due to heating of preliminarily heated by secondary medium at high pressure and condensation of sea water steam in the secondary circuit, and steam of sea water passes through cyclone. General flow of sea water supplied to the primary circuit is separated into the first flow and second flow, approximately equal to volume to the first flow. The first flow is heated in the primary circuit to temperature close to boiling one by hot distilled water coming out of the primary circuit and flowing through the first heat exchanger. The second flow is heated to temperature close to boiling one by flow of withdrawn slime passing through the second heat exchanger. Concentration coefficient expressing relation of total amount of sea water supplied for time unit to amount of slime withdrawn for time unit is selected within 1 to 2. Offered method is applicable in plants for thermal desalination of sea water for production of sterile high quality distillate with simultaneous provision of low concentration of sediment in evaporated water and economical power consumption. EFFECT: higher efficiency. 5 cl, 3 dwg с999гс ПЧ сэ (19) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ ВИ “” 2455 625' (51) МПК? 13) С2 В Ото 3/00, С 02 Е 1/04 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 97103216/12, 04.09.1995 (24) Дата начала действия патента: 04.09.1995 (30) Приоритет: 05.09.1994 ОЕ Р 4431546.5 (46) Дата публикации: 10.09.2000 (56) Ссылки: ЕК 2337693 АЛ, 05.08.1977. ЕР 0142251 А2, 22.05.1985. 5Ц 1130360 А, 23.12.1984. (85) Дата перевода заявки РСТ на национальную фазу: 27 ...

A kind of climbing film evaporator for traditional Chinese drug inspissation system

本发明公开了一种用于中药浓缩系统的升膜蒸发器，涉及蒸发设备技术领域，该用于中药浓缩系统的升膜蒸发器，包括加热室和分离室，加热室的下表面中部固定连接预热管的一端，预热管的另一端固定连接预热器的一侧，预热器的另一侧固定连接有循环泵，预热管的另一端上表面固定安装有进料斗，加热室的下表面固定连接三脚架的顶部，三脚架的底部固定连接有底板，加热室的上表面中部固定安装有驱动电机。该用于中药浓缩系统的升膜蒸发器，通过预热器和预热管能够使低温物料加热至接近沸点，从而有效降低了加热室的负荷，通过循环泵将分离室分离后的蒸汽进行回收利用，起到了节约能源的作用，通过三脚架和底板对加热室起到支撑的作用。

Wasted water treatment system anf construction method thereof

본 발명은 냉각수단을 개선한 폐수처리 시스템 및 이의 시공 방법에 관한 것이다. 이러한 본 발명은, 폐수를 공급하는 폐수공급부, 그리고 공급된 폐수에 포함된 물을 증발시켜 수증기와 농축액을 생성하는 증발농축부, 그리고 수증기를 냉각시키는 냉매를 구비한 라디에이터를 포함하는 열교환부, 그리고 농축액을 저장하는 농축액 저장부를 포함한다. The present invention relates to a wastewater treatment system with improved cooling means and a method for constructing the same. The present invention provides a wastewater supply unit for supplying wastewater, an evaporative concentration unit for evaporating water contained in the supplied wastewater to generate water vapor and a concentrated solution, and a heat exchange unit including a radiator having a refrigerant for cooling the water vapor, and and a concentrate storage unit for storing the concentrate.

High-performance concrete retarder preparation system and preparation method

本发明涉及一种高性能混凝土缓凝剂制备系统及制备方法，包括支撑腿、工作台、下落圆孔、制备筒、喷洒机构、干燥机构、筛分机构、限位机构和收集机构，本发明采用的喷洒机构是可拆卸式的，便于对其进行更换清洗，避免在喷洒缓凝剂液体时，液体中含有大块的固体将喷雾头堵塞时，导致的缓凝剂制备无法正常进行，从而提高了缓凝剂的制备效率，同时通过干燥机构对进行向上送热风，使得雾状缓凝剂停留在制备筒内的时间加长，从而有效的对雾状缓凝剂干燥制备，同时避免下落的雾状缓凝剂粘附到制备筒的内侧壁上造成堆积的现象。

Evaporator and baffle plate structure thereof

本申请公开了一种蒸发器及其挡板结构。所述挡板结构用于阻挡气体中的液滴，其包括：本体，所述本体包括沿第一方向延伸的底部和从所述底部在交叉于所述第一方向的方向上延伸出的侧部；以及挡液区域，所述挡液区域设置于所述侧部上并且所述挡液区域内布置有穿透所述侧部的多个孔以允许气体经由所述孔通过。本申请能提供改善的挡液效率，避免带液现象。

Device for treatment of process or industrial effluents

FIELD: process engineering. ^ SUBSTANCE: proposed device comprises evaporator incorporating heat exchanger with tube bundle with its side with pure distillate communicated with separator intended for separating distillate from supernatant organic phase or similar unbound fluid components. Separator and said heat exchanger are directly communicated so that fluid levels in separator and evaporator get normally equalised. Separator incorporates level regulator to open pressure release valve in fluid level drop and close said valve in fluid level increase. ^ EFFECT: higher quality of distillation. ^ 11 cl, 2 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 429 896 (13) C2 (51) МПК B01D 1/28 (2006.01) B01D 5/00 (2006.01) C02F 1/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2008134861/05, 03.02.2007 (24) Дата начала отсчета срока действия патента: 03.02.2007 (72) Автор(ы): ФИККЕНШЕР Маттиас (DE), ЛАДЕНБЕРГЕР Даниель (DE) R U (73) Патентообладатель(и): Н2ОГмбХ (DE) Приоритет(ы): (30) Конвенционный приоритет: 11.02.2006 DE 102006006324.4 (43) Дата публикации заявки: 20.03.2010 Бюл. № 8 2 4 2 9 8 9 6 (45) Опубликовано: 27.09.2011 Бюл. № 27 (56) Список документов, цитированных в отчете о поиске: WO 92/03203 A1, 05.03.1992. GB 382891 A, 03.11.1932. US 2487884 A, 15.11.1949. RU 2215871 C2, 10.11.2003. 2 4 2 9 8 9 6 R U (86) Заявка PCT: EP 2007/000935 (03.02.2007) C 2 C 2 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 11.09.2008 (87) Публикация заявки РСТ: WO 2007/090583 (16.08.2007) Адрес для переписки: 105064, Москва, а/я 88, "Патентные поверенные Квашнин, Сапельников и партнеры", пат. пов. В.П. Квашнину, рег. № 4 (54) УСТРОЙСТВО ДЛЯ ОЧИСТКИ ТЕХНОЛОГИЧЕСКИХ ИЛИ ПРОМЫШЛЕННЫХ СТОЧНЫХ ВОД (57) Реферат: Изобретение относится к устройству для очистки технологических или промышленных сточных вод. Устройство для очистки технологических или промышленных сточных вод имеет ...

Meg regeneration apparatus

MEG 재생장치가 개시된다. 본 발명의 실시 예에 따른 MEG 재생장치는 전처리부로부터 저용해도염이 제거된 리치 MEG를 공급받아 리치 MEG로부터 물을 증발시켜 린 MEG를 생성하는 증류탑과, 증류탑 하부의 생성물을 공급받아 가열시켜 증류탑으로 돌려보내는 리보일러를 포함하는 재농축부; 재농축부로부터 공급받은 린 MEG로부터 고용해도염을 제거하는 플래시 세퍼레이터와, 플래시 세퍼레이터 상부의 기체성분을 응축시키는 재생응축기와, 재생응축기에 의해 응축된 생성물을 기액 분리하는 재생드럼을 포함하는 재생부; 및 플래시 세퍼레이터 상부의 기체성분 또는 재생드럼에 저장된 액상의 생성물을 증류탑으로 주입하여 증류탑에서 염이 석출되는 현상을 방지하는 염희석라인;을 포함한다. An MEG playback apparatus is disclosed. MEG regeneration apparatus according to an embodiment of the present invention receives a rich MEG from which the low-solubility salt is removed from the pretreatment unit to evaporate water from the rich MEG to produce a lean MEG and a distillation column by receiving a product from the bottom of the distillation column and heated A reconcentration unit including a reboiler returned to the outlet; A regeneration unit including a flash separator for removing solid-solution sea salt from lean MEG supplied from the reconcentration unit, a regeneration condenser for condensing gas components on the upper part of the flash separator, and a regeneration drum for gas-liquid separating the product condensed by the regeneration condenser ; And a salt dilution line for injecting a gaseous component on the flash separator or a liquid product stored in a regeneration drum into a distillation column to prevent the precipitation of salt in the distillation column.

Evaporation system comprising a series of evaporators for treating an ammoxidation process stream

프로세스 스트림으로부터 중질의 유기물 불순물들을 제거하기 위한 방법 및 시스템은 물 및 약 0.5 내지 약 1.5 중량 퍼센트의 중질의 유기물 불순물들을 갖는 프로세스 스트림을 제공하는 단계를 포함한다. 방법은 하나 이상의 증발 스테이지들을 갖는 증발기 시스템에서 중질의 유기물 불순물들로부터 물을 분리하여 수용성 응축액 및 액체 잔여물을 제공하는 단계를 포함한다. 수용성 응축액은 약 0.1 중량 퍼센트 이하의 중질의 유기물 불순물들을 갖고 액체 잔여물은 약 3 내지 약 10 중량 퍼센트의 중질의 유기물 불순물들을 갖는다.

A kind of jasmine flower concrete production technology negative pressure piece-rate system

本发明属于香料提取设备技术领域，具体的说是一种茉莉花浸膏生产工艺用负压分离系统，包括负压抽吸模块、冷凝罐、控制器和收集箱；负压抽吸模块用于将蒸发罐中的石油醚溶剂输送到冷凝罐中，负压抽吸模块同时能够将石油醚蒸气加压液化，冷凝罐通过二号抽吸泵与收集箱连接；控制器用于控制负压抽吸模块工作；负压抽吸模块包括开合单元和抽吸单元，开合单元用于控制一号软管和二号软管中的石油醚蒸气流入抽吸单元中；滑动板能够相对与光杆直线运动；滑动板上固定安装有永磁块；可变极性电磁块通过与永磁块配合用于使滑动板作直线往复运动；本发明主要用于对茉莉浸膏工艺中的浸提液进行浓缩，能够提高石油醚的分离效率。

Downward film evaporator

本发明涉及降膜式蒸发器，包括由圆柱形壳(1)和凸起端(2,3)形成的外壳，由在所述外壳内排列的竖直管(6)形成的至少一个管束(4，5)，由此释放热量的可冷凝蒸气可以从下面向上进料到所述竖直管(6)中，而接受热量的可蒸发液体可以进料到所述管束(4，5)的上端以作为薄液层沿所述竖直管(6)的外表面向下流动，由此用于排放包含在所述释放热量的蒸气中的不可冷凝气体的装置得以布置在所述管束(4，5)中。本发明的特征在于所述蒸发器包括两个或更多个管束(4，5)，它们各自配置有自身的管板(7，8)，由此各管束(4，5)的竖直管(6)在下端与相应管束(4，5)的管板(7,8)连接以及在上端与相应管束(4，5)的收集多支管(9)连接。

Co-current contacting separation tray design and methods for using same

Operation management device for a vaporization device, fresh water generator provided with the operation management device, and operation management method and fresh water-generating method for vaporization devices

가열함으로써 황산칼슘을 포함하는 피처리수를 증발 농축하는 증발 장치(4)의 운전 조건을 제어하는 운전 관리 장치(6)로서, 소정 온도에 있어서의 이온 강도와 황산칼슘의 포화 용해도곱의 관계에 의해 미리 결정되는 포화 용해도곱 곡선 데이터와, 피처리수에 있어서의 이온 강도를 산출하는 이온 강도 산출 수단(62)과, 상기 피처리수에 있어서의 황산칼슘의 용해도곱을 산출하는 용해도곱 산출 수단(63)과, 이온 강도 산출 수단(62) 및 용해도곱 산출 수단(63)에 의해 산출한 이온 강도값 및 황산칼슘의 용해도곱값과 상기 포화 용해도곱 곡선 데이터를 비교함으로써 상기 피처리수의 이온 강도값에 대한 황산칼슘의 용해도곱값이 포화 용해도곱값을 넘지 않는 증발 장치(4)의 운전 조건을 산출하는 운전 조건 산출 수단(64)과, 운전 조건 산출 수단(64)이 산출한 운전 조건으로 되도록 증발 장치(4)의 운전 조건을 변경하는 운전 조건 변경 수단(65)을 구비하고 있다. 이 발명에 따르면, 황산칼슘 스케일 석출을 방지하면서 효율 좋게 담수를 생성할 수 있는 증발 장치의 운전 관리 장치를 제공할 수 있다. (6) for controlling the operating condition of the evaporation device (4) for evaporating and concentrating the water to be treated containing calcium sulfate by heating, characterized in that the relationship between the ionic strength at a predetermined temperature and the saturation solubility of calcium sulfate The ionic strength calculating means 62 for calculating the ionic strength in the water to be treated, and the solubility product calculating means (for calculating the solubility product of calcium sulfate in the for- 63), the ionic strength value and the solubility product value of calcium sulfate calculated by the ionic strength calculating means (62) and the solubility product calculating means (63) and the saturation solubility product curve data, The operation condition calculation means 64 for calculating the operation condition of the evaporation device 4 in which the solubility product value of calcium sulfate does not exceed the saturation solubility product value, Changing the operating conditions to change the operating conditions of the evaporator (4) such that in one operating condition and means (65). According to the present invention, it is possible to provide an operation management apparatus for an evaporation apparatus capable of efficiently generating fresh water while preventing calcium sulfate scale precipitation.

non-condensed gas extracting device of gas heater

본 발명은 가스히터의 불응축가스 추기장치에 관한 것으로, 밀폐용기(10)에서 버너(40) 배기관(30)의 반대쪽 끝 부분에 추기구(11)를 설치하고, 상기 추기구(11)내에 버너(40) 연료공급관을 경유시킴으로써 추기구(11)내 수증기 분압을 최소화하여 불응축가스 추기 효율을 향상시킨다. 또한, 정압기 출구온도 또는 가스히터 출구온도에 따라 버너(40) 작동을 제어하고, 열매체 온도에 따라 진공펌프(50) 작동을 제어함으로써 추기제어로직을 단순화할 수 있고, 필요한 때에 정확하고 효율적으로 추기를 실시할 수 있다. The present invention relates to a non-condensing gas scavenging device of the gas heater, and installs the weight mechanism 11 in the closed end of the burner (40) on the opposite end of the exhaust pipe 30, the inside of the weight mechanism (11) By passing through the burner 40 fuel supply pipe, the partial pressure of water vapor in the extraction mechanism 11 is minimized to improve the efficiency of non-condensable gas extraction. In addition, by controlling the operation of the burner 40 according to the outlet temperature of the constant pressure or the gas heater, and controlling the operation of the vacuum pump 50 according to the heat medium temperature, the bleeding control logic can be simplified, and bleeding is accurately and efficiently when necessary. Can be carried out.

Wiped film evaporator

本发明涉及蒸发器设备领域，且公开了一种刮板式薄膜蒸发器，包括加热套管、包括加热套管、蒸发套管、二次处理箱、传动轴、布料器，蒸发套管设于加热套管内，二次处理箱设在加热套管的顶部，所述加热套管蒸发套管内腔的中部设有可旋转的传动轴，所述传动轴的顶端固定套装有位于二次处理箱上方的旋转接头。该刮板式薄膜蒸发器，通过传动轴、搅拌机构、固定通管、密封塞、连动轴、搅拌轴和导流机构的设计，在使用时，利用蒸发处理后的干蒸汽从蒸发套管的底部斜向上喷出，一定程度上减缓了物料的下流速率，提高物料的蒸发效果，同时，干蒸汽对内侧物料进行加热，进一步提高加热效果，有利于物料的充分加热。

Dimethyl formamide evaporation system and production process

本发明具体涉及一种二甲基甲酰胺的蒸发系统及生产工艺。以一氧化碳、二甲胺作为原料在甲醇/甲醇钠的催化作用下制备二甲基甲酰胺具有产品质量好、成本低的优点，但甲醇钠溶于水易产生结晶，并且会催化DMF在蒸发工序中发生逆反应生成二甲胺。本发明提供了一种适用于上述生产方式的DMF蒸发系统及生产工艺，所述生产工艺包括以下步骤：DMF合成塔的粗DMF进入分离器内进行初步浓缩之后，分两路与过滤机进行强制循环，一路在第二循环泵进口加水，通过加水保证蒸发循环泵正常运行，另一个是抑制DMF的逆反应进行。另一路的第一循环泵起到过滤排出系统盐泥的作用。所述生产工艺能够有效提升DMF运行周期，提高产量。

A kind of organosilicon slag slurry processing unit

本发明属于有机硅生产技术领域，具体的说是一种有机硅渣浆处理装置，包括罐盖、罐体、进料口、出料口和出气口，所述罐盖上设置有进料口和出气口，所述罐盖和罐体之间通过法兰连接，所述罐体呈锥形，所述罐体底部设置有出料口，所述罐体外侧设置有控制器；所述电机安装在安装支架上，所述电机输出轴与转轴连接；所述支撑杆中部固定连接在转轴上，所述支撑架顶部固连在支撑杆上，所述转轴底部固连着一号气缸，所述一号气缸的伸缩杆穿过支撑架底部连接着搅拌模块；本发明通过一号气缸带动搅拌模块转动的同时上下往复移动搅拌罐体内的有机硅渣浆，从而使得有机硅渣浆的搅拌充分，提高装置的蒸发效率。

Thin film descent evaporation concentrator

The present invention relates to a thin film descending type evaporation concentrator. More specifically, the present invention provides a thin film descending type evaporation concentrator capable of enhancing energy efficiency while allowing a solution to disperse and flow evenly from the top. The thin film descending type evaporation concentrator comprises: an evaporator; a heating unit; a fluid circulation unit; and an energy regeneration unit.

Liquid purifying/distillation device

A distillation purifying system including a section which creates a vacuum pressure that is transmitted throughout the system, a distillation/purification zone in which fluids to be distilled/purified are treated, and a collection zone in which the distilled/purified liquids are transferred. The system is effective for use with liquids, solutions, fluids and the like and can be used for water treatment as well as bodily fluid treatment.