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公开(公告)号：US06438994B1
公开(公告)日：2002-08-27
申请号：US09963450
申请日：2001-09-27
申请人： Mohammad Abdul-Aziz Rashad , Kenneth Kai Wong , Henry Edward Howard , Dante Patrick Bonaquist , Bayram Arman
发明人： Mohammad Abdul-Aziz Rashad , Kenneth Kai Wong , Henry Edward Howard , Dante Patrick Bonaquist , Bayram Arman
IPC分类号： F25J100
CPC分类号： F25J1/005 , F25B9/006 , F25B9/06 , F25B25/00 , F25B40/00 , F25B2400/23 , F25J1/0022 , F25J1/0052 , F25J1/0055 , F25J1/0077 , F25J1/0097 , F25J1/0212 , F25J1/0268 , F25J1/0292 , F25J2270/90
摘要： A method for generating refrigeration using a turboexpander or reverse Brayton cycle which can more efficiently generate refrigeration especially to cryogenic temperatures using a defined refrigerant mixture containing argon and/or nitrogen.
摘要翻译： 一种使用涡轮膨胀机或反向布雷顿循环产生制冷的方法，其可以使用包含氩和/或氮的限定的制冷剂混合物更有效地产生特别是低温的制冷。
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公开(公告)号：US06477859B2
公开(公告)日：2002-11-12
申请号：US10000447
申请日：2001-12-04
IPC分类号： F25J300
CPC分类号： F25J3/0266 , F25J3/0295 , F25J3/08 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/02 , F25J2205/60 , F25J2220/82 , F25J2245/02 , F25J2270/02 , F25J2270/12 , F25J2270/60 , F25J2270/90 , F25J2290/40 , Y02C10/12 , Y10S62/928
摘要： A system for producing carbon dioxide wherein carbon dioxide feed fluid is first processed in a cooling section of an integrated heat exchanger before purification in a column, and wherein column bottom fluid operates within one of an evaporating section and desuperheating section of the heat exchanger and refrigerant fluid operates within the other of the evaporating section and desuperheating section of the heat exchanger.
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3.发明授权Cryogenic hybrid system for producing low purity oxygen and high purity nitrogen 失效用于生产低纯氧和高纯度氮的低温混合系统
公开(公告)号：US5701763A
公开(公告)日：1997-12-30
申请号：US778075
申请日：1997-01-07
CPC分类号： B01D53/04 , F25J3/04296 , F25J3/04636 , B01D2256/10 , B01D2257/102 , B01D2257/104 , B01D2257/504 , B01D2257/80 , B01D2259/402 , B01D2259/404 , B01D2259/416 , F25J2200/02 , F25J2200/72 , F25J2205/60 , F25J2205/66 , F25J2210/04 , F25J2215/44 , F25J2215/50 , F25J2245/50 , Y02C10/08 , Y10S62/908
摘要： A hybrid system for producing both low purity oxygen and high purity nitrogen at high product recovery rates wherein desorption effluent from an adsorbent system feeds a cryogenic rectification column and, preferably, bottom fluid from the column provides additional feed for the adsorbent system.
摘要翻译： 用于在高产物回收率下生产低纯度氧和高纯度氮的混合系统，其中来自吸附剂系统的解吸流出物进料低温精馏塔，优选来自塔的底部流体为吸附剂系统提供额外的进料。
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公开(公告)号：US07871457B2
公开(公告)日：2011-01-18
申请号：US11395137
申请日：2006-04-03
申请人： Minish Mahendra Shah , Ravi Kumar , Henry Edward Howard , Bernard Thomas Neu , Dante Patrick Bonaquist , John Fredric Billingham
发明人： Minish Mahendra Shah , Ravi Kumar , Henry Edward Howard , Bernard Thomas Neu , Dante Patrick Bonaquist , John Fredric Billingham
IPC分类号： B01D53/02
CPC分类号： F25J3/0266 , B01D53/0462 , B01D53/047 , B01D53/0476 , B01D2253/10 , B01D2253/106 , B01D2256/16 , B01D2256/22 , B01D2257/504 , B01D2257/80 , B01D2259/40069 , B01D2259/40071 , B01D2259/40073 , B01D2259/4062 , C01B3/384 , C01B3/48 , C01B3/56 , C01B32/50 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/0475 , C01B2203/0816 , C01B2203/1241 , C01B2203/1288 , C01B2203/148 , C01B2203/86 , F25J3/0223 , F25J3/0252 , F25J2200/02 , F25J2200/70 , F25J2205/02 , F25J2205/40 , F25J2205/60 , F25J2205/66 , F25J2205/82 , F25J2210/04 , F25J2220/82 , F25J2230/30 , F25J2230/80 , F25J2240/40 , F25J2245/02 , F25J2260/80 , F25J2270/02 , Y02C10/08 , Y02C10/12 , Y02P20/152 , Y02P30/30
摘要： A method of producing a carbon dioxide product stream from a synthesis gas stream formed within a hydrogen plant having a synthesis gas reactor, a water-gas shift reactor, located downstream of the synthesis gas reactor to form the synthesis gas stream and a hydrogen pressure swing adsorption unit to produce a hydrogen product recovered from the synthesis gas stream. In accordance with the method the carbon dioxide from the synthesis gas stream by separating the carbon dioxide from the synthesis gas stream in a vacuum pressure swing adsorption system, thereby to produce a hydrogen-rich synthesis gas stream and a crude carbon dioxide stream and then purifying the crude carbon dioxide stream by a sub-ambient temperature distillation process thereby to produce the carbon dioxide product. A hydrogen synthesis gas feed stream to the hydrogen pressure swing adsorption unit is formed at least in part from the hydrogen rich stream.
摘要翻译： 一种从在合成气流中形成的合成气流生产二氧化碳产物流的方法，所述氢气装置具有位于合成气反应器下游的合成气反应器，水煤气变换反应器，以形成合成气流和氢气压摆 吸附单元以产生从合成气流中回收的氢产物。 根据该方法，通过在真空变压吸附系统中从合成气流中分离二氧化碳从合成气流中获得二氧化碳，由此产生富氢合成气流和粗二氧化碳流，然后纯化 粗二氧化碳流通过次环境温度蒸馏过程从而产生二氧化碳产物。 至少部分地从富氢流形成氢转化吸附单元的氢合成气进料流。
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5.发明授权Cryogenic hybrid system for producing low purity oxygen and high purity oxygen 失效用于生产低纯氧和高纯氧的低温混合系统
公开(公告)号：US5666828A
公开(公告)日：1997-09-16
申请号：US672463
申请日：1996-06-26
CPC分类号： B01D53/04 , F25J3/04284 , F25J3/04333 , F25J3/04345 , F25J3/04636 , B01D2256/12 , B01D2257/102 , B01D2259/416 , F25J2200/02 , F25J2200/04 , F25J2200/38 , F25J2200/50 , F25J2205/60 , F25J2210/50 , F25J2215/50 , F25J2215/56 , F25J2245/50 , F25J2250/20 , Y10S62/901 , Y10S62/908
摘要： A method for producing low purity oxygen and high purity oxygen using a cryogenic rectification column wherein feed air is enriched in oxygen in an upstream adsorbent bed system prior to passage into the column and refrigeration is generated by turboexpansion of adsorbent bed effluent or column top vapor.
摘要翻译： 一种使用低温精馏塔生产低纯度氧和高纯度氧的方法，其中进料空气在进入塔内之前在上游吸附剂床系统中富含氧气，并且通过吸附床流出物或塔顶蒸气的涡轮膨胀产生冷冻。
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公开(公告)号：US06881354B2
公开(公告)日：2005-04-19
申请号：US10201287
申请日：2002-07-24
CPC分类号： F25J1/0268 , C09K5/041 , C09K5/045 , C09K2205/112 , C09K2205/13 , C09K2205/22 , F25B5/02 , F25B9/006 , F25B2400/06 , F25B2400/23 , F25J1/0022 , F25J1/0052 , F25J1/0055 , F25J1/0097 , F25J1/0212 , F25J1/0214
摘要： Multicomponent refrigerant fluids for generating refrigeration, especially over a wide temperature range including cryogenic temperatures, which are advantageous over conventional refrigerant fluids especially for certain applications, and which are non-toxic, non-flammable and low or non-ozone-depleting and preferably are maintained in variable load form through compression, cooling, expansion and warming steps in a refrigeration cycle.
摘要翻译： 用于产生制冷的多组分制冷剂流体，特别是在包括低温温度的宽温度范围内，其比常规制冷剂流体尤其对于某些应用有利，并且是无毒的，不易燃的和低的或非消耗臭氧的，优选是 通过制冷循环中的压缩，冷却，膨胀和升温步骤保持可变负载形式。
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公开(公告)号：US06591618B1
公开(公告)日：2003-07-15
申请号：US10216359
申请日：2002-08-12
IPC分类号： F25B100
CPC分类号： F25B9/008 , F25B9/002 , F25B9/06 , F25B40/00 , F25B2309/061 , F25B2400/14
摘要： A method for providing refrigeration to a refrigeration load which enables the use of environmentally friendly refrigerants with lower power consumption than with conventional refrigerants wherein the low side pressure of the circuit exceeds the critical pressure of the refrigerant fluid and the refrigerant fluid is compressed to a higher supercritical pressure prior to expansion.
摘要翻译： 一种用于向制冷负荷提供制冷的方法，其能够使用具有比常规制冷剂更低功耗的环保制冷剂，其中电路的低侧压力超过制冷剂流体的临界压力并且制冷剂流体被压缩到更高 扩张前的超临界压力。
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公开(公告)号：US20230115492A1
公开(公告)日：2023-04-13
申请号：US17717189
申请日：2022-04-11
摘要： A small to mid-scale liquefied natural gas production system and method is provided. The disclosed liquefied natural gas production system employs a nitrogen-based refrigerant, at least one heat exchanger, three turbine/expanders and two or more refrigerant compression stages. The expansion ratio of one turbine/expander is appreciably lower than the expansion ratio of the other turbine/expanders such that the temperature of the exhaust stream from the turbine/expander with the lower expansion ratio is above the critical point temperature of the compressed natural gas feed stream but colder than −15° C.
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公开(公告)号：US20230114229A1
公开(公告)日：2023-04-13
申请号：US17717182
申请日：2022-04-11
申请人： Henry Edward Howard
发明人： Henry Edward Howard
摘要： A small to mid-scale liquefied natural gas production system and method is provided. The disclosed liquefied natural gas production system employs a nitrogen-based refrigerant, at least one heat exchanger, three turbine/expanders and two or more refrigerant compression stages. The expansion ratio of one turbine/expander is appreciably lower than the expansion ratio of the other turbine/expanders such that the temperature of the exhaust stream from the turbine/expander with the lower expansion ratio is above the critical point temperature of the compressed natural gas containing feed stream but colder than -15° C.
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公开(公告)号：US10048002B2
公开(公告)日：2018-08-14
申请号：US14994708
申请日：2016-01-13
申请人： Henry Edward Howard
发明人： Henry Edward Howard
IPC分类号： F25J3/04
摘要： A cryogenic air separation method and apparatus in which first and second liquid streams are produced. The first liquid stream has a higher oxygen content than air and can consist of a higher pressure distillation column bottoms and the second liquid stream, for instance, air, has a lower oxygen content than the first liquid stream and an argon content no less than the air. The second liquid stream is subcooled through indirect heat exchange with the first liquid stream and both of such streams are introduced into the lower pressure column. The second liquid stream is introduced into the lower pressure column above that point at which the crude liquid oxygen column bottoms or any portion thereof is introduced into the lower pressure column to increase a liquid to vapor ratio below the introduction of the second liquid stream and therefore, reduce the oxygen present within the column overhead.
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