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41. 发明授权

US5475980A Process and installation for production of high pressure gaseous fluid 失效
标题翻译：用于生产高压气态流体的工艺和安装
公开(公告)号：US5475980A
公开(公告)日：1995-12-19
申请号：US219349
申请日：1994-03-29
申请人： Maurice Grenier , Bao Ha
发明人： Maurice Grenier , Bao Ha
IPC分类号： F25J3/04 , F25J3/02
CPC分类号： F25J3/04381 , F25J3/04054 , F25J3/0406 , F25J3/04084 , F25J3/0409 , F25J3/04175 , F25J3/04296 , F25J3/04303 , F25J3/04351 , F25J3/04393 , F25J3/04412 , F25J2205/04 , F25J2215/54 , F25J2230/20 , F25J2290/10 , Y10S62/94
摘要： Auxiliary gas is withdrawn from the heat exchanger during cooling or reheating at an intermediate temperature which is close to the vaporizing temperature of the oxygen or nitrogen high pressure product stream, then compressed by a cold compressor and reintroduced in the heat exchanger. The invention is particularly applicable to the production of gaseous oxygen at a pressure greater than about 15 bar.
摘要翻译：在接近氧气或氮气高压产物流的蒸发温度的中间温度下冷却或再加热时，辅助气体从热交换器中排出，然后由冷压缩机压缩并重新引入热交换器。本发明特别适用于在大于约15巴的压力下生产气态氧。

42. 发明授权

US5321946A Method and system for a condensing boiler and flue gas cleaning by cooling and liquefaction 失效
标题翻译：冷凝锅炉和冷却液化烟气清洗的方法和系统
公开(公告)号：US5321946A
公开(公告)日：1994-06-21
申请号：US977138
申请日：1992-11-16
申请人： Fawzy T. Abdelmalek
发明人： Fawzy T. Abdelmalek
IPC分类号： B01D53/00 , B01D53/24 , B01D53/32 , B03C3/019 , C01B17/60 , C10J3/54 , F01K23/06 , F23J15/00 , F25B11/02 , F25B11/04 , F25J3/02 , F25J3/06 , F28D15/02 , F01K25/14
CPC分类号： F28D15/0266 , B01D53/002 , B01D53/24 , B01D53/32 , B03C3/019 , C01B17/60 , C10J3/54 , F01K23/067 , F23J15/006 , F25B11/02 , F25B11/04 , F25J3/067 , F23J2215/20 , F23J2217/102 , F23J2219/70 , F25B2400/14 , F25B2400/141 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2220/84 , F25J2230/20 , F25J2230/30 , F25J2245/02 , Y02C10/12 , Y02E20/18 , Y02E20/326 , Y02P20/123 , Y02P20/124 , Y02P20/129 , Y02P20/152 , Y02P20/57 , Y10S165/913
摘要： A method for cleaning a flue gas stream continuously emitting from a thermal power plant fossil fueled boiler, and containing hazardous volatile organic vapors, heavy metal vapors, nitrogen oxides, sulfur dioxide, and carbon dioxide by cooling, condensing and gas liquefaction processes employing a heat recovery condensing heat exchanging, and a gas compressor-expander open heat cycle systems.
摘要翻译：一种用于清洁从火力发电厂化石燃料锅炉连续发射的烟气流的方法，并且通过使用热量的冷却，冷凝和气体液化方法含有有害挥发性有机蒸气，重金属蒸汽，氮氧化物，二氧化硫和二氧化碳回收冷凝热交换，以及气体压缩机 - 膨胀机开放式循环系统。

43. 发明授权

US4977745A Method for the recovery of low purity carbon dioxide 失效
标题翻译：回收低纯二氧化碳的方法
公开(公告)号：US4977745A
公开(公告)日：1990-12-18
申请号：US325766
申请日：1989-03-20
申请人： Albert N. Heichberger
发明人： Albert N. Heichberger
IPC分类号： F25J3/02 , F25J3/06
CPC分类号： F25J3/0266 , F25J3/0257 , F25J2205/30 , F25J2205/40 , F25J2205/80 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2230/20 , F25J2230/30 , F25J2240/12 , F25J2240/70 , F25J2240/80 , F25J2245/90 , F25J2260/20 , F25J2270/02 , F25J2270/04 , F25J2270/06 , F25J2270/90 , F25J2270/904 , Y02C10/12 , Y10S62/928
摘要： A process for the economical recovery of carbon dioxide from a gas stream containing less than 85% carbon dioxide, by cooling the contaminating gas to remove water vapor, compressing the cooled gas to an elevated temperature and pressure, and drying the gas to a dewpoint of not more than about -85.degree. F.; condensing and removing the carbon dioxide from the dried compressed gas; and heating the remaining noncondensed gas mixture and expanding it to produce and recover kinetic energy and a cooled gas mixture.
摘要翻译：一种从含有少于85％二氧化碳的气流中经济回收二氧化碳的方法，通过冷却污染气体以除去水蒸汽，将冷却的气体压缩至升高的温度和压力，并将气体干燥至不超过约-85°F。从干燥的压缩气体中冷凝和去除二氧化碳; 并加热剩余的非冷凝气体混合物并使其膨胀以产生并回收动能和冷却的气体混合物。

44. 发明授权

US4548629A Process for the liquefaction of natural gas 失效
标题翻译：天然气液化过程
公开(公告)号：US4548629A
公开(公告)日：1985-10-22
申请号：US540957
申请日：1983-10-11
申请人： Chen-hwa Chiu
发明人： Chen-hwa Chiu
IPC分类号： F25J1/02 , F25J3/02
CPC分类号： F25J1/0264 , F25J1/0022 , F25J1/0035 , F25J1/004 , F25J1/0045 , F25J1/0052 , F25J1/0055 , F25J1/0085 , F25J1/0095 , F25J1/0097 , F25J1/0216 , F25J1/0218 , F25J1/0249 , F25J1/0268 , F25J1/0292 , F25J2205/02 , F25J2205/30 , F25J2210/06 , F25J2220/62 , F25J2220/64 , F25J2220/66 , F25J2220/68 , F25J2230/20 , F25J2230/60 , F25J2245/90 , F25J2270/90
摘要： The present invention is a process for the liquefaction of high pressure natural gas. The natural gas is expanded through a turboexpander to reduce its pressure and thereby cool it. The natural gas is then passed through a demethanizer to remove the heavier components therefrom. The natural gas is then precooled, before substantial warming occurs, by heat exchange with a C.sub.2 hydrocarbon refrigerant, either ethane or ethylene, contained in a single refrigerant system. The precooled natural gas is liquefied by heat exchange with a mixed refrigerant contained in a mixed refrigerant system. The mixed refrigerant consists essentially of nitrogen, methane and a C.sub.2 hydrocarbon, either ethane or ethylene. The mixed refrigerant contained in the mixed refrigerant system is cooled by heat exchange with the C.sub.2 hydrocarbon refrigerant contained in the single refrigerant system.
摘要翻译：本发明是用于液化高压天然气的方法。天然气通过涡轮膨胀机膨胀以降低其压力，从而使其冷却。然后将天然气通过脱甲烷塔以从其中除去较重的组分。然后通过与包含在单个制冷剂系统中的C2烃制冷剂（乙烷或乙烯）进行热交换，在大量升温之前将天然气预冷却。通过与包含在混合制冷剂系统中的混合制冷剂进行热交换，将预冷却的天然气液化。混合的制冷剂主要由氮，甲烷和C2烃，乙烷或乙烯组成。包含在混合制冷剂系统中的混合制冷剂通过与包含在单个制冷剂系统中的C2烃制冷剂进行热交换而被冷却。

45. 发明授权

US4453956A Recovering condensables from natural gas 失效
标题翻译：从天然气中回收冷凝物
公开(公告)号：US4453956A
公开(公告)日：1984-06-12
申请号：US390686
申请日：1982-06-21
申请人： Cesare Fabbri , Gianfranco Bellitto , Giuseppe La Mantia , Biagio Failla
发明人： Cesare Fabbri , Gianfranco Bellitto , Giuseppe La Mantia , Biagio Failla
IPC分类号： C10G5/06 , C01D20060101 , F25J3/02
CPC分类号： F25J3/0238 , F25J3/0209 , F25J3/0233 , F25J3/0242 , F25J2200/04 , F25J2200/70 , F25J2200/78 , F25J2205/02 , F25J2205/04 , F25J2205/60 , F25J2220/68 , F25J2230/20 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2270/04 , F25J2290/40
摘要： To recover condensates from natural gas the raw gas is sent to a high-pressure separator (4) and the incondensable gas is sent to the first stage of an expansion turbine (16) and expanded to a pressure nearly equal to that of the head of a fractionation column (25, 28, 29) composed of three sections, top (25), intermediate (29) and bottom (28). The liquids from the separator (4) are expanded in a second separator (14) and fed to the bottom section (28). The gas from the second separator (14) is mixed with the exhaust from the first turbine stage (16) and fed to the lower portion of the top section (25) to the head of which there is sent the liquid issuing from the intermediate section (29). The latter receives the exhaust from the second turbine stage (36) which is fed by the gas from the top section (25) head. The liquid on the bottom of the top section (25) is fed to the bottom section (28 ). The residual gas is drawn from the top of the intermediate section (29) is compressed by the coaxial compressor to the turbine whereas the condensates are drawn from the bottom section (28).
摘要翻译：为了从天然气中回收冷凝物，原料气体被输送到高压分离器（4），并且不可冷凝气体被输送到膨胀涡轮机（16）的第一级，并且膨胀到几乎等于由三个部分，顶部（25），中间（29）和底部（28）组成的分馏塔（25,28,29）。来自分离器（4）的液体在第二分离器（14）中膨胀并被供给到底部部分（28）。来自第二分离器（14）的气体与来自第一涡轮机台（16）的排气混合，并被供给到顶部（25）的下部，从而将从中间部分发出的液体送出（29）。后者从第二涡轮级（36）接收来自顶部（25）头的气体供给的排气。顶部（25）的底部上的液体被供给到底部（28）。从中间部分（29）的顶部抽出的残余气体被同轴压缩机压缩到涡轮机，而冷凝物从底部部分（28）拉出。

46. 发明授权

US4312851A Treatment of ammonia synthesis purge gas 失效
标题翻译：处理氨合成吹扫气
公开(公告)号：US4312851A
公开(公告)日：1982-01-26
申请号：US83827
申请日：1979-10-11
申请人： Wieslaw H. Isalski , Terence R. Tomlinson
发明人： Wieslaw H. Isalski , Terence R. Tomlinson
IPC分类号： C01C1/04 , F25J3/06
CPC分类号： F25J3/068 , C01C1/0476 , F25J3/062 , F25J2210/20 , F25J2230/20 , F25J2240/02 , Y02P20/52
摘要： A method of synthesizing ammonia by reacting a synthesis gas comprising nitrogen and hydrogen at superatmospheric pressure in a synthesis reaction zone with recycling of unreacting gas to the reacting zone is disclosed in which a purge gas stream is withdrawn at superatmospheric pressure and subjected to the steps of: (a) work expansion, (b) separation of methane and argon to form a gaseous product stream comprising nitrogen and hydrogen, (c) recompression of at least a portion of the gaseous product stream from step (b) using work generated in step (a), and (d) recycling of at least a portion of the recompressed product from step (c) to the reaction zone.Apparatus for effecting said process is also claimed.
摘要翻译：公开了一种合成氨的方法，该方法是通过在合成反应区中使含氮和氢的合成气在超大气压下反应而将反应气体再循环到反应区，其中吹扫气流在超大气压下被排出，：（a）工作膨胀，（b）分离甲烷和氩气以形成包含氮气和氢气的气态产物流，（c）使用在步骤（b）中产生的工作来重新压缩来自步骤（b）的气态产物流的至少一部分（a）和（d）将来自步骤（c）的再压缩产物的至少一部分再循环到反应区。还要求用于实现所述方法的装置。

47. 发明授权

US4184325A Plant and process for recovering waste heat 失效
标题翻译：回收废热的设备和工艺
公开(公告)号：US4184325A
公开(公告)日：1980-01-22
申请号：US809399
申请日：1977-06-23
申请人： Charles Mandrin
发明人： Charles Mandrin
IPC分类号： F01K23/10 , F01K25/10 , F02C6/18 , F02C7/00 , F04D29/58 , F17D1/02 , F02C7/02
CPC分类号： F25J3/061 , F01K23/10 , F01K25/10 , F02C6/18 , F04D29/5833 , F17D1/02 , F25J3/0635 , F25J3/0645 , F25J2230/20 , F25J2230/22 , F25J2230/30 , F25J2230/60 , F25J2240/82 , F25J2270/12 , F25J2270/60 , Y02E20/16
摘要： A flow of hot combustion gas from an open gas turbine plant surrenders heat via an intermediate forced-flow circuit to a vapor circuit system in which a hydrocarbon working medium flows. The forced-flow intermediate circuit uses a liquid heat vehicle such as a mixture of diphenyl and diphenyl oxide to transfer heat from the hot exhaust gas of the open gas turbine plant to the working medium of the vapor circuit system. This heat vehicle is passed through a plurality of successively connected tubes in the exhaust gas duct so as to reduce the amount of leakage should a leak occur in the tubes and, thus, the chance of an explosion.The waste heat transferred to the vapor circuit system can be used to drive a compressor of a refrigerating circuit, e.g. used to cool a flow of natural gas in a pipeline located in an arctic region.
摘要翻译：来自开放式燃气轮机设备的热燃烧气体流经由中间强制流动回路将热量传递到其中烃工作介质流动的蒸气回路系统。强制流动中间回路使用诸如二苯基和二苯基氧化物的混合物的液体热交换器将热量从开放式燃气轮机设备的热废气转移到蒸汽回路系统的工作介质。该热交换器通过排气管道中的多个连续连接的管，以减少管中发生泄漏的泄漏量，从而减少爆炸的机会。传递到蒸汽回路系统的废热可用于驱动制冷回路的压缩机，例如，用于冷却位于北极地区的管道中的天然气流。

48. 发明授权

US3919852A Reliquefaction of boil off gas 失效
标题翻译：蒸发气体的再液化
公开(公告)号：US3919852A
公开(公告)日：1975-11-18
申请号：US49309474
申请日：1974-07-30
申请人： PETROCARBON DEV LTD
发明人： JONES JAMES KEVIN
IPC分类号： F25J1/00 , F25J1/02 , F25B19/00
CPC分类号： F25J1/0204 , F25J1/0025 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/005 , F25J1/0052 , F25J1/0072 , F25J1/0202 , F25J1/023 , F25J1/0259 , F25J1/0265 , F25J1/0283 , F25J1/0288 , F25J2210/06 , F25J2220/62 , F25J2230/20
摘要： Method of reliquefying gas resulting from the evaporation of a ship''s cargo of liquefied gas which utilizes a compression refrigerator having two refrigerant loops in one of which the compressed refrigerant is expanded in a turbine and in the other of which it is expanded without the performance of external work. The expansion turbine and a gas turbine which can be fueled by the gas provide the power for compressing the refrigerant, and the gas is reliquefied by heat exchange with cold expanded refrigerant in the second loop. In one embodiment open loops are used with the gas providing the refrigerant.
摘要翻译：重新液化气体蒸发的气体的方法，其利用具有两个制冷剂回路的压缩制冷机，其中压缩制冷剂中的一个压缩制冷剂在涡轮机中膨胀，而另一个压缩制冷剂在不具有外部性能的情况下膨胀工作。可以由气体燃料的膨胀涡轮机和燃气轮机提供用于压缩制冷剂的动力，并且通过与第二回路中的冷膨胀制冷剂的热交换再气化气体。在一个实施例中，与提供制冷剂的气体一起使用开环。

49. 发明授权

US3657898A Method and apparatus for producing refrigeration 失效
公开(公告)号：US3657898A
公开(公告)日：1972-04-25
申请号：US3657898D
申请日：1968-08-15
申请人： AIR PROD & CHEM
发明人： NESS LEIF A , THOMAS EDMUND P
IPC分类号： F25B27/00 , F01D1/08 , F01D15/00 , F25B9/06 , F25J1/00 , F25J1/02
CPC分类号： F25B9/06 , F01D1/08 , F01D15/005 , F25J1/0015 , F25J1/0037 , F25J1/004 , F25J1/0208 , F25J1/0234 , F25J1/0236 , F25J1/0279 , F25J1/0288 , F25J3/04224 , F25J3/04278 , F25J3/04357 , F25J3/04375 , F25J3/04381 , F25J3/04393 , F25J3/04866 , F25J2230/20 , F25J2240/02 , F25J2270/06 , F25J2270/90
摘要： Refrigeration system including a multi-stage compressor and two work expansion engines of the turbine type with the impellers of the expansion engines and the impeller of the final stage of the compressor being mounted on a common shaft. The work developed in the expansion engines provides the total power required for the final stage of the compressor and the final stage of the compressor provides the pressurized gas expanded in both expansion engines.

50. 发明授权

US3503220A Expander cycle for natural gas liquefication with split feed stream 失效
标题翻译：用于自然进气流量的膨胀剂循环
公开(公告)号：US3503220A
公开(公告)日：1970-03-31
申请号：US3503220D
申请日：1967-07-27
申请人： CHICAGO BRIDGE & IRON CO
发明人： DESAI SUDHIR HARILAL
IPC分类号： F25J1/00 , F25J1/02 , F25J3/08
CPC分类号： F25J1/0022 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/0201 , F25J1/0232 , F25J2210/06 , F25J2220/64 , F25J2220/66 , F25J2230/20 , F25J2230/60 , F25J2245/90 , F25J2270/06
摘要： 1,180,496. Natural gas liquefaction process. CHICAGO BRIDGE & IRON CO. 20 Feb., 1968 [27 July, 1967], No. 8221/68. Heading F4P. Liquefaction of compressed natural gas containing carbon dioxide, methane and higher hydrocarbons is effected by dividing the feed gas into first and second streams 12, 30 cooling the first stream by work-expansion in a turbine 18 without solidification of carbon dioxide, absorbing carbon dioxide at 31 from the second stream 30, cooling the latter to effect partial liquefaction in heat exchangers 24, 23, 22 in countercurrent to said expanded first stream, separating at 62 an impure liquid fraction containing heavy hydrocarbons from said cooled second stream, expanding this separated liquid at a valve 64 and using the cold so produced in a terminal exchanger 67 to liquefy vapour withdrawn from the separator 62 through a line 70. Most of the liquid methane is expanded at a valve 72 into a storage tank 74 at about atmospheric pressure whilst a minor portion of liquid methane is expanded at a valve 77 and joins the cold vapour leaving valve 64. A phase separator 44 is interposed in the second stream between exchangers 24, 23 and separated higher hydrocarbons are expanded at a valve 48 whilst a portion of the uncondensed vapour is withdrawn through a line 45, expanded in a turbine 37 and the two portions combined in a line 50 with the aforementioned expanded portions from separator 62. Effluent from tank 74 is compressed at 79, added to the first feed stream leaving turbine 18 and is then warmed in exchangers 22, 23, 24, 13 and fed into a consumer line 26.

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