JP2009542881A - 炭化水素流の液化方法及び装置 - Google Patents
炭化水素流の液化方法及び装置 Download PDFInfo
- Publication number
- JP2009542881A JP2009542881A JP2009518861A JP2009518861A JP2009542881A JP 2009542881 A JP2009542881 A JP 2009542881A JP 2009518861 A JP2009518861 A JP 2009518861A JP 2009518861 A JP2009518861 A JP 2009518861A JP 2009542881 A JP2009542881 A JP 2009542881A
- Authority
- JP
- Japan
- Prior art keywords
- point
- hydrocarbon stream
- removal
- treated
- stream
- 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.)
- Pending
Links
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 89
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 89
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 81
- 238000000034 method Methods 0.000 title claims abstract description 32
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000003345 natural gas Substances 0.000 claims abstract description 27
- 239000003507 refrigerant Substances 0.000 claims description 24
- 239000003949 liquefied natural gas Substances 0.000 description 18
- 239000007789 gas Substances 0.000 description 9
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 8
- 238000011084 recovery Methods 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000005194 fractionation Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 239000003915 liquefied petroleum gas Substances 0.000 description 4
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 4
- 229910052753 mercury Inorganic materials 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001294 propane Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- -1 H 2 O Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
- F25J1/0277—Offshore use, e.g. during shipping
- F25J1/0278—Unit being stationary, e.g. on floating barge or fixed platform
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. natural gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/64—Separating heavy hydrocarbons, e.g. NGL, LPG, C4+ hydrocarbons or heavy condensates in general
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/30—Compression of the feed stream
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/12—Particular process parameters like pressure, temperature, ratios
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/60—Details about pipelines, i.e. network, for feed or product distribution
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Ocean & Marine Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
【解決手段】(a)沿岸にある第一地点(2)に炭化水素流(10)を供給する工程、(b)第一地点(2)の炭化水素流(10)を処理して、処理炭化水素流(20)を得る工程、(c)処理炭化水素流(20)を、海上にある第二地点(3)に2km以上に亘ってパイプライン経由で輸送する工程、(d)第二地点(3)の処理炭化水素流(20)を液化して、大気圧で液化炭化水素製品(50)を得る工程を含む、天然ガスのような炭化水素流の液化方法、及び第一地点にあって、処理炭化水素流を得るための1つ以上の処理ユニット(11,12,13,14,18,19);海上である第二地点にあって、液化炭化水素製品を大気圧で製造するための1つ以上の液化プラント(21);処理炭化水素流を2km以上の距離に亘って第二地点に輸送するためのパイプラインを備えた炭化水素流の液化装置。
【選択図】図1
Description
本発明の別の目的は、特に北極圏で遭遇するような極寒条件下での天然ガス流のような炭化水素流の代替液化方法を提供することである。
(a)沿岸にある第一地点に炭化水素流を供給する工程、
(b)第一地点の炭化水素流を処理して、処理炭化水素流を得る工程、
(c)処理炭化水素流を、海上にある第二地点に2km以上に亘ってパイプライン経由で輸送する工程、
(d)第二地点の処理炭化水素流を液化して、大気圧で液化炭化水素製品を得る工程、
を少なくとも含む。
第一地点及び第二地点は、単一のプロセス又は処理ユニットだけ含むように制限されず、むしろ1つ以上のプロセスユニットを含むプラント用地を含むように意図される。第一地点及び第二地点は、互いに2km以上、好ましくは5km以上、更に好ましくは10km以上距離がある。この距離は、1000kmを超えてもよいが、好ましくは900km未満である。
供給源によっては、天然ガスは、メタンより重質の炭化水素、例えばエタン、プロパン、ブタン及びペンタン並びに幾つかの芳香族炭化水素を変化量で含有する。天然ガスは、その他、H2O,N2,CO2,H2S,その他の硫黄化合物等のような非炭化水素も含有してよい。
更に工程(b)の処理は、水銀(Hg)の除去を含むことが好ましい。
沿岸である第一地点にあって、処理炭化水素流を得るための1つ以上の処理ユニット;
海上である第二地点にあって、液化炭化水素製品を大気圧で製造するための1つ以上の液化プラント;
処理炭化水素流を2km以上の距離に亘って第二地点(3)に輸送するためのパイプライン;
を少なくとも備える。
以下に本発明を非限定的図面により説明する。
図1は、天然ガスのような炭化水素流の処理及び液化用工程計画(包括的に符号1で示す)の概略図である。
図2は、スクラブ塔18及び分留ユニット19を第一地点2に配置した本発明の代りの実施態様を示す。この実施態様では処理流20は、パイプライン4経由で第二地点3に送られる前に既に液化に好適である。したがって、第二地点3で処理を行う必要はない。
当業者は、本発明の範囲を逸脱することなく、多くの改変を行ってよいことを理解している。
2 沿岸の第一地点
3 海上の第二地点
4 パイプライン
10 炭化水素流
11 処理ユニット
12 処理ユニット
13 処理ユニット
14 処理ユニット
18 処理ユニット
19 処理ユニット
20 処理炭化水素流
50 液化炭化水素製品
Claims (16)
- (a)沿岸にある第一地点(2)に炭化水素流(10)を供給する工程、
(b)第一地点(2)の炭化水素流(10)を処理して、処理炭化水素流(20)を得る工程、
(c)処理炭化水素流(20)を、海上にある第二地点(3)に2km以上に亘ってパイプライン経由で輸送する工程、
(d)第二地点(3)の処理炭化水素流(20)を液化して、大気圧で液化炭化水素製品(50)を得る工程、
を少なくとも含む、天然ガスのような炭化水素流の液化方法。 - 工程(b)での処理が、CO2の除去、好ましくは処理済炭化水素流(20)中のCO2含有量が500ppm未満、更に好ましくは200ppm未満、なお更に好ましくは50ppm未満となるようなCO2の除去を少なくとも含む請求項1に記載の方法。
- 第二地点(3)ではCO2の除去は行わない請求項2に記載の方法。
- 工程(b)での処理が、H2Oの除去、好ましくは処理済炭化水素流(20)中のH2O含有量が100ppm未満、更に好ましくは10ppm未満、なお更に好ましくは1ppm未満となるようなH2Oの除去を少なくとも含む請求項1〜3のいずれか1項以上に記載の方法。
- 処理済炭化水素流(20)が、工程(c)の輸送前に、好ましくは50バールを超え、更に好ましくは60バールを超え、なお更に好ましくは70バールを超える圧力に圧縮される請求項1〜4のいずれか1項以上に記載の方法。
- 処理炭化水素流(20)が、ほぼ臨界点を超える状態で輸送される請求項1〜5のいずれか1項以上に記載の方法。
- 処理炭化水素流(20)が、輸送中、周囲との熱交換により冷却される請求項1〜6のいずれか1項以上に記載の方法。
- 処理炭化水素流(20)が、第二地点(3)に着く前に、<10℃、好ましくは<0℃、更に好ましくは<−10℃の温度に冷却される請求項7に記載の方法。
- 液化炭化水素製品(50)が、輸送され、再ガス化される請求項1〜8のいずれか1項以上に記載の方法。
- 工程(d)で冷媒が使用され、該冷媒は、第二地点以外の異なる地点で製造され、パイプライン経由で第二地点に供給される請求項1〜9のいずれか1項に記載の方法。
- 沿岸である第一地点(2)にあって、処理炭化水素流(20)を得るための1つ以上の処理ユニット(11,12,13,14,18,19,...);
海上である第二地点(3)にあって、液化炭化水素製品(50)を大気圧で製造するための1つ以上の液化プラント(21);
処理炭化水素流(20)を2km以上の距離に亘って第二地点(3)に輸送するためのパイプライン(4);
を少なくとも備えた、天然ガス流のような炭化水素流(10)の液化装置(1)。 - 第一地点(2)の処理ユニット(11,12,13,14,18,19,...)の1つが、CO2の除去用に適応される請求項11に記載の装置(1)。
- 第二地点(3)では、処理炭化水素流(20)からのCO2除去は行わない請求項11又は12に記載の装置(1)。
- 第一地点(2)の処理ユニット(11,12,13,14,18,19,...)の1つが、H2Oの除去用に適応される請求項11〜13のいずれか1項に記載の装置(1)。
- 第一地点(2)の処理済炭化水素流(20)を、好ましくは40バールを超え、更に好ましくは50バールを超え、なお更に好ましくは60バールを超える圧力に圧縮するための圧縮器(17)を更に備える請求項11〜14のいずれか1項以上に記載の装置(1)。
- パイプライン(4)が実質的に熱絶縁されていない請求項11〜15のいずれか1項以上に記載の装置(1)。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06117142 | 2006-07-13 | ||
PCT/EP2007/056929 WO2008006788A2 (en) | 2006-07-13 | 2007-07-09 | Method and apparatus for liquefying a hydrocarbon stream |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2009542881A true JP2009542881A (ja) | 2009-12-03 |
Family
ID=37678890
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2009518861A Pending JP2009542881A (ja) | 2006-07-13 | 2007-07-09 | 炭化水素流の液化方法及び装置 |
JP2009518882A Abandoned JP2009542882A (ja) | 2006-07-13 | 2007-07-11 | 天然ガス流の液化方法及び装置 |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2009518882A Abandoned JP2009542882A (ja) | 2006-07-13 | 2007-07-11 | 天然ガス流の液化方法及び装置 |
Country Status (10)
Country | Link |
---|---|
US (2) | US20100000251A1 (ja) |
EP (2) | EP2047194A2 (ja) |
JP (2) | JP2009542881A (ja) |
KR (2) | KR20090028829A (ja) |
CN (1) | CN101490490A (ja) |
AU (2) | AU2007274367B2 (ja) |
BR (1) | BRPI0713628A2 (ja) |
NO (1) | NO20090697L (ja) |
RU (1) | RU2009145096A (ja) |
WO (2) | WO2008006788A2 (ja) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013172416A1 (ja) * | 2012-05-16 | 2013-11-21 | 石油資源開発株式会社 | 天然ガスの生産方法及び生産システム |
JP2016532846A (ja) * | 2013-07-31 | 2016-10-20 | ゼネラル・エレクトリック・カンパニイ | 液化天然ガス生成のためのシステム及び組み込みプロセス |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2928719A1 (fr) * | 2008-03-11 | 2009-09-18 | Total Sa Sa | Procede segmente de production de gaz naturel liquefie. |
US8876960B2 (en) * | 2009-09-16 | 2014-11-04 | Chevron U.S.A Inc. | Method and system for transporting and processing sour fluids |
US8454727B2 (en) | 2010-05-28 | 2013-06-04 | Uop Llc | Treatment of natural gas feeds |
US8388732B2 (en) | 2010-06-25 | 2013-03-05 | Uop Llc | Integrated membrane and adsorption system for carbon dioxide removal from natural gas |
US8282707B2 (en) | 2010-06-30 | 2012-10-09 | Uop Llc | Natural gas purification system |
US20120047942A1 (en) * | 2010-08-30 | 2012-03-01 | Chevron U.S.A. Inc. | METHOD, SYSTEM, AND PRODUCTION AND STORAGE FACILITY FOR OFFSHORE LPG and LNG PROCESSING OF ASSOCIATED GASES |
EP2439255A1 (en) * | 2010-10-05 | 2012-04-11 | Shell Internationale Research Maatschappij B.V. | Method and system for producing a contaminant-depleted gas stream |
EP2749830A1 (en) | 2012-12-27 | 2014-07-02 | Shell Internationale Research Maatschappij B.V. | Method for the manufacture of conditioned ethane and an apparatus therefor |
JP6208847B2 (ja) * | 2013-04-12 | 2017-10-04 | エクセラレート・リケファクション・ソリューションズ・エルエルシイ | 浮き埠頭で天然ガスを液化するシステムおよび方法 |
KR102372754B1 (ko) * | 2015-05-15 | 2022-03-10 | 대우조선해양 주식회사 | 천연가스의 이산화탄소 제거 방법 |
US10072889B2 (en) * | 2015-06-24 | 2018-09-11 | General Electric Company | Liquefaction system using a turboexpander |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09100478A (ja) * | 1995-10-03 | 1997-04-15 | Mitsubishi Heavy Ind Ltd | 高圧天然ガス中の高濃度炭酸ガスを除去する方法 |
WO2006052392A2 (en) * | 2004-11-05 | 2006-05-18 | Exxonmobil Upstream Research Company | Lng transportation vessel and method for transporting hydrocarbons |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3498077A (en) * | 1968-02-26 | 1970-03-03 | Us Navy | Atmospheric water recovery method and means |
US4025321A (en) * | 1975-09-30 | 1977-05-24 | Union Carbide Corporation | Purification of natural gas streams containing oxygen |
DE2616594C2 (de) * | 1976-04-14 | 1981-10-29 | Mannesmann AG, 4000 Düsseldorf | Verfahren und Anlage zum Rohrleitungstransport von Erdgas durch arktische Gebiete |
GB2106623B (en) * | 1981-06-19 | 1984-11-07 | British Gas Corp | Liquifaction and storage of gas |
NO161941C (no) * | 1987-06-25 | 1991-04-30 | Kvaerner Eng | Fremgangsmaate ved og anlegg for transport av hydrokarboner over lang avstand fra en hydrokarbonkilde til havs. |
DE4223160C2 (de) * | 1992-07-10 | 1998-02-12 | Mannesmann Ag | Verfahren und Anlage zur Verdichtung von Gas |
US5325673A (en) * | 1993-02-23 | 1994-07-05 | The M. W. Kellogg Company | Natural gas liquefaction pretreatment process |
AUPM485694A0 (en) * | 1994-04-05 | 1994-04-28 | Bhp Petroleum Pty. Ltd. | Liquefaction process |
NO180469B1 (no) * | 1994-12-08 | 1997-05-12 | Statoil Petroleum As | Fremgangsmåte og system for fremstilling av flytendegjort naturgass til havs |
NO179986C (no) * | 1994-12-08 | 1997-01-22 | Norske Stats Oljeselskap | Fremgangsmåte og system for fremstilling av flytendegjort naturgass til havs |
RU2141084C1 (ru) * | 1995-10-05 | 1999-11-10 | Би Эйч Пи Петролеум ПТИ. Лтд. | Установка для сжижения |
TW396254B (en) * | 1997-06-20 | 2000-07-01 | Exxon Production Research Co | Pipeline distribution network systems for transportation of liquefied natural gas |
MY115506A (en) * | 1998-10-23 | 2003-06-30 | Exxon Production Research Co | Refrigeration process for liquefaction of natural gas. |
US6460721B2 (en) * | 1999-03-23 | 2002-10-08 | Exxonmobil Upstream Research Company | Systems and methods for producing and storing pressurized liquefied natural gas |
US6298671B1 (en) * | 2000-06-14 | 2001-10-09 | Bp Amoco Corporation | Method for producing, transporting, offloading, storing and distributing natural gas to a marketplace |
US6584781B2 (en) * | 2000-09-05 | 2003-07-01 | Enersea Transport, Llc | Methods and apparatus for compressed gas |
FR2814378B1 (fr) * | 2000-09-26 | 2002-10-31 | Inst Francais Du Petrole | Procede de pretraitement d'un gaz naturel contenant des gaz acides |
MY129091A (en) * | 2001-09-07 | 2007-03-30 | Exxonmobil Upstream Res Co | Acid gas disposal method |
GB2398276B (en) * | 2001-12-14 | 2005-05-04 | Shell Int Research | Floating hydrocarbon treating plant |
FR2841330B1 (fr) * | 2002-06-21 | 2005-01-28 | Inst Francais Du Petrole | Liquefaction de gaz naturel avec recyclage de gaz naturel |
US6694774B1 (en) * | 2003-02-04 | 2004-02-24 | Praxair Technology, Inc. | Gas liquefaction method using natural gas and mixed gas refrigeration |
US7360367B2 (en) * | 2004-07-18 | 2008-04-22 | Wood Group Advanced Parts Manufacture | Apparatus for cryogenic fluids having floating liquefaction unit and floating regasification unit connected by shuttle vessel, and cryogenic fluid methods |
WO2005090152A1 (en) * | 2004-03-23 | 2005-09-29 | Single Buoy Moorings Inc. | Field development with centralised power generation unit |
US7223298B2 (en) * | 2005-03-17 | 2007-05-29 | Pgr Filters, L.L.C. | Filter assembly for pipelines |
WO2007064209A1 (en) * | 2005-12-01 | 2007-06-07 | Single Buoy Moorings Inc. | Hydrocarbon liquefaction system and method |
-
2007
- 2007-07-09 RU RU2009145096/06A patent/RU2009145096A/ru not_active Application Discontinuation
- 2007-07-09 WO PCT/EP2007/056929 patent/WO2008006788A2/en active Application Filing
- 2007-07-09 JP JP2009518861A patent/JP2009542881A/ja active Pending
- 2007-07-09 AU AU2007274367A patent/AU2007274367B2/en not_active Ceased
- 2007-07-09 US US12/373,107 patent/US20100000251A1/en not_active Abandoned
- 2007-07-09 EP EP07787211A patent/EP2047194A2/en not_active Withdrawn
- 2007-07-09 KR KR1020097002654A patent/KR20090028829A/ko not_active Application Discontinuation
- 2007-07-11 EP EP07787343A patent/EP2041506A2/en not_active Withdrawn
- 2007-07-11 CN CNA2007800264775A patent/CN101490490A/zh active Pending
- 2007-07-11 BR BRPI0713628-5A patent/BRPI0713628A2/pt not_active IP Right Cessation
- 2007-07-11 KR KR1020097002655A patent/KR20090028651A/ko not_active Application Discontinuation
- 2007-07-11 JP JP2009518882A patent/JP2009542882A/ja not_active Abandoned
- 2007-07-11 US US12/373,099 patent/US20090205365A1/en not_active Abandoned
- 2007-07-11 WO PCT/EP2007/057069 patent/WO2008006842A2/en active Application Filing
- 2007-07-11 AU AU2007274331A patent/AU2007274331A1/en not_active Abandoned
-
2009
- 2009-02-12 NO NO20090697A patent/NO20090697L/no not_active Application Discontinuation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09100478A (ja) * | 1995-10-03 | 1997-04-15 | Mitsubishi Heavy Ind Ltd | 高圧天然ガス中の高濃度炭酸ガスを除去する方法 |
WO2006052392A2 (en) * | 2004-11-05 | 2006-05-18 | Exxonmobil Upstream Research Company | Lng transportation vessel and method for transporting hydrocarbons |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013172416A1 (ja) * | 2012-05-16 | 2013-11-21 | 石油資源開発株式会社 | 天然ガスの生産方法及び生産システム |
CN104334829A (zh) * | 2012-05-16 | 2015-02-04 | 石油资源开发株式会社 | 天然气的生产方法及生产系统 |
US9417008B2 (en) | 2012-05-16 | 2016-08-16 | Japan Petroleum Exploration Co., Ltd. | Production method and production system for natural gas |
EA027637B1 (ru) * | 2012-05-16 | 2017-08-31 | Джапан Петролеум Эксплорейшн Ко., Лтд. | Способ переработки и система переработки природного газа |
JP2016532846A (ja) * | 2013-07-31 | 2016-10-20 | ゼネラル・エレクトリック・カンパニイ | 液化天然ガス生成のためのシステム及び組み込みプロセス |
JP2020003203A (ja) * | 2013-07-31 | 2020-01-09 | ゼネラル・エレクトリック・カンパニイ | 液化天然ガス生成のためのシステム及び組み込みプロセス |
Also Published As
Publication number | Publication date |
---|---|
WO2008006788A2 (en) | 2008-01-17 |
AU2007274367A1 (en) | 2008-01-17 |
US20090205365A1 (en) | 2009-08-20 |
BRPI0713628A2 (pt) | 2012-10-23 |
CN101490490A (zh) | 2009-07-22 |
JP2009542882A (ja) | 2009-12-03 |
AU2007274367B2 (en) | 2010-07-29 |
WO2008006788A3 (en) | 2008-10-30 |
WO2008006842A3 (en) | 2008-11-27 |
EP2047194A2 (en) | 2009-04-15 |
NO20090697L (no) | 2009-02-12 |
EP2041506A2 (en) | 2009-04-01 |
WO2008006842A2 (en) | 2008-01-17 |
RU2009145096A (ru) | 2011-06-10 |
KR20090028829A (ko) | 2009-03-19 |
KR20090028651A (ko) | 2009-03-18 |
AU2007274331A1 (en) | 2008-01-17 |
US20100000251A1 (en) | 2010-01-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2009542881A (ja) | 炭化水素流の液化方法及び装置 | |
US20200248871A1 (en) | Method of Purging a Dual Purpose LNG/LIN Storage Tank | |
KR102137940B1 (ko) | 액화 질소를 사용하여 액화 천연 가스로부터 질소를 분리하기 위한 방법 및 시스템 | |
CN108369060B (zh) | 用液氮增强的基于膨胀器的lng生产方法 | |
US9459042B2 (en) | Method of producing a gasified hydrocarbon stream; method of liquefying a gaseous hydrocarbon stream; and a cyclic process | |
KR101145303B1 (ko) | Lng fpso용 천연가스 액화방법 및 장치 | |
WO2009007439A2 (en) | Method and apparatus for liquefying a gaseous hydrocarbon stream | |
WO2000025060A1 (en) | Refrigeration process for liquefaction of natural gas | |
JP2008539282A (ja) | 天然ガス流の液化方法及び装置 | |
US11402152B2 (en) | Large scale coastal liquefaction | |
KR20210024629A (ko) | 유일한 냉매로서 액화 가스를 이용한 공기 냉각식 대규모 부유식 lng 생산을 위한 방법 | |
JP2009540080A (ja) | 炭化水素流の処理方法及び処理装置 | |
Choi | LNG for petroleum engineers | |
Amin et al. | The Cryocell: an advanced gas sweetening technology | |
Ostovar et al. | Small-Scale Liquefied Natural Gas–Opportunities and Challenges | |
NL2005419C2 (en) | Method and apparatus for liquefying a natural gas stream. | |
EP2439255A1 (en) | Method and system for producing a contaminant-depleted gas stream | |
Teles et al. | Evaluation of Floating Liquefied Natural Gas Units for Brazilian Scenarios |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20100702 |
|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20100802 |
|
RD04 | Notification of resignation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7424 Effective date: 20100825 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20130312 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20130820 |