CO5090917A1 - Remocion de aromaticos y/o pesados a partir de una alimenta- cion basada en metano por condensacion y destilacion de despojo - Google Patents
Remocion de aromaticos y/o pesados a partir de una alimenta- cion basada en metano por condensacion y destilacion de despojoInfo
- Publication number
- CO5090917A1 CO5090917A1 CO97015904A CO97015904A CO5090917A1 CO 5090917 A1 CO5090917 A1 CO 5090917A1 CO 97015904 A CO97015904 A CO 97015904A CO 97015904 A CO97015904 A CO 97015904A CO 5090917 A1 CO5090917 A1 CO 5090917A1
- Authority
- CO
- Colombia
- Prior art keywords
- heavy
- stream
- rich
- methane
- column
- Prior art date
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title abstract 14
- 238000009833 condensation Methods 0.000 title abstract 2
- 230000005494 condensation Effects 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 abstract 5
- 238000004821 distillation Methods 0.000 abstract 4
- 230000002051 biphasic effect Effects 0.000 abstract 3
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 230000002787 reinforcement Effects 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
- F25J3/0242—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 3 carbon atoms 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
- 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
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- 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
- F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
- F25J1/0032—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
- F25J1/004—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by flash gas recovery
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- 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
- F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
- F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
- F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F25J1/0209—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 using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle in combination with an internal quasi-closed refrigeration loop, e.g. with deep flash recycle loop as at least a three level refrigeration cascade
- F25J1/021—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 using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle in combination with an internal quasi-closed refrigeration loop, e.g. with deep flash recycle loop as at least a three level refrigeration cascade using a deep flash recycle loop
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- F25J1/0237—Heat exchange integration integrating refrigeration provided for liquefaction and purification/treatment of the gas to be liquefied, e.g. heavy hydrocarbon removal from natural gas
- F25J1/0238—Purification or treatment step is integrated within one refrigeration cycle only, i.e. the same or single refrigeration cycle provides feed gas cooling (if present) and overhead gas cooling
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- 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
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- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
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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
- 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
- F25J1/0244—Operation; Control and regulation; Instrumentation
- F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
- F25J1/0247—Different modes, i.e. 'runs', of operation; Process control start-up of the process
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- 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
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- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
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- F25J1/0264—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
- F25J1/0265—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams comprising cores associated exclusively with the cooling of a refrigerant stream, e.g. for auto-refrigeration or economizer
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- 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
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- 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
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- 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
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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
- F25J2280/00—Control of the process or apparatus
- F25J2280/02—Control in general, load changes, different modes ("runs"), measurements
-
- 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
- F25J2280/00—Control of the process or apparatus
- F25J2280/10—Control for or during start-up and cooling down of the installation
-
- 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
- F25J2290/34—Details about subcooling of liquids
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Treating Waste Gases (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/621,923 US5669238A (en) | 1996-03-26 | 1996-03-26 | Heat exchanger controls for low temperature fluids |
US08/659,732 US5737940A (en) | 1996-06-07 | 1996-06-07 | Aromatics and/or heavies removal from a methane-based feed by condensation and stripping |
Publications (1)
Publication Number | Publication Date |
---|---|
CO5090917A1 true CO5090917A1 (es) | 2001-10-30 |
Family
ID=27089093
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CO97015904A CO5090917A1 (es) | 1996-03-26 | 1997-03-31 | Remocion de aromaticos y/o pesados a partir de una alimenta- cion basada en metano por condensacion y destilacion de despojo |
Country Status (15)
Country | Link |
---|---|
JP (1) | JP4612122B2 (de) |
AR (1) | AR006440A1 (de) |
AU (1) | AU707336B2 (de) |
CA (1) | CA2250123C (de) |
CO (1) | CO5090917A1 (de) |
EA (1) | EA000800B1 (de) |
ID (1) | ID17331A (de) |
IN (1) | IN191375B (de) |
MY (1) | MY123833A (de) |
NO (1) | NO309397B1 (de) |
OA (1) | OA11014A (de) |
SA (1) | SA97180452B1 (de) |
TR (1) | TR199801906T2 (de) |
TW (1) | TW426665B (de) |
WO (1) | WO1997036139A1 (de) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7310971B2 (en) * | 2004-10-25 | 2007-12-25 | Conocophillips Company | LNG system employing optimized heat exchangers to provide liquid reflux stream |
US7484385B2 (en) | 2003-01-16 | 2009-02-03 | Lummus Technology Inc. | Multiple reflux stream hydrocarbon recovery process |
US6742357B1 (en) * | 2003-03-18 | 2004-06-01 | Air Products And Chemicals, Inc. | Integrated multiple-loop refrigeration process for gas liquefaction |
CN100565061C (zh) * | 2003-10-30 | 2009-12-02 | 弗劳尔科技公司 | 柔性液态天然气工艺和方法 |
US7866184B2 (en) | 2004-06-16 | 2011-01-11 | Conocophillips Company | Semi-closed loop LNG process |
US20070012072A1 (en) * | 2005-07-12 | 2007-01-18 | Wesley Qualls | Lng facility with integrated ngl extraction technology for enhanced ngl recovery and product flexibility |
DE102005050388A1 (de) * | 2005-10-20 | 2007-04-26 | Linde Ag | Rückgewinnungssystem für die Weiterverarbeitung eines Spaltgasstroms einer Ethylenanlage |
US8127938B2 (en) | 2009-03-31 | 2012-03-06 | Uop Llc | Apparatus and process for treating a hydrocarbon stream |
AP3423A (en) * | 2009-09-30 | 2015-09-30 | Shell Int Research | Method fo fractionating a hydrocarbon stream an apparatus therefor |
WO2013028363A1 (en) | 2011-08-10 | 2013-02-28 | Conocophillips Company | Liquefied natural gas plant with ethylene independent heavies recovery system |
KR102367522B1 (ko) * | 2014-03-14 | 2022-02-25 | 루머스 테크놀로지 엘엘씨 | 액화 전 희박 천연 가스로부터의 중질 탄화수소 제거를 위한 공정 및 장비 |
DE102015002164A1 (de) * | 2015-02-19 | 2016-08-25 | Linde Aktiengesellschaft | Verfahren zum Verflüssigen von Erdgas |
KR102291922B1 (ko) * | 2015-04-28 | 2021-08-20 | 대우조선해양 주식회사 | 천연가스를 이용하여 중질탄화수소를 생산하는 flng 및 flng에서 천연가스를 이용하여 중질탄화수소를 생산하는 방법 |
US11402155B2 (en) | 2016-09-06 | 2022-08-02 | Lummus Technology Inc. | Pretreatment of natural gas prior to liquefaction |
US11473837B2 (en) * | 2018-08-31 | 2022-10-18 | Uop Llc | Gas subcooled process conversion to recycle split vapor for recovery of ethane and propane |
US10894929B1 (en) | 2019-10-02 | 2021-01-19 | Saudi Arabian Oil Company | Natural gas liquids recovery process |
CN115317947B (zh) * | 2022-08-30 | 2023-08-11 | 山东神驰石化有限公司 | 一种丙烯生产用高效精馏塔 |
US11905480B1 (en) | 2022-10-20 | 2024-02-20 | Saudi Arabian Oil Company | Enhancing H2S specification in NGL products |
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US3407052A (en) * | 1966-08-17 | 1968-10-22 | Conch Int Methane Ltd | Natural gas liquefaction with controlled b.t.u. content |
US3413816A (en) * | 1966-09-07 | 1968-12-03 | Phillips Petroleum Co | Liquefaction of natural gas |
BE758567A (fr) * | 1969-11-07 | 1971-05-06 | Fluor Corp | Procede de recuperation d'ethylene a basse pression |
US4142876A (en) * | 1975-05-22 | 1979-03-06 | Phillips Petroleum Company | Recovery of natural gas liquids by partial condensation |
US4318723A (en) * | 1979-11-14 | 1982-03-09 | Koch Process Systems, Inc. | Cryogenic distillative separation of acid gases from methane |
FR2471567B1 (fr) * | 1979-12-12 | 1986-11-28 | Technip Cie | Procede et systeme de refrigeration d'un fluide a refroidir a basse temperature |
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 |
SU1075065A1 (ru) * | 1982-02-01 | 1984-02-23 | Всесоюзный научно-исследовательский институт природных газов | Способ разделени жирных углеводородных газов |
US4410342A (en) * | 1982-05-24 | 1983-10-18 | United States Riley Corporation | Method and apparatus for separating a liquid product from a hydrocarbon-containing gas |
US4445916A (en) * | 1982-08-30 | 1984-05-01 | Newton Charles L | Process for liquefying methane |
US4559070A (en) * | 1984-01-03 | 1985-12-17 | Marathon Oil Company | Process for devolatilizing natural gas liquids |
DE3408997A1 (de) * | 1984-03-12 | 1985-09-12 | Linde Ag, 6200 Wiesbaden | Verfahren zum abtrennen schwerer komponenten aus verfluessigten gasen |
SU1259083A1 (ru) * | 1985-03-26 | 1986-09-23 | Всесоюзный Научно-Исследовательский И Проектный Институт По Переработке Газа | Способ переработки нефт ных газов |
US5170630A (en) * | 1991-06-24 | 1992-12-15 | The Boc Group, Inc. | Process and apparatus for producing nitrogen of ultra-high purity |
FR2681859B1 (fr) * | 1991-09-30 | 1994-02-11 | Technip Cie Fse Etudes Const | Procede de liquefaction de gaz naturel. |
JP3328749B2 (ja) * | 1992-12-11 | 2002-09-30 | 日本酸素株式会社 | 低沸点不純物を含むガスの液化方法及び装置 |
-
1997
- 1997-03-19 WO PCT/US1997/004397 patent/WO1997036139A1/en active IP Right Grant
- 1997-03-19 AU AU23351/97A patent/AU707336B2/en not_active Expired
- 1997-03-19 TR TR1998/01906T patent/TR199801906T2/xx unknown
- 1997-03-19 EA EA199800856A patent/EA000800B1/ru not_active IP Right Cessation
- 1997-03-19 CA CA002250123A patent/CA2250123C/en not_active Expired - Lifetime
- 1997-03-19 JP JP53448697A patent/JP4612122B2/ja not_active Expired - Fee Related
- 1997-03-21 IN IN518CA1997 patent/IN191375B/en unknown
- 1997-03-25 MY MYPI97001277A patent/MY123833A/en unknown
- 1997-03-26 AR ARP970101258A patent/AR006440A1/es active IP Right Grant
- 1997-03-26 ID IDP970998A patent/ID17331A/id unknown
- 1997-03-31 CO CO97015904A patent/CO5090917A1/es unknown
- 1997-05-22 TW TW086106889A patent/TW426665B/zh not_active IP Right Cessation
- 1997-09-29 SA SA97180452A patent/SA97180452B1/ar unknown
-
1998
- 1998-09-25 OA OA9800178A patent/OA11014A/en unknown
- 1998-09-25 NO NO984488A patent/NO309397B1/no not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
CA2250123C (en) | 2004-01-27 |
TW426665B (en) | 2001-03-21 |
OA11014A (en) | 2003-03-06 |
CA2250123A1 (en) | 1997-10-02 |
JP2000512724A (ja) | 2000-09-26 |
JP4612122B2 (ja) | 2011-01-12 |
SA97180452B1 (ar) | 2006-10-30 |
TR199801906T2 (xx) | 1999-01-18 |
AU2335197A (en) | 1997-10-17 |
AR006440A1 (es) | 1999-08-25 |
IN191375B (de) | 2003-11-29 |
ID17331A (id) | 1997-12-18 |
MY123833A (en) | 2006-06-30 |
NO984488D0 (no) | 1998-09-25 |
EA199800856A1 (ru) | 1999-04-29 |
EA000800B1 (ru) | 2000-04-24 |
WO1997036139A1 (en) | 1997-10-02 |
NO309397B1 (no) | 2001-01-22 |
NO984488L (no) | 1998-11-26 |
AU707336B2 (en) | 1999-07-08 |
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