CA1069817A - Procede de recuperation a basse temperature des gaz propanes et hydrocarbures plus lourds en presence dans les debits de gaz naturel - Google Patents

Procede de recuperation a basse temperature des gaz propanes et hydrocarbures plus lourds en presence dans les debits de gaz naturel

Info

Publication number: CA1069817A
Authority: CA; Canada
Prior art keywords: gas; hydrocarbon; condensate; propane; liquid
Prior art date: 1977-01-19
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.): Expired

Application number

CA294,761A

Other languages

English (en)

Inventor

Jerry G. Gulsby

Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Randall Corp

Original Assignee

Randall Corp

Priority date (The priority date 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 date listed.)

1977-01-19

Filing date

1978-01-11

Publication date

1980-01-15

1978-01-11 Application filed by Randall Corp filed Critical Randall Corp

1980-01-15 Application granted granted Critical

1980-01-15 Publication of CA1069817A publication Critical patent/CA1069817A/fr

Status Expired legal-status Critical Current

Links

ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 95
VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 89
229930195733 hydrocarbon Natural products 0.000 title claims abstract description 67
150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 67
239000001294 propane Substances 0.000 title claims abstract description 47
238000000034 method Methods 0.000 title claims abstract description 35
239000003345 natural gas Substances 0.000 title claims abstract description 13
239000007789 gas Substances 0.000 claims abstract description 135
239000004215 Carbon black (E152) Substances 0.000 claims abstract description 48
OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims abstract description 41
239000007788 liquid Substances 0.000 claims abstract description 39
238000010992 reflux Methods 0.000 claims abstract description 19
238000005057 refrigeration Methods 0.000 claims abstract description 18
238000000926 separation method Methods 0.000 claims abstract description 16
238000005194 fractionation Methods 0.000 claims abstract description 6
239000000203 mixture Substances 0.000 claims description 19
238000001816 cooling Methods 0.000 claims description 14
239000000047 product Substances 0.000 claims description 10
239000012263 liquid product Substances 0.000 claims description 6
230000000694 effects Effects 0.000 claims description 5
238000005191 phase separation Methods 0.000 claims description 5
238000010438 heat treatment Methods 0.000 claims 2
239000000112 cooling gas Substances 0.000 claims 1
239000000470 constituent Substances 0.000 abstract description 2
239000000306 component Substances 0.000 description 11
238000011084 recovery Methods 0.000 description 7
IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
VMXUWOKSQNHOCA-UKTHLTGXSA-N ranitidine Chemical compound [O-][N+](=O)\C=C(/NC)NCCSCC1=CC=C(CN(C)C)O1 VMXUWOKSQNHOCA-UKTHLTGXSA-N 0.000 description 4
229910052757 nitrogen Inorganic materials 0.000 description 3
241000196324 Embryophyta Species 0.000 description 2
IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
239000001569 carbon dioxide Substances 0.000 description 2
229910002092 carbon dioxide Inorganic materials 0.000 description 2
150000002500 ions Chemical class 0.000 description 2
NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
241000640882 Condea Species 0.000 description 1
DOMWKUIIPQCAJU-LJHIYBGHSA-N Hydroxyprogesterone caproate Chemical compound C1CC2=CC(=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@@](C(C)=O)(OC(=O)CCCCC)[C@@]1(C)CC2 DOMWKUIIPQCAJU-LJHIYBGHSA-N 0.000 description 1
241001527806 Iti Species 0.000 description 1
101100409194 Rattus norvegicus Ppargc1b gene Proteins 0.000 description 1
HATRDXDCPOXQJX-UHFFFAOYSA-N Thapsigargin Natural products CCCCCCCC(=O)OC1C(OC(O)C(=C/C)C)C(=C2C3OC(=O)C(C)(O)C3(O)C(CC(C)(OC(=O)C)C12)OC(=O)CCC)C HATRDXDCPOXQJX-UHFFFAOYSA-N 0.000 description 1
150000001768 cations Chemical class 0.000 description 1
235000019628 coolness Nutrition 0.000 description 1
230000018044 dehydration Effects 0.000 description 1
238000006297 dehydration reaction Methods 0.000 description 1
238000004880 explosion Methods 0.000 description 1
230000004907 flux Effects 0.000 description 1
ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
239000001282 iso-butane Substances 0.000 description 1
230000004048 modification Effects 0.000 description 1
238000012986 modification Methods 0.000 description 1
229920000136 polysorbate Polymers 0.000 description 1
238000000746 purification Methods 0.000 description 1
239000003507 refrigerant Substances 0.000 description 1
-1 ~a~ural gas~ Chemical compound 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
- 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
- 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
- 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
- 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
- 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
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration

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)
Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Separation By Low-Temperature Treatments (AREA)

CA294,761A 1977-01-19 1978-01-11 Procede de recuperation a basse temperature des gaz propanes et hydrocarbures plus lourds en presence dans les debits de gaz naturel Expired CA1069817A (fr)

Applications Claiming Priority (1)

Application Number	Priority Date	Filing Date	Title
US76051577A	1977-01-19	1977-01-19

Publications (1)

Publication Number	Publication Date
CA1069817A true CA1069817A (fr)	1980-01-15

Family

ID=25059334

Family Applications (1)

Application Number	Title	Priority Date	Filing Date
CA294,761A Expired CA1069817A (fr)	1977-01-19	1978-01-11	Procede de recuperation a basse temperature des gaz propanes et hydrocarbures plus lourds en presence dans les debits de gaz naturel

Country Status (1)

Country	Link
CA (1)	CA1069817A (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
WO2016053668A1 (fr)	2014-09-30	2016-04-07	Dow Global Technologies Llc	Procédé pour augmenter le rendement d'éthylène et de propylène d'une installation de production de propylène

1978
- 1978-01-11 CA CA294,761A patent/CA1069817A/fr not_active Expired

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
WO2016053668A1 (fr)	2014-09-30	2016-04-07	Dow Global Technologies Llc	Procédé pour augmenter le rendement d'éthylène et de propylène d'une installation de production de propylène
US10808999B2 (en)	2014-09-30	2020-10-20	Dow Global Technologies Llc	Process for increasing ethylene and propylene yield from a propylene plant

Legal Events

Date	Code	Title	Description
1997-01-15	MKEX	Expiry

Publication	Publication Date	Title
US4251249A (en)	1981-02-17	Low temperature process for separating propane and heavier hydrocarbons from a natural gas stream
US5953935A (en)	1999-09-21	Ethane recovery process
US4507133A (en)	1985-03-26	Process for LPG recovery
US4687499A (en)	1987-08-18	Process for separating hydrocarbon gas constituents
US5275005A (en)	1994-01-04	Gas processing
US4617039A (en)	1986-10-14	Separating hydrocarbon gases
USRE33408E (en)	1990-10-30	Process for LPG recovery
US5890377A (en)	1999-04-06	Hydrocarbon gas separation process
CA1297913C (fr)	1992-03-24	Procede de recuperation du propane et d'hydro-carbures lourds a partir d'un gaz
US6516631B1 (en)	2003-02-11	Hydrocarbon gas processing
US4718927A (en)	1988-01-12	Process for the separation of C2+ hydrocarbons from natural gas
US6199403B1 (en)	2001-03-13	Process for separating a multi-component pressurizied feed stream using distillation
RU2093765C1 (ru)	1997-10-20	Способ сжижения природного газа
US4061481A (en)	1977-12-06	Natural gas processing
US4203741A (en)	1980-05-20	Separate feed entry to separator-contactor in gas separation
US4456461A (en)	1984-06-26	Separation of low boiling constituents from a mixed gas
US3702541A (en)	1972-11-14	Low temperature method for removing condensable components from hydrocarbon gas
JPS6346366A (ja)	1988-02-27	供給原料ガスの低温分離方法
NO822107L (no)	1983-01-10	Fremgangsmaate for utvinning av kondenserbare hydrokarboner fra hydrokarbonblandinger
EA005990B1 (ru)	2005-08-25	Установка для извлечения газоконденсатных жидкостей
US5402645A (en)	1995-04-04	Liquid product recovery from a hydrocarbon gas stream
EP0161100A2 (fr)	1985-11-13	Procédé de distillation à haute efficacité thermodynamique
US4444577A (en)	1984-04-24	Cryogenic gas processing
US4272269A (en)	1981-06-09	Cryogenic expander recovery process
EP0126309A1 (fr)	1984-11-28	Procédé de récupération des C4-hydrocarbures en utilisant un déphlegmateur