| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 61 | 液化气的汽化 | CN91105202.X | 1991-07-31 | CN1058643A | 1992-02-12 | J·T·拉文 |
| 在一个用于分离空气的双精馏柱2中，来自低压精馏柱6的液态氧收集在罐25中并且在重力作用下流出该罐25，向下流过一个热交换器或冷凝-再沸器16，在其中液态氧的落膜藉助与来自高压精馏柱4的冷凝氮蒸汽的热交换而再沸。未汽化的液态氧流出冷凝-再沸器16的底，落入低压精馏柱6的槽68中的大量的液态氧66中。热交换器70和72部分地浸没在该大量液态氧66中，藉助与冷凝的氮蒸汽的热交换将热虹吸的液态氧汽化。 | ||||||
| 62 | 열교환기 분리형 천연가스 액화 장치 | KR1020100103733 | 2010-10-22 | KR101064576B1 | 2011-09-15 | 정제헌; 최동규; 문영식; 유진열; 이정한 |
| 본 발명은 천연가스를 공급받아 냉매와의 열교환에 의해 액화되도록 하며, 스테인레스 스틸 재질로 이루어지는 액화용 열교환기와, 액화용 열교환기에 냉매를 알루미늄 재질로 이루어지는 냉매용 열교환기에 의해 냉각시켜서 공급하는 냉매 냉각부를 포함하는 열교환기 분리형 천연가스 액화 장치가 제공된다.
본 발명에 따르면, 냉매용 열교환기와 액화용 열교환기가 분리되도록 하여 냉매용 열교환기는 알루미늄 재질의 열교환기를 적용함으로써 비용 절감을 가져오도록 하고, 액화용 열교환기는 스테인레스 스틸 재질의 열교환기를 적용함으로써 천연가스에 대한 불순물의 제거가 필요없도록 하거나 낮은 수준의 불순물 제거만으로 액화 공정이 수행되도록 함으로써 액화 공정이 복잡해지는 것을 방지할 수 있다. |
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| 63 | 극저온 분리에 의한 천연가스의 정제방법 | KR1020017009836 | 2000-01-26 | KR1020010101983A | 2001-11-15 | 바클레이마이클에이.; 브룩토마스씨.; 바클레이존에이.; 티슨레이몬드알. |
| 활성열교환기및 재생열교환기를포함하는, CO와제 2 가스를포함하는가스혼합물로부터의 CO분리장치. 활성열교환기는가스의혼합물과접촉하고있는열교환표면을포함한다. 가스의혼합물은 CO가예정된압력에서응결되는온도보다낮은온도를가지는냉매에의해표면이냉각될때 열교환표면에서 CO가응결되도록선택된예정된압력에서활성열교환기에존재한다. 재생열교환기는냉매및 또한응결된 CO의층과접촉하고있는열교환표면을포함한다. 냉매는 CO의응결된층에서 CO가승화되는온도보다높은온도에서재생열교환기에진입한다. 고체 CO의승화는냉매의온도를예정된압력에서 CO의응결점보다낮은온도까지하강시키는, 팽창밸브를통해팽창하기에앞서냉매를냉각시킨다. 냉매는활성열교환기를이탈한후에압축기에의해재압축된다. 본발명의바람직한양태에서, 재생열교환기에의해배출된가스 CO는진입하는가스혼합물을예비냉각하는데 사용된다. 제 2 예비냉각열교환기는활성열교환기를이탈하는냉매와의열적접촉을제공함으로써압축된냉매를예비냉각시킨다. | ||||||
| 64 | Hydrocyclone For Cryogenic Gas-Vapor Separation | US15439177 | 2017-02-22 | US20180236397A1 | 2018-08-23 | Larry Baxter; Christopher Hoeger; Aaron Sayre; Skyler Chamberlain; Kyler Stitt; Eric Mansfield; Stephanie Burt; Andrew Baxter; Jacom Chamberlain; Nathan Davis |
| A hydrocyclone for separating a vapor from a carrier gas is disclosed. The hydrocyclone comprises one or more nozzles. A cryogenic liquid is injected to a tangential feed inlet at a velocity that induces a tangential flow and a cyclone vortex in the hydrocyclone. The carrier gas is injected into the cryogenic liquid, causing the vapor to dissolve, condense, desublimate, or a combination thereof, forming a vapor-depleted carrier gas and a vapor-enriched cryogenic liquid. The vapor-depleted carrier gas is drawn through a vortex finder and the vapor-enriched cryogenic liquid is drawn through an apex nozzle outlet. In this manner, the vapor is removed from the carrier gas. | ||||||
| 65 | HEAT EXCHANGERS FOR LOW TEMPERATURE CARBON DIOXIDE SEPARATION FROM NATURAL GAS | US15846898 | 2017-12-19 | US20180106535A1 | 2018-04-19 | Lubo Zhou; Thomas J. Godry; Zhanping Xu |
| A reboiler in fluid communication with a fractionator column in an offshore low temperature process removing carbon dioxide from natural gas has a vessel volume. A carbon steel tubing bundle is disposed within the vessel volume. Each tube in the bundle has an outer surface with a porous granular metal layer deposited thereon. The granular metal layer comprises a pore size distribution which promotes bubble nucleation during vaporization of a nearly pure liquid carbon dioxide stream. | ||||||
| 66 | HEAT EXCHANGER COMPRISING MICROSTRUCTURE ELEMENTS AND SEPARATION UNIT COMPRISING SUCH A HEAT EXCHANGER | US15566913 | 2016-04-13 | US20180106534A1 | 2018-04-19 | Erwan LE GULUDEC; Clement LIX; David QUERE; Quentin SANIEZ; Bernard SAULNIER; Evan SPRUIJT; Marc WAGNER |
| The invention relates to a heat exchanger comprising parallel plates and spacers arranged in parallel and defining i) rough primary channels and ii) secondary channels arranged so as to exchange heat. Said heat exchanger comprises a primary liquid inlet to be fluidically connected to a primary liquid dispenser. Each rough primary channel has the shape of a prism having a polygonal cross-section and consisting of a plurality of essentially flat faces. The primary channels comprise rough primary channels. Each rough primary channel has microstructure elements which are distributed along the entire length of the channel and have dimensions of between 1 μm and 300 μm. | ||||||
| 67 | Carbon Dioxide Capture from Flu Gas | US15728014 | 2017-10-09 | US20180031315A1 | 2018-02-01 | Larry Baxter |
| A method for capturing carbon dioxide from a flue gas includes (i) removing moisture from a flue gas to yield a dried flue gas; (ii) compressing the dried flue gas to yield a compressed gas stream; (iii) reducing the temperature of the compressed gas stream to a temperature T1 using a first heat exchanger; (iv) reducing the temperature of the compressed gas stream to a second temperarature T2 using a second heat exchanger stream, where T2 | ||||||
| 68 | Defroster for oxygen liquefier | US14004910 | 2012-03-09 | US09845920B2 | 2017-12-19 | Laurent Brouqueyre; Brian Edward Dickerson |
| An oxygen liquefier system may be configured to defrost an oxygen line included therein. The system may include one or more sieve beds, a liquid oxygen reservoir, an oxygen line, a controller, a heating apparatus, and/or other components. The one or more sieve beds are configured to extract oxygen from air obtained from an ambient environment. The liquid oxygen reservoir is configured to store oxygen extracted at the one or more sieve beds that has been liquefied. The oxygen line is configured to provide fluid communication between the one or more sieve beds and the liquid oxygen reservoir. The controller is configured to detect a blockage caused by frozen liquid within the oxygen line based on a liquid oxygen production rate. The heating apparatus is configured to defrost the oxygen line to melt frozen liquid within the oxygen line responsive to the detection of the blockage. | ||||||
| 69 | DISTILLATION METHOD AND STRUCTURED PACKING | US15161369 | 2016-05-23 | US20160263548A1 | 2016-09-15 | John F. Billingham; Guang X. Chen |
| A method of conducting a distillation process and a cross-corrugated structured packing for use in such a process in which ascending vapor phases and descending liquid phases are contacted in such packing. The cross-corrugated structured packing contains corrugated sheets fabricated of an open cell foam-like material. The liquid phase produces a liquid film descending along struts forming cells of the material and the vapor phase ascends within the cross-corrugated structured packing and enters the cells and contacts the liquid film. The cross-corrugated structured packing is configured such that a superficial velocity at which ambient air would flow through the cross-corrugated structured packing at a pressure drop of 0.3″ wc/ft is no greater than 20 times a reference superficial velocity at which the ambient air would flow through the foam-like material making up the corrugated sheets at the same pressure drop to ensure that vapor enters the cells of the foam-like material. | ||||||
| 70 | CONDENSER-REBOILER SYSTEM AND METHOD WITH PERFORATED VENT TUBES | US15153179 | 2016-05-12 | US20160258678A1 | 2016-09-08 | Hanfei Tuo; Karl K. Kibler; Maulik R. Shelat |
| A system and method for the concurrent condensation of a nitrogen-rich vapor and vaporization of an oxygen-rich liquid in a distillation column based air separation unit is provided. The disclosed system includes a condenser-reboiler heat exchanger located between a lower pressure column and a higher pressure column and configured to condense a nitrogen-rich vapor from the higher pressure column and partially vaporize an oxygen-rich liquid from the lower pressure column. Within the condenser-reboiler heat exchanger, the nitrogen-rich vapor flows in an upward direction such that any non-condensables present in the nitrogen-rich vapor will accumulate proximate the upper portion or top of the condenser-reboiler modules where they can be easily removed through venting by means of a venting apparatus having a plurality of perforated tubes. | ||||||
| 71 | Distillation method and structured packing | US13981924 | 2012-01-13 | US09375655B2 | 2016-06-28 | John Billingham; Guang X. Chen |
| A method of conducting a distillation process and a cross-corrugated structured packing for use in such a process in which ascending vapor phases and descending liquid phases are contacted in such packing. The cross-corrugated structured packing contains corrugated sheets fabricated of an open cell foam-like material. The liquid phase produces a liquid film descending along struts forming cells of the material and the vapor phase ascends within the cross-corrugated structured packing and enters the cells and contacts the liquid film. The cross-corrugated structured packing is configured such that a superficial velocity at which ambient air would flow through the cross-corrugated structured packing at a pressure drop of 0.3″ wc/ft is no greater than 20 times a reference superficial velocity at which the ambient air would flow through the foam-like material making up the corrugated sheets at the same pressure drop to ensure that vapor enters the cells of the foam-like material. | ||||||
| 72 | CONDENSER-REBOILER SYSTEM AND METHOD WITH PERFORATED VENT TUBES | US14947466 | 2015-11-20 | US20160076809A1 | 2016-03-17 | Hanfei Tuo; Karl K. Kibler; Maulik R. Shelat |
| A system and method for the concurrent condensation of a nitrogen-rich vapor and vaporization of an oxygen-rich liquid in a distillation column based air separation unit is provided. The disclosed system includes a condenser-reboiler heat exchanger located between a lower pressure column and a higher pressure column and configured to condense a nitrogen-rich vapor from the higher pressure column and partially vaporize an oxygen-rich liquid from the lower pressure column. Within the condenser-reboiler heat exchanger, the nitrogen-rich vapor flows in an upward direction such that any non-condensables present in the nitrogen-rich vapor will accumulate proximate the upper portion or top of the condenser-reboiler modules where they can be easily removed through venting by means of a venting apparatus having a plurality of perforated tubes. | ||||||
| 73 | HEAT EXCHANGER FOR A LIQUEFIED NATURAL GAS FACILITY | US14633307 | 2015-02-27 | US20150253071A1 | 2015-09-10 | Wesley R. QUALLS; Matthew C. GENTRY; Paula A. LEGER; Robert L. BOULANGER |
| A method of constructing a plate fin heat exchanger includes joining a first side bar formed from a nickel-iron alloy to a first end of a fin element formed from a nickel-iron alloy through a first nickel-iron alloy bond, and joining a second side bar formed from a nickel-iron alloy to a second end of the fin element through a second nickel-iron alloy bond to create a first layer of the plate fin heat exchanger. The fin element defines a fluid passage. | ||||||
| 74 | EFFICIENT SELF COOLING HEAT EXCHANGER | US14034500 | 2013-09-23 | US20140020874A1 | 2014-01-23 | Phillip F. Daly; Kurt M. Vanden Bussche |
| An inexpensive heat exchanger is disclosed, wherein the heat exchanger is made up of a plurality of plates and each plate has at least one channel defined in the plate. The plates are stacked and bonded together to form a block having conduits for carrying at least one fluid and where the exchanger includes an expansion device enclosed within the unit. The plates include construction to thermally insulate the sections of the heat exchanger to control the heat flow within the heat exchanger. | ||||||
| 75 | Self cooling heat exchanger with channels having an expansion device | US12485284 | 2009-06-16 | US08631858B2 | 2014-01-21 | Phillip F. Daly; Kurt M. Vanden Bussche |
| An inexpensive heat exchanger is disclosed, wherein the heat exchanger is made up of a plurality of plates and each plate has at least one channel defined in the plate. The plates are stacked and bonded together to form a block having conduits for carrying at least one fluid and where the exchanger includes an expansion device enclosed within the unit. | ||||||
| 76 | DISTILLATION METHOD AND STRUCTURED PACKING | US13981924 | 2012-01-13 | US20130313103A1 | 2013-11-28 | John Billingham; Guang X. Chen |
| A method of conducting a distillation process and a cross-corrugated structured packing for use in such a process in which ascending vapor phases and descending liquid phases are contacted in such packing. The cross-corrugated structured packing contains corrugated sheets fabricated of an open cell foam-like material. The liquid phase produces a liquid film descending along struts forming cells of the material and the vapor phase ascends within the cross-corrugated structured packing and enters the cells and contacts the liquid film. The cross-corrugated structured packing is configured such that a superficial velocity at which ambient air would flow through the cross-corrugated structured packing at a pressure drop of 0.3″ wc/ft is no greater than 20 times a reference superficial velocity at which the ambient air would flow through the foam-like material making up the corrugated sheets at the same pressure drop to ensure that vapor enters the cells of the foam-like material. | ||||||
| 77 | Efficient self cooling heat exchanger | US13397716 | 2012-02-16 | US08555954B2 | 2013-10-15 | Phillip F. Daly; Kurt M. Vanden Bussche |
| An inexpensive heat exchanger is disclosed, wherein the heat exchanger is made up of a plurality of plates and each plate has at least one channel defined in the plate. The plates are stacked and bonded together to form a block having conduits for carrying at least one fluid and where the exchanger includes an expansion device enclosed within the unit. The plates include construction to thermally insulate the sections of the heat exchanger to control the heat flow within the heat exchanger. | ||||||
| 78 | SYTEM AND METHOD FOR LIQUEFYING AND STORING A FLUID | US13498387 | 2010-08-17 | US20120180900A1 | 2012-07-19 | Laurent Brouqueyre; Tuan Nguyen; Gregg Russell Hurst |
| A fluid is liquefied from a gaseous state to a liquid state, and the liquefied fluid is stored. In one embodiment, the fluid is oxygen. Mechanisms are employed that enhance the durability, longevity, reliability, efficiency, of a system used to liquefy the fluid. | ||||||
| 79 | SYTEM AND METHOD FOR LIQUEFYING AND STORING A FLUID | US13498394 | 2010-08-17 | US20120180520A1 | 2012-07-19 | Brian Edward Dickerson; Laurent Brouqueyre; Gregg Russell Hurdst |
| A fluid is liquefied from a gaseous state to a liquid state, and the liquefied fluid is stored. In one embodiment, the fluid is oxygen. Mechanisms are employed that enhance the durability, longevity, reliability, efficiency, of a system used to liquefy the fluid. | ||||||
| 80 | Process for decreasing or eliminating unwanted hydrocarbon and oxygenate products caused by Fisher Tropsch Synthesis reactions in a syngas treatment unit | US12627601 | 2009-11-30 | US08163809B2 | 2012-04-24 | Trapti Chaubey; Yudong Chen; Robert Gagliano |
| The present invention provides a process for decreasing or eliminating unwanted hydrocarbon and oxygenate products caused by FTS reactions in a syngas treatment unit by utilizing heat exchangers and optionally associated pipes that are substantially fabricated of a material selected from the group consisting of chromium containing alloys and carbon steel for heating up gas streams having a carbon monoxide partial pressure of less than or equal to one bar and obtained from a front end purification unit/cold box unit. | ||||||
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