PE20060221A1 - LIQUEFIED NATURAL GAS TREATMENT - Google Patents
LIQUEFIED NATURAL GAS TREATMENTInfo
- Publication number
- PE20060221A1 PE20060221A1 PE2005000796A PE2005000796A PE20060221A1 PE 20060221 A1 PE20060221 A1 PE 20060221A1 PE 2005000796 A PE2005000796 A PE 2005000796A PE 2005000796 A PE2005000796 A PE 2005000796A PE 20060221 A1 PE20060221 A1 PE 20060221A1
- Authority
- PE
- Peru
- Prior art keywords
- current
- liquid
- gas
- components
- natural gas
- Prior art date
Links
- 239000003949 liquefied natural gas Substances 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 abstract 4
- 238000009835 boiling Methods 0.000 abstract 3
- 239000012530 fluid Substances 0.000 abstract 2
- 239000002737 fuel gas Substances 0.000 abstract 2
- 238000004064 recycling Methods 0.000 abstract 2
- 238000010992 reflux Methods 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
Classifications
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0257—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of nitrogen
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0209—Natural gas or substitute natural gas
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0233—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
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- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/40—Features relating to the provision of boil-up in the bottom of a column
-
- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/76—Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration cycle
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- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/78—Refluxing the column with a liquid stream originating from an upstream or downstream fractionator column
-
- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
-
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/04—Recovery of liquid products
-
- 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
- F25J2230/60—Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being hydrocarbons or a mixture of hydrocarbons
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- 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
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/60—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being (a mixture of) hydrocarbons
-
- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/30—Dynamic liquid or hydraulic expansion with extraction of work, e.g. single phase or two-phase turbine
-
- 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
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/90—Processes or apparatus involving steps for recycling of process streams the recycled stream being boil-off gas from storage
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/02—Internal refrigeration with liquid vaporising loop
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/04—Internal refrigeration with work-producing gas expansion loop
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/42—Quasi-closed internal or closed external nitrogen refrigeration cycle
-
- 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
- F25J2290/40—Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
-
- 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
- F25J2290/62—Details of storing a fluid in a tank
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (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)
Abstract
SE REFIERE A UN METODO DE TRATAMIENTO DE GAS NATURAL LIQUIDO PARA OBTENER UNA CORRIENTE LIQUIDA CON MENOR CONTENIDO DE COMPONENTES DE MENOR PUNTO DE EBULLICION, QUE INCLUYE: EXPANDIR EL GAS LIQUIDO PARA OBTENER UN FLUIDO DE DOS FASES EXPANDIDO; INTRODUCIR EL FLUIDO DE DOS FASES EN UNA COLUMNA POR DEBAJO DE LA SECCION DE CONTACTO DE GAS-LIQUIDO; RETIRAR DEL FONDO UNA CORRIENTE LIQUIDA CON MENOR CONTENIDO DE COMPONENTES CON MENORES PUNTOS DE EBULLICION; INTRODUCIR LA CORRIENTE EN UN RECIPIENTE DE EXPANSION; RETIRAR DE LA PARTE SUPERIOR DE LA COLUMNA UNA CORRIENTE GASEOSA ENRIQUECIDA EN COMPONENTES CON BAJO PUNTO DE EBULLICION; COMPRIMIR LA CORRIENTE A PRESION DE GAS DE COMBUSTIBLE PARA OBTENER EL GAS COMBUSTIBLE; SEPARAR UNA CORRIENTE DE RECICLADO DEL GAS DE COMBUSTIBLE; CONDENSAR EN PARTE LA CORRIENTE DE RECICLADO PARA OBTENER UNA CORRIENTE DE REFLUJO; E INTRODUCIR LA CORRIENTE DE REFLUJO EN LA COLUMNA POR ENCIMA DE LA SECCION DE CONTACTOREFERS TO A LIQUID NATURAL GAS TREATMENT METHOD TO OBTAIN A LIQUID CURRENT WITH LOWER CONTENT OF LOWER BOILING POINT COMPONENTS, INCLUDING: EXPANDING THE LIQUID GAS TO OBTAIN AN EXPANDED TWO-PHASE FLUID; INTRODUCE THE TWO-PHASE FLUID INTO A COLUMN BELOW THE GAS-LIQUID CONTACT SECTION; WITHDRAWAL FROM THE FUND A LIQUID CURRENT WITH LOWER CONTENT OF COMPONENTS WITH LOWER BOILING POINTS; INTRODUCE THE CURRENT INTO AN EXPANSION VESSEL; REMOVE FROM THE UPPER PART OF THE COLUMN AN ENRICHED GASEOUS CURRENT IN COMPONENTS WITH A LOW BOILING POINT; COMPRESS THE CURRENT TO FUEL GAS PRESSURE TO OBTAIN THE COMBUSTIBLE GAS; SEPARATE A RECYCLING STREAM FROM THE FUEL GAS; CONDENSING IN PART THE RECYCLING CURRENT TO OBTAIN A REFLUX CURRENT; AND INSERT THE REFLUX CURRENT INTO THE COLUMN ABOVE THE CONTACT SECTION
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP04254152 | 2004-07-12 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PE20060221A1 true PE20060221A1 (en) | 2006-05-03 |
Family
ID=34930484
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PE2005000796A PE20060221A1 (en) | 2004-07-12 | 2005-07-08 | LIQUEFIED NATURAL GAS TREATMENT |
| PE2005000795A PE20060219A1 (en) | 2004-07-12 | 2005-07-08 | LIQUEFIED NATURAL GAS TREATMENT |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PE2005000795A PE20060219A1 (en) | 2004-07-12 | 2005-07-08 | LIQUEFIED NATURAL GAS TREATMENT |
Country Status (10)
| Country | Link |
|---|---|
| US (2) | US20080066492A1 (en) |
| EP (2) | EP1766312A1 (en) |
| JP (2) | JP5378681B2 (en) |
| KR (2) | KR101178072B1 (en) |
| AU (2) | AU2005261727B2 (en) |
| BR (2) | BRPI0512693A (en) |
| MY (2) | MY141887A (en) |
| PE (2) | PE20060221A1 (en) |
| RU (3) | RU2392552C1 (en) |
| WO (2) | WO2006005746A1 (en) |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| MY141887A (en) * | 2004-07-12 | 2010-07-16 | Shell Int Research | Treating liquefied natural gas |
| US8522574B2 (en) * | 2008-12-31 | 2013-09-03 | Kellogg Brown & Root Llc | Method for nitrogen rejection and or helium recovery in an LNG liquefaction plant |
| KR20120040700A (en) * | 2009-07-21 | 2012-04-27 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | Method for treating a multi-phase hydrocarbon stream and an apparatus therefor |
| US9823014B2 (en) * | 2011-04-19 | 2017-11-21 | Babcock Ip Management (Number One) Limited | Method of cooling boil off gas and an apparatus therefor |
| JP5679201B2 (en) * | 2011-08-08 | 2015-03-04 | エア・ウォーター株式会社 | Method for removing nitrogen in boil-off gas and nitrogen removing apparatus used therefor |
| RU2474778C1 (en) * | 2011-09-19 | 2013-02-10 | Сергей Николаевич Кузнецов | Heat exchanger for liquefying mixed vapours |
| EP2597406A1 (en) * | 2011-11-25 | 2013-05-29 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for removing nitrogen from a cryogenic hydrocarbon composition |
| MY172968A (en) * | 2011-12-12 | 2019-12-16 | Shell Int Research | Method and apparatus for removing nitrogen from a cryogenic hydrocarbon composition |
| RU2622212C2 (en) * | 2011-12-12 | 2017-06-13 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Method and device for removing nitrogen from cryogenic hydrocarbon composition |
| AU2012354774B2 (en) * | 2011-12-12 | 2015-09-10 | Shell Internationale Research Maatschappij B. V. | Method and apparatus for removing nitrogen from a cryogenic hydrocarbon composition |
| DK2638942T3 (en) * | 2012-03-15 | 2017-01-02 | Cryostar Sas | Fog Separation Device |
| DE102012008961A1 (en) * | 2012-05-03 | 2013-11-07 | Linde Aktiengesellschaft | Process for re-liquefying a methane-rich fraction |
| EP2796818A1 (en) | 2013-04-22 | 2014-10-29 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for producing a liquefied hydrocarbon stream |
| CA2909614C (en) | 2013-04-22 | 2021-02-16 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for producing a liquefied hydrocarbon stream |
| EP2857782A1 (en) | 2013-10-04 | 2015-04-08 | Shell International Research Maatschappij B.V. | Coil wound heat exchanger and method of cooling a process stream |
| US10563913B2 (en) * | 2013-11-15 | 2020-02-18 | Black & Veatch Holding Company | Systems and methods for hydrocarbon refrigeration with a mixed refrigerant cycle |
| EP2957620A1 (en) * | 2014-06-17 | 2015-12-23 | Shell International Research Maatschappij B.V. | Method and system for producing a pressurized and at least partially condensed mixture of hydrocarbons |
| EP2957621A1 (en) | 2014-06-17 | 2015-12-23 | Shell International Research Maatschappij B.V. | De-superheater system and compression system employing such de-superheater system, and method of producing a pressurized and at least partially condensed mixture of hydrocarbons |
| EP2977430A1 (en) * | 2014-07-24 | 2016-01-27 | Shell Internationale Research Maatschappij B.V. | A hydrocarbon condensate stabilizer and a method for producing a stabilized hydrocarbon condenstate stream |
| EP2977431A1 (en) | 2014-07-24 | 2016-01-27 | Shell Internationale Research Maatschappij B.V. | A hydrocarbon condensate stabilizer and a method for producing a stabilized hydrocarbon condenstate stream |
| EP3043133A1 (en) * | 2015-01-12 | 2016-07-13 | Shell Internationale Research Maatschappij B.V. | Method of removing nitrogen from a nitrogen containing stream |
| FR3038964B1 (en) * | 2015-07-13 | 2017-08-18 | Technip France | METHOD FOR RELAXING AND STORING A LIQUEFIED NATURAL GAS CURRENT FROM A NATURAL GAS LIQUEFACTION SYSTEM, AND ASSOCIATED INSTALLATION |
| CN105240064B (en) * | 2015-11-25 | 2017-06-16 | 杰瑞石油天然气工程有限公司 | A kind of LNG energy recovery process |
| RU2626612C2 (en) * | 2015-12-16 | 2017-07-31 | Общество с ограниченной ответственностью "Научно-исследовательский институт природных газов и газовых технологий - Газпром ВНИИГАЗ" | Autonomous plant of liquefied natural gas cleaning (versions) |
| US10330363B2 (en) | 2016-02-08 | 2019-06-25 | Trane International Inc. | Lubricant separator for a heating, ventilation, and air conditioning system |
| EP3517869A1 (en) * | 2018-01-24 | 2019-07-31 | Gas Technology Development Pte Ltd | Process and system for reliquefying boil-off gas (bog) |
| JP7246285B2 (en) * | 2019-08-28 | 2023-03-27 | 東洋エンジニアリング株式会社 | Lean LNG processing method and apparatus |
| US12366408B2 (en) * | 2022-10-14 | 2025-07-22 | Honeywell Lng Llc | Open loop liquefaction process with NGL recovery |
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-
2005
- 2005-07-08 MY MYPI20053134A patent/MY141887A/en unknown
- 2005-07-08 MY MYPI20053135A patent/MY140540A/en unknown
- 2005-07-08 PE PE2005000796A patent/PE20060221A1/en not_active Application Discontinuation
- 2005-07-08 PE PE2005000795A patent/PE20060219A1/en not_active Application Discontinuation
- 2005-07-12 WO PCT/EP2005/053316 patent/WO2006005746A1/en not_active Ceased
- 2005-07-12 EP EP05769936A patent/EP1766312A1/en not_active Withdrawn
- 2005-07-12 JP JP2007520826A patent/JP5378681B2/en not_active Expired - Fee Related
- 2005-07-12 AU AU2005261727A patent/AU2005261727B2/en not_active Expired
- 2005-07-12 BR BRPI0512693-2A patent/BRPI0512693A/en not_active IP Right Cessation
- 2005-07-12 RU RU2009111890/06A patent/RU2392552C1/en active
- 2005-07-12 US US11/632,105 patent/US20080066492A1/en not_active Abandoned
- 2005-07-12 KR KR1020077002375A patent/KR101178072B1/en not_active Expired - Fee Related
- 2005-07-12 US US11/632,137 patent/US20080066493A1/en not_active Abandoned
- 2005-07-12 BR BRPI0512692-4A patent/BRPI0512692A/en not_active IP Right Cessation
- 2005-07-12 KR KR1020077000538A patent/KR101238172B1/en not_active Expired - Fee Related
- 2005-07-12 WO PCT/EP2005/053319 patent/WO2006005748A1/en not_active Ceased
- 2005-07-12 JP JP2007520827A patent/JP5043655B2/en not_active Expired - Fee Related
- 2005-07-12 AU AU2005261729A patent/AU2005261729B2/en not_active Expired
- 2005-07-12 RU RU2007105106/06A patent/RU2362954C2/en active
- 2005-07-12 EP EP05761177A patent/EP1766311A1/en not_active Withdrawn
- 2005-07-12 RU RU2007105107/06A patent/RU2007105107A/en not_active Application Discontinuation
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| Publication number | Publication date |
|---|---|
| US20080066493A1 (en) | 2008-03-20 |
| KR101178072B1 (en) | 2012-08-30 |
| KR20070032003A (en) | 2007-03-20 |
| JP2008506026A (en) | 2008-02-28 |
| EP1766312A1 (en) | 2007-03-28 |
| MY141887A (en) | 2010-07-16 |
| BRPI0512693A (en) | 2008-04-01 |
| US20080066492A1 (en) | 2008-03-20 |
| RU2007105106A (en) | 2008-08-20 |
| MY140540A (en) | 2009-12-31 |
| BRPI0512692A (en) | 2008-04-01 |
| KR101238172B1 (en) | 2013-02-28 |
| RU2362954C2 (en) | 2009-07-27 |
| JP2008506027A (en) | 2008-02-28 |
| JP5043655B2 (en) | 2012-10-10 |
| AU2005261729A1 (en) | 2006-01-19 |
| AU2005261727A1 (en) | 2006-01-19 |
| AU2005261729B2 (en) | 2008-07-17 |
| WO2006005746A1 (en) | 2006-01-19 |
| JP5378681B2 (en) | 2013-12-25 |
| PE20060219A1 (en) | 2006-05-03 |
| AU2005261727B2 (en) | 2008-07-10 |
| RU2392552C1 (en) | 2010-06-20 |
| WO2006005748A1 (en) | 2006-01-19 |
| EP1766311A1 (en) | 2007-03-28 |
| RU2007105107A (en) | 2008-08-20 |
| KR20070034612A (en) | 2007-03-28 |
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