JP2008513726A - Lpgおよび熱電併給の構成および方法 - Google Patents
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Abstract
Description
Claims (22)
- 希薄LNGと、エタンおよびLPGの少なくとも1種を製造するためのLNG分留プラントであって、
分留カラムに結合され、カラム頂部を部分的に凝縮して還流を生成し、希薄蒸気を完全に凝縮して希薄LNG凝縮物を形成するように構成された熱交換器と、
気化された高濃度LNGの加圧された超臨界の過熱部分の減衰を用い、それによってエネルギーとカラムへの分解蒸気流を生成する膨張器によって駆動されるエネルギー発生器とを含む、LNG分留プラント。 - 希薄LNG凝縮物からの残留冷能を用いてエネルギーサイクルの作動流体を凝縮するランキンエネルギーサイクルに結合される、請求項1に記載のLNG分留プラント。
- 希薄LNGをパイプライン圧力にポンプ加圧するように構成されたポンプをさらに含む、請求項1に記載のLNG分留プラント。
- エネルギーサイクル中の作動流体が、窒素、メタン、エタン、プロパン、ブタン、およびペンタンの少なくとも1種を含む、多成分流体を含む、請求項2に記載のLNG分留プラント。
- 加熱された高濃度LNGを液体部分と蒸気部分に分離する分離器をさらに含む、請求項1に記載のLNG分留プラント。
- 加熱された高濃度LNGの液体部分をポンプ加圧し、それによって気化した高濃度LNGの加圧された超臨界部分を形成するポンプをさらに含む、請求項5に記載のLNG分留プラント。
- 加熱された高濃度LNGの加圧された超臨界部分を加熱し、それによって高濃度LNGの加圧された超臨界および過熱された部分を形成する熱源をさらに含む、請求項6に記載のLNG分留プラント。
- 熱源が、高濃度LNGの膨張された超臨界の過熱された部分によって、分留器の必要とする分解と加熱の少なくとも一部を提供するように構成される、請求項7に記載のLNG分留プラント。
- 高濃度LNGの加熱され加圧された液体部分を受容して膨張された原料を形成し、それによって電気的エネルギーを発生する膨張器によって駆動されるエネルギー発生器と、
膨張された原料および加熱された高濃度LNGの蒸気部分を受容し、それによってエタンおよびLPGの少なくとも1種、および頂部希薄蒸気を生成する分留器と、
頂部希薄蒸気の少なくとも一部を少なくとも部分的に凝縮するように構成された第1熱交換器と、
頂部希薄蒸気から、還流として分留器にポンプ送給される液体部分と、凝縮されて希薄LNG凝縮物を形成する蒸気部分とに分離する還流分離器と、
ポンプが希薄LNG凝縮物を受容しパイプライン圧力に加圧するように構成された第2熱交換器上流のポンプとを含む、プラント。 - 第1熱交換器が、頂部希薄蒸気を部分的に凝縮し還流分離器蒸気を完全に凝縮する冷媒として高濃度LNGを用いるように構成される、請求項9に記載のプラント。
- 第2熱交換器が、エネルギーサイクルの作動流体からの凝縮デューティを用い、それによって加圧された希薄LNG凝縮物を再ガス化するように構成される、請求項9に記載のプラント。
- 加熱された高濃度LNGの加圧された超臨界部分を加熱し、それによって高濃度LNGの加熱され加圧された超臨界部分を形成する第3熱交換器をさらに含む、請求項9に記載のプラント。
- 第3熱交換器が、高濃度LNGの加熱され加圧された液体部分によって、分留器の必要とする分解と加熱の少なくとも一部を提供するように構成される、請求項12に記載のプラント。
- 高濃度LNGの液体部分を加圧および加熱し、加圧され加熱された部分を膨張させ、それによってエネルギーを発生し、膨張した部分を分留器に供給するステップと、
高濃度LNGの蒸気部分を分留器に送り、それによってエタンおよびLPGの少なくとも1種、および頂部希薄蒸気を生成するステップと、
高濃度LNGの冷却容量を用いて、頂部蒸気を希薄蒸気および希薄液体へ少なくとも部分的に凝縮するステップと、
希薄液体を分留器への還流としてポンプ送給し、希薄蒸気をさらに凝縮して希薄LNG凝縮物を形成するステップと、
希薄LNGをパイプライン圧力までポンプ加圧し、エネルギーサイクルを運転する作動流体の凝縮デューティを用いて熱交換器中で希薄LNG凝縮物を気化するステップとを含む、プラントの運転方法。 - 加熱された高濃度LNGを蒸気部分と液体部分に分離し、それによって高濃度LNGの液体部分を形成するステップをさらに含む、請求項14に記載の方法。
- カラム頂部蒸気を少なくとも部分的に凝縮するステップが、(1)カラム頂部蒸気を冷却するステップと、(2)冷却された生成物の蒸気部分を液体部分から分離するステップと、(3)エタンおよび/またはLPG回収を改善するために、カラムへの還流としてポンプ送給すべき冷却された生成物の液体部分を分離するステップと、(4)分離された蒸気部分をさらに冷却し、それによって希薄LNG凝縮物を形成するステップとを含む、請求項14に記載の方法。
- ステップ(1)および(2)および(4)が高濃度LNGの冷却容量を利用する、請求項16に記載の方法。
- 高濃度LNGの液体部分の加熱ステップが、高濃度LNGの加熱され加圧された超臨界部分によって、分留器の必要とする分解と加熱の少なくとも一部を提供する、請求項14に記載の方法。
- 凝縮されたLNG頂部生成物を気化するステップの前に、凝縮されたLNG頂部生成物をパイプライン圧力まで加圧するステップをさらに含む、請求項14に記載の方法。
- 作動流体が、メタン、エタン、プロパン、ブタン、およびペンタンの少なくとも1種を含む多成分流体を含む、請求項14に記載の方法。
- 少なくとも95%のプロパンが回収される、請求項14に記載の方法。
- 少なくとも75%のエタンが回収される、請求項14に記載の方法。
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US61247304P | 2004-09-22 | 2004-09-22 | |
US60/612,473 | 2004-09-22 | ||
PCT/US2005/031005 WO2006036441A1 (en) | 2004-09-22 | 2005-08-30 | Configurations and methods for lpg and power cogeneration |
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JP (1) | JP4901740B2 (ja) |
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JP2019219062A (ja) * | 2018-06-15 | 2019-12-26 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 天然ガスの製造装置および天然ガスの製造方法 |
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Publication number | Priority date | Publication date | Assignee | Title |
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EP1824583A4 (en) * | 2004-12-16 | 2011-07-27 | Fluor Tech Corp | DESIGNS AND METHODS FOR LNG REGASIFICATION AND BTU CONTROL |
EP2032921A2 (en) * | 2006-06-27 | 2009-03-11 | Fluor Technologies Corporation | Ethane recovery methods and configurations |
CA2552327C (en) | 2006-07-13 | 2014-04-15 | Mackenzie Millar | Method for selective extraction of natural gas liquids from "rich" natural gas |
US9470452B2 (en) * | 2006-07-27 | 2016-10-18 | Cosmodyne, LLC | Imported LNG treatment |
US8132411B2 (en) * | 2008-11-06 | 2012-03-13 | Air Products And Chemicals, Inc. | Rankine cycle for LNG vaporization/power generation process |
CN101832157A (zh) * | 2010-03-08 | 2010-09-15 | 翁志远 | 一种使用低温液体做工质的热机发电技术 |
CA2763081C (en) | 2011-12-20 | 2019-08-13 | Jose Lourenco | Method to produce liquefied natural gas (lng) at midstream natural gas liquids (ngls) recovery plants. |
CA2772479C (en) | 2012-03-21 | 2020-01-07 | Mackenzie Millar | Temperature controlled method to liquefy gas and a production plant using the method. |
CA2790961C (en) | 2012-05-11 | 2019-09-03 | Jose Lourenco | A method to recover lpg and condensates from refineries fuel gas streams. |
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WO2016053668A1 (en) | 2014-09-30 | 2016-04-07 | Dow Global Technologies Llc | Process for increasing ethylene and propylene yield from a propylene plant |
WO2016130574A1 (en) | 2015-02-09 | 2016-08-18 | Fluor Technologies Corporation | Methods and configuration of an ngl recovery process for low pressure rich feed gas |
PL413001A1 (pl) * | 2015-07-06 | 2017-01-16 | Tadeusz Bąk | Sposób regazyfikacji skroplonego gazu ziemnego oraz system regazyfikacji skroplonego gazu ziemnego |
CN105065901B (zh) * | 2015-08-14 | 2017-04-19 | 中国石油化工股份有限公司青岛安全工程研究院 | 用于液化天然气接收站的轻烃回收工艺 |
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CN112324530B (zh) * | 2020-11-02 | 2022-07-19 | 江苏科技大学 | 船用lng冷能利用冷电联供系统 |
RU2758364C1 (ru) * | 2021-03-10 | 2021-10-28 | Андрей Владиславович Курочкин | Способ реконструкции установки низкотемпературной сепарации газа для получения сжиженного природного газа (варианты) |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5572616A (en) * | 1978-11-25 | 1980-05-31 | Mitsui Eng & Shipbuild Co Ltd | Low-temperature heat utilizing device for liquefied natural gas |
JPS55123306A (en) * | 1979-03-14 | 1980-09-22 | Chiyoda Chem Eng & Constr Co Ltd | Vaporization of liquefied natural gas and its energy recovering method |
JPS5773299A (en) * | 1980-10-24 | 1982-05-07 | Kobe Steel Ltd | Gasification of liquefied natural gas |
JPS5822872A (ja) * | 1981-07-31 | 1983-02-10 | 東洋エンジニアリング株式会社 | 天燃ガス中のlpg回収方法 |
JPS58152128A (ja) * | 1982-03-04 | 1983-09-09 | Ishikawajima Harima Heavy Ind Co Ltd | 液化天然ガスの冷熱利用発電方法 |
JPS60205166A (ja) * | 1984-03-30 | 1985-10-16 | 石川島播磨重工業株式会社 | 液化天然ガス冷熱発電設備の再生ガス液化方法 |
JPS63163770A (ja) * | 1986-12-19 | 1988-07-07 | ザ エム.ダブリュ.ケロッグ カンパニー | 高圧ガス流の分離方法 |
JPH08269468A (ja) * | 1995-03-30 | 1996-10-15 | Osaka Gas Co Ltd | 分留機能付き液化天然ガス気化設備 |
JP2000186886A (ja) * | 1998-12-21 | 2000-07-04 | Mitsubishi Heavy Ind Ltd | 液化天然ガスの分離装置並びに分離方法、発電方法及び液化天然ガスの使用方法 |
JP2004150687A (ja) * | 2002-10-30 | 2004-05-27 | Mitsubishi Heavy Ind Ltd | 液化天然ガスの分離装置燃焼排ガス |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3394555A (en) * | 1964-11-10 | 1968-07-30 | Mc Donnell Douglas Corp | Power-refrigeration system utilizing waste heat |
US3837172A (en) * | 1972-06-19 | 1974-09-24 | Synergistic Services Inc | Processing liquefied natural gas to deliver methane-enriched gas at high pressure |
GB1444176A (en) * | 1972-11-17 | 1976-07-28 | Garwin L | Isotopically enriched helium - 4 |
DE2523672C3 (de) * | 1975-05-28 | 1980-03-20 | Gutehoffnungshuette Sterkrade Ag, 4200 Oberhausen | Einrichtung zur Verdampfung von verflüssigtem Erdgas mit Hilfe einer Gasturbinenanlage mit geschlossenem Kreislauf |
JPS5491648A (en) * | 1977-12-29 | 1979-07-20 | Toyokichi Nozawa | Lnggfleon generation system |
DE3172221D1 (en) * | 1980-07-01 | 1985-10-17 | Costain Petrocarbon | Producing power from a cryogenic liquid |
US4444015A (en) * | 1981-01-27 | 1984-04-24 | Chiyoda Chemical Engineering & Construction Co., Ltd. | Method for recovering power according to a cascaded Rankine cycle by gasifying liquefied natural gas and utilizing the cold potential |
US4551979A (en) * | 1981-05-11 | 1985-11-12 | Soma Kurtis | Method and apparatus for a thermodynamic cycle by use of distillation |
US5114451A (en) * | 1990-03-12 | 1992-05-19 | Elcor Corporation | Liquefied natural gas processing |
US5295350A (en) * | 1992-06-26 | 1994-03-22 | Texaco Inc. | Combined power cycle with liquefied natural gas (LNG) and synthesis or fuel gas |
US5615561A (en) * | 1994-11-08 | 1997-04-01 | Williams Field Services Company | LNG production in cryogenic natural gas processing plants |
AU699635B2 (en) * | 1996-02-29 | 1998-12-10 | Shell Internationale Research Maatschappij B.V. | Reducing the amount of components having low boiling points in liquefied natural gas |
US5944984A (en) * | 1996-03-20 | 1999-08-31 | Ormat Industries Ltd. | Solvent deasphalting unit and method for using the same |
US5890377A (en) * | 1997-11-04 | 1999-04-06 | Abb Randall Corporation | Hydrocarbon gas separation process |
TW432192B (en) * | 1998-03-27 | 2001-05-01 | Exxon Production Research Co | Producing power from pressurized liquefied natural gas |
US6233938B1 (en) * | 1998-07-14 | 2001-05-22 | Helios Energy Technologies, Inc. | Rankine cycle and working fluid therefor |
US6367286B1 (en) * | 2000-11-01 | 2002-04-09 | Black & Veatch Pritchard, Inc. | System and process for liquefying high pressure natural gas |
FR2818365B1 (fr) * | 2000-12-18 | 2003-02-07 | Technip Cie | Procede de refrigeration d'un gaz liquefie, gaz obtenus par ce procede, et installation mettant en oeuvre celui-ci |
WO2002097252A1 (en) * | 2001-05-30 | 2002-12-05 | Conoco Inc. | Lng regasification process and system |
US6564579B1 (en) * | 2002-05-13 | 2003-05-20 | Black & Veatch Pritchard Inc. | Method for vaporizing and recovery of natural gas liquids from liquefied natural gas |
US6945075B2 (en) * | 2002-10-23 | 2005-09-20 | Elkcorp | Natural gas liquefaction |
US7143606B2 (en) * | 2002-11-01 | 2006-12-05 | L'air Liquide-Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etide Et L'exploitation Des Procedes Georges Claude | Combined air separation natural gas liquefaction plant |
US6751959B1 (en) * | 2002-12-09 | 2004-06-22 | Tennessee Valley Authority | Simple and compact low-temperature power cycle |
US7278281B2 (en) * | 2003-11-13 | 2007-10-09 | Foster Wheeler Usa Corporation | Method and apparatus for reducing C2 and C3 at LNG receiving terminals |
US8132411B2 (en) * | 2008-11-06 | 2012-03-13 | Air Products And Chemicals, Inc. | Rankine cycle for LNG vaporization/power generation process |
-
2005
- 2005-08-30 EA EA200700700A patent/EA010641B1/ru not_active IP Right Cessation
- 2005-08-30 AU AU2005290036A patent/AU2005290036B2/en not_active Ceased
- 2005-08-30 JP JP2007532355A patent/JP4901740B2/ja not_active Expired - Fee Related
- 2005-08-30 EP EP05793897A patent/EP1792129A1/en not_active Withdrawn
- 2005-08-30 MX MX2007003102A patent/MX2007003102A/es active IP Right Grant
- 2005-08-30 CA CA2578471A patent/CA2578471C/en not_active Expired - Fee Related
- 2005-08-30 WO PCT/US2005/031005 patent/WO2006036441A1/en active Application Filing
- 2005-08-30 CN CN2005800320723A patent/CN101027526B/zh not_active Expired - Fee Related
- 2005-08-30 US US11/574,271 patent/US8065890B2/en not_active Expired - Fee Related
-
2007
- 2007-03-16 NO NO20071425A patent/NO20071425L/no not_active Application Discontinuation
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5572616A (en) * | 1978-11-25 | 1980-05-31 | Mitsui Eng & Shipbuild Co Ltd | Low-temperature heat utilizing device for liquefied natural gas |
JPS55123306A (en) * | 1979-03-14 | 1980-09-22 | Chiyoda Chem Eng & Constr Co Ltd | Vaporization of liquefied natural gas and its energy recovering method |
JPS5773299A (en) * | 1980-10-24 | 1982-05-07 | Kobe Steel Ltd | Gasification of liquefied natural gas |
JPS5822872A (ja) * | 1981-07-31 | 1983-02-10 | 東洋エンジニアリング株式会社 | 天燃ガス中のlpg回収方法 |
JPS58152128A (ja) * | 1982-03-04 | 1983-09-09 | Ishikawajima Harima Heavy Ind Co Ltd | 液化天然ガスの冷熱利用発電方法 |
JPS60205166A (ja) * | 1984-03-30 | 1985-10-16 | 石川島播磨重工業株式会社 | 液化天然ガス冷熱発電設備の再生ガス液化方法 |
JPS63163770A (ja) * | 1986-12-19 | 1988-07-07 | ザ エム.ダブリュ.ケロッグ カンパニー | 高圧ガス流の分離方法 |
JPH08269468A (ja) * | 1995-03-30 | 1996-10-15 | Osaka Gas Co Ltd | 分留機能付き液化天然ガス気化設備 |
JP2000186886A (ja) * | 1998-12-21 | 2000-07-04 | Mitsubishi Heavy Ind Ltd | 液化天然ガスの分離装置並びに分離方法、発電方法及び液化天然ガスの使用方法 |
JP2004150687A (ja) * | 2002-10-30 | 2004-05-27 | Mitsubishi Heavy Ind Ltd | 液化天然ガスの分離装置燃焼排ガス |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2019219062A (ja) * | 2018-06-15 | 2019-12-26 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 天然ガスの製造装置および天然ガスの製造方法 |
JP7084219B2 (ja) | 2018-06-15 | 2022-06-14 | レール・リキード-ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 天然ガスの製造装置および天然ガスの製造方法 |
Also Published As
Publication number | Publication date |
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EA010641B1 (ru) | 2008-10-30 |
MX2007003102A (es) | 2007-05-16 |
US8065890B2 (en) | 2011-11-29 |
JP4901740B2 (ja) | 2012-03-21 |
US20080190135A1 (en) | 2008-08-14 |
NO20071425L (no) | 2007-04-20 |
CN101027526A (zh) | 2007-08-29 |
AU2005290036B2 (en) | 2008-06-12 |
CA2578471C (en) | 2010-09-21 |
WO2006036441A1 (en) | 2006-04-06 |
EA200700700A1 (ru) | 2007-10-26 |
AU2005290036A1 (en) | 2006-04-06 |
CA2578471A1 (en) | 2006-04-06 |
EP1792129A1 (en) | 2007-06-06 |
CN101027526B (zh) | 2010-12-08 |
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