EP2601472A1 - U-tube vaporizer - Google Patents
U-tube vaporizerInfo
- Publication number
- EP2601472A1 EP2601472A1 EP11736387.9A EP11736387A EP2601472A1 EP 2601472 A1 EP2601472 A1 EP 2601472A1 EP 11736387 A EP11736387 A EP 11736387A EP 2601472 A1 EP2601472 A1 EP 2601472A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- chamber
- partition
- liquid
- vaporizer
- tubes
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B7/00—Steam boilers of furnace-tube type, i.e. the combustion of fuel being performed inside one or more furnace tubes built-in in the boiler body
- F22B7/16—Component parts thereof; Accessories therefor, e.g. stay-bolt connections
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/06—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/02—Tubular elements of cross-section which is non-circular
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0265—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0061—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
- F28D2021/0064—Vaporizers, e.g. evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/0071—Evaporators
Definitions
- the present invention relates to a vaporizer.
- a vaporizer constituted by a heat exchanger in which a heat transfer fluid transfers heat to a liquid to be vaporized, the liquid flowing in at least one U-shaped tube connected to a plate.
- This vaporizer may for example be a backup vaporizer, which vaporizes cryogenic liquid to a network, to compensate the flow from a cryogenic unit.
- This system is usually powered by a cryogenic pump and the vaporized liquid in the pin is sent to the customer when the air separation unit stops.
- a vaporizer 4 consisting of a cylindrical chamber 7 and a hemispherical dome, both being separated by a vertical plate 13 pierced with openings. These openings are connected to U-shaped pipes so that one end of the pipe is attached to an opening in the lower part of the vertical plate 13 and the other end is attached to an opening in the upper part of this plate .
- the dome is divided in a sealed manner into an upper part 5 and a lower part 3 by a horizontal flat plate forming a partition 6.
- a liquid to be vaporized is introduced into the lower part 3 which forms a feed chamber and circulates in tubes U-shaped 17.
- the liquid arrives towards the upper part 5 of the dome 2, which constitutes an evacuation chamber. There it is entirely vaporized by the exchange of heat with steam 9 or other heat transfer gas sent into the chamber 7 and which circulates around the tube or tubes 17. The gas formed by vaporizing the liquid is withdrawn from the upper part 5 of the dome 2. The cooled water vapor 1 1 leaves the atmosphere at the top of the chamber 7.
- This vaporization system has a relatively long start-up time, even when the cryogenic pump sends the full flow to this system emergency, it is necessary to wait between 30 seconds and a minute before observing the full flow of vaporization.
- An object of the invention is to reduce the commissioning time of a vaporizer and reduce the overall cost of the apparatus incorporating the vaporizer by eliminating or reducing the size of the buffer capacity.
- a vaporizer comprising a plurality of U-shaped tubes contained in an enclosure, each tube having two ends, the tubes being arranged in at least one plane, the enclosure being closed on one side by a plate having as many apertures as there are tube ends, the apertures comprising apertures and low apertures, each tube being connected at one end to a top aperture of the plate and at a bottom end to a low opening of the plate, a dome covering the plate on the opposite side to that of the tubes, the dome being delimited by a partition orthogonal to the plane of the tubes to form an admission chamber and an evacuation chamber characterized in that the intake chamber is divided into two parts by a partition perpendicular to the plane of the tubes and the partition to form a liquid inlet chamber between the plate and the partition and a chamber on the other side of the partition, the liquid inlet from the outside of the vaporizer opening into the inlet chamber and the auxiliary chamber being arranged to receive only liquid from the inlet chamber so that the liquid coming from the outside arriving
- the partition includes an opening towards its bottom edge to allow a circulation of liquid between the partition and the dome.
- the volume of the inlet chamber is smaller than that of the auxiliary chamber.
- the volume of the inlet chamber is at least two times smaller than that of the auxiliary chamber.
- the lower openings are arranged at different distances from the partition.
- the vaporizer comprises an inlet of circulating fluid opening into the chamber.
- the chamber of ad dition and the evacuation chamber have substantially the same shape and volume
- the partition is a flat plate.
- the liquid from the outside can enter the auxiliary chamber only through an opening in the partition or passing over the partition.
- the liquid inlet is formed in the enclosure.
- the liquid inlet is arranged so that in use the liquid enters the bottom of the vaporizer.
- a cryogenic distillation separation apparatus comprising a vaporizer according to one of the preceding claims and means for supplying it with cryogenic liquid.
- a method of vaporizing a liquid in a vaporizer in which a heat-generating gas is sent to the chamber, a liquid to be vaporized is introduced into the inlet chamber and evacuates the liquid vaporized by the evacuation chamber.
- the improvement device according to the invention is therefore a weir system which preferentially feeds the tubes of the exchanger to the rise in production of the vaporization system.
- This spillway consists of a solid plate open at the top and equipped with a deconcentration hole for hydrocarbon safety located at the bottom of the tank.
- Figure 2 illustrates a vertical section of the vaporizer
- Figure 3 shows a side view of the interior of the vaporizer of Figure 2.
- the vaporizer of FIG. 2 differs from that of FIG. 1 in that a solid plate 21 forms a partial partition dividing the lower part 3 of the dome 2 into two unequal parts.
- the left part of FIG. 1 corresponds to the left part of the vaporizer of FIG. 2.
- the partition 21 is arranged substantially vertically, so that about one third of the volume of the lower part 3 is located between this partition 21 and the plate 13.
- the partition 21 does not extend to the horizontal plate of the partition 6 and an opening 23 is formed in the middle of the partition 21 at its bottom edge.
- the liquid enters from the outside into the space of the lower part 3 only through an inlet disposed between the plate 13 and the partition 21.
- the opening 23 is small, the liquid accumulates in this space and the liquid level rises so that all the pipes 17 opening into the plate 13 are fed.
- the liquid flows to the other side of the plate 21.
- the liquid can also pass into the opening 23.
- the plate 13 is seen, the openings being not illustrated for the sake of simplification.
- the plate 21 has a horizontal edge and a curved edge that matches the interior of the lower part 3 of the dome 2.
- the invention is also applicable to the vaporization of liquids which condense at temperatures above cryogenic temperatures.
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1056376A FR2963417B1 (en) | 2010-08-02 | 2010-08-02 | U-SHAPED TUBE VAPORIZER |
PCT/EP2011/063061 WO2012016915A1 (en) | 2010-08-02 | 2011-07-29 | U-tube vaporizer |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2601472A1 true EP2601472A1 (en) | 2013-06-12 |
EP2601472B1 EP2601472B1 (en) | 2015-03-04 |
Family
ID=43767345
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11736387.9A Active EP2601472B1 (en) | 2010-08-02 | 2011-07-29 | U-tube vaporizer |
Country Status (8)
Country | Link |
---|---|
US (1) | US9109795B2 (en) |
EP (1) | EP2601472B1 (en) |
JP (1) | JP2013532815A (en) |
KR (1) | KR101816951B1 (en) |
CN (1) | CN103052861B (en) |
ES (1) | ES2535390T3 (en) |
FR (1) | FR2963417B1 (en) |
WO (1) | WO2012016915A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11371655B2 (en) | 2017-11-15 | 2022-06-28 | Taylor-Wharton Malaysia Sdn. Bhd. | Cryogenic fluid vaporizer |
CN108731493A (en) * | 2018-05-17 | 2018-11-02 | 无锡市鹅湖玫瑰园艺文化有限公司 | A kind of Rosa Damascana extraction condensing unit |
CN108917447A (en) * | 2018-08-07 | 2018-11-30 | 广州市铁鑫金属结构有限公司 | A kind of vaporizer |
Family Cites Families (38)
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US2995341A (en) * | 1959-01-08 | 1961-08-08 | Griscom Russell Co | Feed water heater sub-cooling zone |
US3213833A (en) * | 1960-12-30 | 1965-10-26 | Westinghouse Electric Corp | Unitized vapor generation system |
GB1225967A (en) * | 1967-03-22 | 1971-03-24 | ||
US3568764A (en) * | 1969-09-05 | 1971-03-09 | Daniel J Newman | Heat exchanger |
US3759319A (en) * | 1972-05-01 | 1973-09-18 | Westinghouse Electric Corp | Method for increasing effective scavenging vent steam within heat exchangers which condense vapor inside long tubes |
DE2243417B2 (en) * | 1972-09-04 | 1976-07-29 | Siemens AG, 1000 Berlin und 8000 München | STEAM GENERATORS, IN PARTICULAR FOR PRESSURE WATER REACTORS |
AR202467A1 (en) * | 1973-01-25 | 1975-06-13 | Siemens Ag | STEAM GENERATOR |
US3996897A (en) * | 1975-11-21 | 1976-12-14 | General Electric Company | Reheater for a moisture separator reheater |
US4167968A (en) * | 1977-12-30 | 1979-09-18 | Babcock-Brown Boveri Reaktor Gmbh | Pressure vessel |
US4223722A (en) * | 1978-10-02 | 1980-09-23 | General Electric Company | Controllable inlet header partitioning |
US4305548A (en) * | 1980-01-21 | 1981-12-15 | Armstrong Machine Works | Energy loss detection system |
DE3022480A1 (en) * | 1980-06-14 | 1982-01-07 | Uhde Gmbh, 4600 Dortmund | DEVICE FOR EXCHANGING HEAT BETWEEN AN NH (DOWN ARROW) 3 (DOWN ARROW) CONVERTER LEAVING CYCLE GAS AND WATER |
JPS5787235U (en) * | 1980-10-15 | 1982-05-29 | ||
US4396508A (en) * | 1981-08-27 | 1983-08-02 | Broughton Amos W | Separator for multi-phase liquids |
IN160977B (en) * | 1983-09-22 | 1987-08-22 | Sulzer Ag | |
FR2580271B1 (en) * | 1985-04-16 | 1994-07-08 | Air Liquide | OZONE PRODUCTION PROCESS |
US4664754A (en) * | 1985-07-18 | 1987-05-12 | General Electric Company | Spent liquid organic solvent recovery system |
FR2635189B1 (en) * | 1988-08-05 | 1994-01-14 | Framatome | DEVICE FOR NON-DESTRUCTIVE TESTING OF A CIRCULAR WELDING WITHIN A STEAM GENERATOR TUBE |
US5100610A (en) * | 1990-11-20 | 1992-03-31 | Westinghouse Electric Corp. | Tube plug inspection system |
EP0491591B1 (en) * | 1990-12-17 | 1996-05-22 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Air distillation column with a corrugated cross packing |
US5245843A (en) * | 1991-01-31 | 1993-09-21 | Nippondenso Co., Ltd. | Evaporator |
DE4120800C2 (en) * | 1991-06-24 | 1994-09-29 | Siemens Ag | Heat exchanger |
US5390507A (en) * | 1992-09-17 | 1995-02-21 | Nippondenso Co., Ltd. | Refrigerant evaporator |
US6161613A (en) * | 1996-11-21 | 2000-12-19 | Carrier Corporation | Low pressure drop heat exchanger |
CN2288409Y (en) * | 1996-12-06 | 1998-08-19 | 李凯 | Geothermal heating exchanger |
DE19703681A1 (en) * | 1997-01-31 | 1998-08-06 | Linde Ag | Method and device for removing condensable components from gases and / or gas mixtures |
JPH11201685A (en) * | 1998-01-08 | 1999-07-30 | Mitsubishi Electric Corp | Heat-exchanger device |
FR2797942B1 (en) * | 1999-08-24 | 2001-11-09 | Air Liquide | VAPORIZER-CONDENSER AND CORRESPONDING AIR DISTILLATION SYSTEM |
CN1331404A (en) * | 2000-06-22 | 2002-01-16 | 中国船舶重工集团公司第七研究院第七一一研究所 | Heat exchange method for water heater |
US7185698B1 (en) * | 2004-01-22 | 2007-03-06 | Bernert Jr Robert E | Thermal shield for heat exchangers |
JP4023459B2 (en) * | 2004-03-04 | 2007-12-19 | 株式会社デンソー | Heat exchanger |
US7384539B2 (en) * | 2004-07-28 | 2008-06-10 | Conocophillips Company | Optimized preheating of hydrogen/hydrocarbon feed streams |
DE112005002755T5 (en) * | 2004-11-30 | 2007-11-08 | Showa Denko K.K., Minato-ku | heat exchangers |
US7261148B2 (en) * | 2005-05-31 | 2007-08-28 | York International Corporation | Direct expansion cooler high velocity dished head |
WO2007009713A1 (en) * | 2005-07-19 | 2007-01-25 | Behr Gmbh & Co. Kg | Heat exchanger |
US20090064821A1 (en) * | 2006-08-23 | 2009-03-12 | Air Liquide Industrial U.S. Lp | Vapor-Reinforced Expanding Volume of Gas to Minimize the Contamination of Products Treated in a Melting Furnace |
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FI122778B (en) * | 2008-03-31 | 2012-06-29 | Metso Power Oy | Pyrolysis method in conjunction with a boiler, and pyrolysis device |
-
2010
- 2010-08-02 FR FR1056376A patent/FR2963417B1/en not_active Expired - Fee Related
-
2011
- 2011-07-29 ES ES11736387.9T patent/ES2535390T3/en active Active
- 2011-07-29 WO PCT/EP2011/063061 patent/WO2012016915A1/en active Application Filing
- 2011-07-29 CN CN201180038153.XA patent/CN103052861B/en not_active Expired - Fee Related
- 2011-07-29 JP JP2013522211A patent/JP2013532815A/en not_active Withdrawn
- 2011-07-29 EP EP11736387.9A patent/EP2601472B1/en active Active
- 2011-07-29 KR KR1020137002781A patent/KR101816951B1/en active IP Right Grant
- 2011-07-29 US US13/813,098 patent/US9109795B2/en active Active
Non-Patent Citations (1)
Title |
---|
See references of WO2012016915A1 * |
Also Published As
Publication number | Publication date |
---|---|
FR2963417B1 (en) | 2014-03-28 |
US20130125839A1 (en) | 2013-05-23 |
CN103052861B (en) | 2016-04-13 |
KR20140005847A (en) | 2014-01-15 |
US9109795B2 (en) | 2015-08-18 |
CN103052861A (en) | 2013-04-17 |
FR2963417A1 (en) | 2012-02-03 |
ES2535390T3 (en) | 2015-05-11 |
WO2012016915A1 (en) | 2012-02-09 |
JP2013532815A (en) | 2013-08-19 |
EP2601472B1 (en) | 2015-03-04 |
KR101816951B1 (en) | 2018-01-09 |
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