公开(公告)号：EP2442056A3

公开(公告)日：2018-03-07

申请号：EP11185499.8

申请日：2011-10-17

申请人： Daewoo Shipbuilding&Marine Engineering Co., Ltd.

发明人： Yoo, Seong Jin ,  Lee, Jung Han ,  Moon, Young Sik ,  Jung, Je Heon ,  Lee, Jae Yeol ,  Choi, Dong Kyu ,  Yu, Jin Yeol

IPC分类号： F25J1/00 ,  F25J1/02 ,  F17C1/00

CPC分类号： F25J1/0055 ,  F17C2201/0109 ,  F17C2201/032 ,  F17C2201/054 ,  F17C2203/015 ,  F17C2203/035 ,  F17C2203/0631 ,  F17C2203/0636 ,  F17C2203/0643 ,  F17C2203/0646 ,  F17C2205/0111 ,  F17C2205/0146 ,  F17C2205/0323 ,  F17C2205/0326 ,  F17C2205/0341 ,  F17C2205/0397 ,  F17C2209/221 ,  F17C2209/228 ,  F17C2209/234 ,  F17C2221/033 ,  F17C2223/0161 ,  F17C2223/035 ,  F17C2223/045 ,  F17C2227/0121 ,  F17C2227/0341 ,  F17C2227/036 ,  F17C2227/0393 ,  F17C2250/032 ,  F17C2250/0439 ,  F17C2265/012 ,  F17C2265/03 ,  F17C2265/037 ,  F17C2265/05 ,  F17C2270/0105 ,  F17C2270/0113 ,  F25J1/0022 ,  F25J1/005 ,  F25J1/0254 ,  F25J1/0263 ,  F25J1/0265 ,  F25J1/0272 ,  F25J2205/20 ,  F25J2205/24 ,  F25J2205/84 ,  F25J2220/66 ,  F25J2220/68 ,  F25J2290/44 ,  F25J2290/62

摘要： A method for producing pressurized liquefied natural gas and a production system therefor are provided. The method for producing pressurized liquefied natural gas includes: performing a dehydration process (S11) to remove water from natural gas supplied from a natural gas field, without a process of removing acid gas from the natural gas; and performing a liquefaction process (S12) to produce pressurized liquefied natural gas by liquefying the natural gas, which has undergone the dehydration process, at a pressure of 13 to 25 bar and a temperature of -120 to - 95°C, without a process of fractionating natural gas liquid (NGL). Accordingly, it is possible to reduce plant construction costs and maintenance expenses and reduce LNG production costs. In addition, it is possible to guarantee high economic profit and reduce payback period in small and medium-sized gas fields, from which economic feasibility could not be ensured by the use of a conventional method.

摘要翻译： 提供了一种生产加压液化天然气的方法及其生产系统。 用于生产加压液化天然气的方法包括：执行脱水过程（S11），以从天然气田供应的天然气中去除水，而不需要从天然气中去除酸气的过程; 以及在13至25巴的压力和-120至-95℃的温度下通过液化已经过脱水过程的天然气来执行液化过程（S12）以产生加压液化天然气，而无需工艺 分馏天然气液体（NGL）。 因此，可以降低工厂建设成本和维护费用并降低LNG生产成本。 另外，可以保证中小型气田的高经济效益和减少投资回收期，使用传统方法无法保证经济可行性。

公开(公告)号：EP2758724B1

公开(公告)日：2016-02-24

申请号：EP12756777.4

申请日：2012-08-14

申请人： L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude

发明人： BERNHARDT, Jean-Marc ,  DESCHILDRE, Cindy ,  FAUVE, Eric ,  GRILLOT, David

IPC分类号： F25B5/02 ,  F25B43/02 ,  F25B1/10 ,  F25J1/00 ,  F25J1/02 ,  F25B9/00

CPC分类号： F25B43/02 ,  F25B1/10 ,  F25B5/02 ,  F25B9/002 ,  F25J1/0065 ,  F25J1/0201 ,  F25J1/0265 ,  F25J1/027 ,  F25J1/0271 ,  F25J1/0272 ,  F25J1/0279 ,  F25J1/0294 ,  F25J5/00 ,  F25J2230/20 ,  F25J2230/24 ,  F25J2270/912

公开(公告)号：EP0697573B1

公开(公告)日：1998-07-22

申请号：EP95910750.9

申请日：1995-03-07

申请人： KABUSHIKI KAISHA KOBE SEIKO SHO

发明人： ASADA, Kazuhiko Takasago Works in Kobe Steel, Ltd. ,  UENO, Koichi Takasago Works in Kobe Steel, Ltd. ,  KASHIHARA, Shin-ichiro Takasago Works ,  OKAMOTO, Shigemi Takasago Works ,  KUROSE, Katsuo Takasago Works ,  KUWAHARA, Kazuhiko Takasago Works ,  MITSUHASHI, Ken-ichiro Takasago Works

IPC分类号： F25B39/00 ,  F25B39/02 ,  F25B39/04 ,  F25B43/00 ,  F25J3/06 ,  F25B41/00

CPC分类号： F25J1/0022 ,  F25B39/00 ,  F25B41/00 ,  F25J1/0052 ,  F25J1/0262 ,  F25J1/0272 ,  F25J5/002 ,  F25J2205/02 ,  F25J2290/32 ,  F25J2290/50 ,  F28D9/0062 ,  F28F2250/104

摘要： The invention is directed to miniaturizing a housing (2) by combining a plate-fin heat exchanger (1, 1) having a great heat exchange rate relative to a volume with a gas-liquid separator (10) having a lateral H-shape. Provided in the housing (2) are the plate-fin heat exchanger (1, 1) for performing heat exchange between a refrigerant and a fluid to be cooled and the gas-liquid separator (10) such that the refrigerant and the fluid to be cooled are transported through a piping in the housing (2) and heat exchange is performed between the refrigerant and the fluid to be cooled so as to cool the fluid to be cooled while performing separation and mixing of a gas and a liquid in the refrigerant. In order to be laterally H-shaped, the gas-liquid separator (10) comprises an upper storage section (10a) having a hollow cylindrical member gas-tightly sealed at both ends thereof, a lower storage section (10c) and an intermediate section (10b) allowing the both storage sections (10a, 10c) to communicate with each other.

公开(公告)号：EP3379186A1

公开(公告)日：2018-09-26

申请号：EP17290042.5

申请日：2017-03-23

申请人： Dresser-Rand SAS

发明人： BARDON, Patrice ,  NIENHAUS, Georg

IPC分类号： F25J1/00 ,  F25J1/02

CPC分类号： F25J1/0022 ,  F25J1/0052 ,  F25J1/0055 ,  F25J1/0087 ,  F25J1/0216 ,  F25J1/0272 ,  F25J1/0283 ,  F25J1/0284 ,  F25J1/0289 ,  F25J1/0292 ,  F25J1/0294

摘要： Systems and methods are provided for the production of liquefied natural gas. At least one of the systems may include a plurality of compression assemblies in fluid communication with a precooler assembly. One compression assembly may be a part of a precooling loop and may include at least one compressor driven by a variable or fixed speed motor. Another compression assembly may be part of a liquefaction loop and may include at least one pair of compressors, each compressor driven by a respective turbine. The liquefaction loop may be fluidly coupled to a main heat exchanger utilized to liquefy at least a portion of a feed gas stream containing natural gas flowing through the main heat exchanger, thereby producing liquefied natural gas.

公开(公告)号：EP2795214A1

公开(公告)日：2014-10-29

申请号：EP12860640.7

申请日：2012-12-19

申请人： ConocoPhillips Company

发明人： DAVIES, Paul, R. ,  JAMES, Will, T. ,  GRAVOIS, Shaun, P.

IPC分类号： F25J1/02

CPC分类号： F25J1/0022 ,  F25J1/0052 ,  F25J1/0259 ,  F25J1/0262 ,  F25J1/0272 ,  F25J1/0278 ,  F25J1/0279 ,  F25J5/005 ,  F25J2250/02 ,  F25J2250/20 ,  F25J2290/72 ,  F28D21/0017

摘要： In an embodiment, a system for cooling or liquefying a process gas in a motion environment, includes: (a) a separation vessel, wherein the separation vessel includes motion suppressing baffles, wherein the separation vessel separates a high pressure refrigerant stream thereby producing a vapor refrigerant stream and a liquid refrigerant stream; (b) a vapor liquid refrigerant pipe for delivering the liquid refrigerant stream from the separation vessel to an external heat exchanger core; (c) at least one external heat exchanger core, wherein the external heat exchanger core is external to a kettle, wherein the liquid refrigerant stream and a warmer process stream undergo indirect heat exchange in the external heat exchanger core thereby producing a cooled process stream and a vaporized refrigerant stream.

公开(公告)号：EP1281033B1

公开(公告)日：2006-02-08

申请号：EP01927923.1

申请日：2001-04-24

申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.

发明人： ELION, Wiveka, Jacoba ,  JONES, Keith, Anthony ,  MCLACHLAN, Gregory, John ,  WILSON, Jonathan, Hamilton

IPC分类号： F25J1/02

CPC分类号： F25J1/0244 ,  F25J1/0022 ,  F25J1/0055 ,  F25J1/0212 ,  F25J1/0258 ,  F25J1/0272

摘要： Controlling the production of a liquefied natural gas (31) comprises measuring the temperature (50) and the flow rate (55) of the liquefied natural gas (31); maintaining the flow rate of the heavy mixed refrigerant (60a) at an operator manipulated set point (80), and determining the flow rate of the light mixed refrigerant (86) from (i) the flow rate of the heavy mixed refrigerant (80) and (ii) an operator manipulated set point for the ratio of the flow rate of the heavy mixed refrigerant to the flow rate of the light mixed refrigerant (81); determining a dependent set point (91) for the ratio of the flow rate of the liquefied natural gas to the flow rate of the heavy mixed refrigerant such that the temperature (50) of the liquefied natural gas is maintained at an operator manipulated set point (90); determining a dependent set point (95) for the flow rate of the liquefied natural gas (95) from (i) the dependent set point (91) for the ratio of the flow rate of the liquefied natural gas product stream to the flow rate of the heavy mixed refrigerant and (ii) the flow rate of the heavy mixed refrigerant (60c); and maintaining the flow rate of the liquefied natural gas (55a) at its dependent set point (95).

公开(公告)号：EP1281033A1

公开(公告)日：2003-02-05

申请号：EP01927923.1

申请日：2001-04-24

申请人： SHELL INTERNATIONALE RESEARCHMAATSCHAPPIJ B.V.

发明人： ELION, Wiveka, Jacoba ,  JONES, Keith, Anthony ,  MCLACHLAN, Gregory, John ,  WILSON, Jonathan, Hamilton

IPC分类号： F25J1/02

CPC分类号： F25J1/0244 ,  F25J1/0022 ,  F25J1/0055 ,  F25J1/0212 ,  F25J1/0258 ,  F25J1/0272

摘要： Controlling the production of a liquefied natural gas (31) comprises measuring the temperature (50) and the flow rate (55) of the liquefied natural gas (31); maintaining the flow rate of the heavy mixed refrigerant (60a) at an operator manipulated set point (80), and determining the flow rate of the light mixed refrigerant (86) from (i) the flow rate of the heavy mixed refrigerant (80) and (ii) an operator manipulated set point for the ratio of the flow rate of the heavy mixed refrigerant to the flow rate of the light mixed refrigerant (81); determining a dependent set point (91) for the ratio of the flow rate of the liquefied natural gas to the flow rate of the heavy mixed refrigerant such that the temperature (50) of the liquefied natural gas is maintained at an operator manipulated set point (90); determining a dependent set point (95) for the flow rate of the liquefied natural gas (95) from (i) the dependent set point (91) for the ratio of the flow rate of the liquefied natural gas product stream to the flow rate of the heavy mixed refrigerant and (ii) the flow rate of the heavy mixed refrigerant (60c); and maintaining the flow rate of the liquefied natural gas (55a) at its dependent set point (95).

公开(公告)号：EP0697573A4

公开(公告)日：1996-04-24

申请号：EP95910750

申请日：1995-03-07

申请人： KOBE STEEL LTD

发明人： ASADA KAZUHIKO ,  UENO KOICHI ,  KASHIHARA SHIN-ICHIRO ,  OKAMOTO SHIGEMI ,  KUROSE KATSUO ,  KUWAHARA KAZUHIKO ,  MITSUHASHI KEN-ICHIRO

IPC分类号： F25B39/00 ,  F25B41/00 ,  F25J3/00 ,  F25J5/00 ,  F28D9/00 ,  F25B39/02 ,  F25B39/04 ,  F25B43/00 ,  F25J3/06

CPC分类号： F25J1/0022 ,  F25B39/00 ,  F25B41/00 ,  F25J1/0052 ,  F25J1/0262 ,  F25J1/0272 ,  F25J5/002 ,  F25J2205/02 ,  F25J2290/32 ,  F25J2290/50 ,  F28D9/0062 ,  F28F2250/104

摘要： The invention is directed to miniaturizing a housing (2) by combining a plate-fin heat exchanger (1, 1) having a great heat exchange rate relative to a volume with a gas-liquid separator (10) having a lateral H-shape. Provided in the housing (2) are the plate-fin heat exchanger (1, 1) for performing heat exchange between a refrigerant and a fluid to be cooled and the gas-liquid separator (10) such that the refrigerant and the fluid to be cooled are transported through a piping in the housing (2) and heat exchange is performed between the refrigerant and the fluid to be cooled so as to cool the fluid to be cooled while performing separation and mixing of a gas and a liquid in the refrigerant. In order to be laterally H-shaped, the gas-liquid separator (10) comprises an upper storage section (10a) having a hollow cylindrical member gas-tightly sealed at both ends thereof, a lower storage section (10c) and an intermediate section (10b) allowing the both storage sections (10a, 10c) to communicate with each other.

公开(公告)号：EP0580276A1

公开(公告)日：1994-01-26

申请号：EP93301751.9

申请日：1993-03-08

申请人： CHIYODA CORPORATION

发明人： Kikkawa, Yoshitsugi, Chiyoda Corporation ,  Yamamoto, Osamu, Chiyoda Corporation ,  Ohmori, Kenrou, Chiyoda Corporation ,  Ohmori, Motohiro, Chiyoda Corporation ,  Nozawa, Noriyoshi, Chiyoda Corporation

IPC分类号： F25J3/06 ,  F28D9/00

CPC分类号： F25J1/0055 ,  F25J1/0022 ,  F25J1/0052 ,  F25J1/0087 ,  F25J1/0216 ,  F25J1/0262 ,  F25J1/0265 ,  F25J1/0267 ,  F25J1/0272 ,  F25J1/0282 ,  F25J1/0292 ,  F25J5/002 ,  F25J5/005 ,  F25J2205/02 ,  F25J2220/62 ,  F25J2220/64 ,  F25J2230/60 ,  F25J2245/02 ,  F25J2250/02 ,  F25J2290/32 ,  F25J2290/50 ,  Y10S62/903

摘要： Provided is an improved refrigeration system for pre-cooling natural gas or cooling a mixed refrigerant for natural gas liquefaction in a propane refrigeration process widely used for the liquefaction of natural gas. The system comprises a plurality of plate-fin heat exchangers (31) preferably arranged in a parallel relationship for passing a propane refrigerant as a vertical flow and pre-cooling natural gas or cooling a mixed refrigerant for liquefying natural gas, and a thermo siphon drum (33,35,37,39) for the propane refrigerant consisting of a horizontally disposed, laterally elongated tank. Because the passages of the heat exchanger for the natural gas or the mixed refrigerant extend over their entire length in mutually separate relationship, even when the propane refrigerant, the natural gas or the mixed refrigerant is in both gas and liquid phases, a high efficiency of heat transfer can be attained, and the size of the heat exchanger can be reduced. In particular, from an economic view point, it is preferable if the thermo siphon drum serves also as a flash tank.

摘要翻译： 提供了一种改进的用于在天然气液化中的丙烷制冷过程中预冷天然气或用于天然气液化的混合制冷剂的制冷系统。 该系统包括多个板翅式热交换器（31），优选以平行关系布置，用于使作为垂直流的丙烷制冷剂和预冷天然气或冷却用于液化天然气的混合制冷剂，以及热虹吸鼓 （33,35,37,39），用于由水平布置的横向细长的罐组成的丙烷制冷剂。 由于用于天然气或混合制冷剂的热交换器的通道以相互分离的关系在其全长上延伸，所以即使丙烷制冷剂，天然气或混合制冷剂都处于气相和液相两者，高效率 可以实现热传递，并且可以减小热交换器的尺寸。 特别地，从经济的观点来看，优选的是，热虹吸鼓也用作闪蒸罐。

公开(公告)号：EP1782008A4

公开(公告)日：2018-06-20

申请号：EP05760533

申请日：2005-06-10

申请人： EXXONMOBIL UPSTREAM RES CO

发明人： HAWRYSZ DANIEL J ,  STONE JOHN B

IPC分类号： F25J1/02 ,  C10L3/10 ,  F25J3/02

CPC分类号： C10L3/10 ,  B01D53/1406 ,  B01D53/1462 ,  C10L3/102 ,  C10L3/12 ,  E05Y2800/205 ,  F25J1/0022 ,  F25J1/0042 ,  F25J1/0045 ,  F25J1/0052 ,  F25J1/0057 ,  F25J1/0214 ,  F25J1/0242 ,  F25J1/0259 ,  F25J1/027 ,  F25J1/0271 ,  F25J1/0272 ,  F25J1/0274 ,  F25J1/0283 ,  F25J1/0284 ,  F25J1/0294 ,  F25J3/0209 ,  F25J3/0233 ,  F25J3/0242 ,  F25J3/0257 ,  F25J3/029 ,  F25J2200/02 ,  F25J2200/38 ,  F25J2200/70 ,  F25J2200/78 ,  F25J2205/04 ,  F25J2220/62 ,  F25J2220/66 ,  F25J2230/24 ,  F25J2230/60 ,  F25J2235/60 ,  F25J2240/04 ,  F25J2240/30 ,  F25J2240/70 ,  F25J2240/82 ,  F25J2270/12 ,  F25J2270/66 ,  F25J2290/10 ,  F25J2290/40 ,  F25J2290/50 ,  F25J2290/80

摘要： The current invention is related to hydrocarbon fluid processing plants, methods of designing hydrocarbon fluid processing plants, methods of operating hydrocarbon fluid processing plants, and methods of producing hydrocarbon fluids using hydrocarbon fluid processing plants. More particularly, some embodiments of the invention are related to natural gas liquefaction plants, methods of designing natural gas liquefaction plants, methods of operating natural gas liquefaction plants and methods of producing LNG using natural gas liquefaction plants. One embodiment of the invention includes a hydrocarbon fluid processing plant including a plurality of process unit module types, the plurality of process unit module types including at least a first process unit module type including one or more first process unit modules and a second process unit module type including two or more integrated second process unit modules wherein at least one of the first process unit modules and at least one of the second process unit modules are sized at their respective substantially maximum processing efficiency.