EA201171266A1 - Криогенная система для удаления кислотных газов из потока углеводородного газа и способ удаления кислотных газов - Google Patents
Криогенная система для удаления кислотных газов из потока углеводородного газа и способ удаления кислотных газовInfo
- Publication number
- EA201171266A1 EA201171266A1 EA201171266A EA201171266A EA201171266A1 EA 201171266 A1 EA201171266 A1 EA 201171266A1 EA 201171266 A EA201171266 A EA 201171266A EA 201171266 A EA201171266 A EA 201171266A EA 201171266 A1 EA201171266 A1 EA 201171266A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- removal
- distillation column
- acid
- molecular sieve
- sieve layer
- Prior art date
Links
- 239000007789 gas Substances 0.000 title abstract 8
- 239000002253 acid Substances 0.000 title abstract 5
- 239000004215 Carbon black (E152) Substances 0.000 title 1
- 229930195733 hydrocarbon Natural products 0.000 title 1
- 150000002430 hydrocarbons Chemical class 0.000 title 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 8
- 238000004821 distillation Methods 0.000 abstract 5
- 239000002808 molecular sieve Substances 0.000 abstract 4
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 abstract 4
- 238000001816 cooling Methods 0.000 abstract 1
- 230000002262 irrigation Effects 0.000 abstract 1
- 238000003973 irrigation Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000011144 upstream manufacturing Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
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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
- F25J3/0209—Natural gas or substitute natural gas
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
- C10L3/101—Removal of contaminants
- C10L3/102—Removal of contaminants of acid contaminants
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Engineering & Computer Science (AREA)
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- Separation By Low-Temperature Treatments (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
Система для удаления кислотных газов из исходного газового потока, которая включает в себя криогенную дистилляционную колонну. Данная колонна принимает и разделяет исходный газовый поток на верхний метановый поток и нижний поток сжиженного кислотного газа. Охлаждающее оборудование ниже по ходу от криогенной дистилляционной колонны охлаждает верхний метановый поток и возвращает часть верхнего метанового потока в криогенную дистилляционную колонну в виде жидкого орошения. Данная система также может включать в себя первый слой молекулярного сита выше по ходу от дистилляционной колонны и второй слой молекулярного сита ниже по ходу от дистилляционной колонны. Первый слой молекулярного сита адсорбирует воду, тогда как второй слой молекулярного сита адсорбирует дополнительные кислотные газы из охлажденного верхнего метанового потока.
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US17091909P | 2009-04-20 | 2009-04-20 | |
PCT/US2010/021785 WO2010123598A1 (en) | 2009-04-20 | 2010-01-22 | Cryogenic system for removing acid gases from a hyrdrocarbon gas stream, and method of removing acid gases |
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EA201171266A1 true EA201171266A1 (ru) | 2012-03-30 |
EA021006B1 EA021006B1 (ru) | 2015-03-31 |
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EA201171266A EA021006B1 (ru) | 2009-04-20 | 2010-01-22 | Способ удаления кислотных газов из потока углеводородного газа |
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US (1) | US9423174B2 (ru) |
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CA (1) | CA2759037C (ru) |
EA (1) | EA021006B1 (ru) |
MX (1) | MX2011010404A (ru) |
MY (1) | MY155414A (ru) |
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WO (1) | WO2010123598A1 (ru) |
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- 2010-01-22 CN CN201080017582.4A patent/CN102405275B/zh not_active Expired - Fee Related
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CN102405275B (zh) | 2015-01-14 |
EP2421942B1 (en) | 2014-06-18 |
US20120031144A1 (en) | 2012-02-09 |
JP5632455B2 (ja) | 2014-11-26 |
WO2010123598A1 (en) | 2010-10-28 |
JP2012524231A (ja) | 2012-10-11 |
EP2421942A1 (en) | 2012-02-29 |
MY155414A (en) | 2015-10-15 |
SG174865A1 (en) | 2011-11-28 |
CA2759037C (en) | 2018-09-25 |
MX2011010404A (es) | 2011-10-24 |
AU2010239718A1 (en) | 2011-11-10 |
US9423174B2 (en) | 2016-08-23 |
CN102405275A (zh) | 2012-04-04 |
AU2010239718B2 (en) | 2016-02-04 |
EP2421942A4 (en) | 2013-05-22 |
EA021006B1 (ru) | 2015-03-31 |
CA2759037A1 (en) | 2010-10-28 |
BRPI1014038A2 (pt) | 2016-04-12 |
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