RU2014128347A - Способ удаления кислотных газов из природного газа - Google Patents
Способ удаления кислотных газов из природного газа Download PDFInfo
- Publication number
- RU2014128347A RU2014128347A RU2014128347A RU2014128347A RU2014128347A RU 2014128347 A RU2014128347 A RU 2014128347A RU 2014128347 A RU2014128347 A RU 2014128347A RU 2014128347 A RU2014128347 A RU 2014128347A RU 2014128347 A RU2014128347 A RU 2014128347A
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- RU
- Russia
- Prior art keywords
- carbon dioxide
- pressure
- hydrocarbon
- fraction
- refrigerant
- Prior art date
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- 238000000034 method Methods 0.000 title claims abstract 19
- 239000007789 gas Substances 0.000 title claims abstract 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract 6
- 239000002253 acid Substances 0.000 title claims abstract 3
- 239000003345 natural gas Substances 0.000 title claims abstract 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract 30
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract 14
- 239000001569 carbon dioxide Substances 0.000 claims abstract 14
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract 12
- 238000004821 distillation Methods 0.000 claims abstract 12
- 229930195733 hydrocarbon Natural products 0.000 claims abstract 12
- 239000003507 refrigerant Substances 0.000 claims abstract 12
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract 10
- 238000005057 refrigeration Methods 0.000 claims abstract 7
- 239000007788 liquid Substances 0.000 claims abstract 6
- 238000001816 cooling Methods 0.000 claims abstract 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims abstract 2
- 238000010438 heat treatment Methods 0.000 claims abstract 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims abstract 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims 3
- 238000005406 washing Methods 0.000 claims 2
- 150000001412 amines Chemical class 0.000 claims 1
- 238000009835 boiling Methods 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 230000008020 evaporation Effects 0.000 claims 1
- 239000012528 membrane Substances 0.000 claims 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
- F25J3/0266—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 carbon dioxide
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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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- 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
- 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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- 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
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- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
- F25J3/0635—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
- F25J3/067—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of carbon dioxide
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- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/543—Distillation, fractionation or rectification for separating fractions, components or impurities during preparation or upgrading of a fuel
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- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/545—Washing, scrubbing, stripping, scavenging for separating fractions, components or impurities during preparation or upgrading of a fuel
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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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/548—Membrane- or permeation-treatment for separating fractions, components or impurities during preparation or upgrading of a fuel
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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
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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
- 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
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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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/70—Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
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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
- 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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- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
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- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/40—Processes or apparatus using other separation and/or other processing means using hybrid system, i.e. combining cryogenic and non-cryogenic separation techniques
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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
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- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/50—Processes or apparatus using other separation and/or other processing means using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
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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
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- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/04—Mixing or blending of fluids with the feed stream
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- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/06—Splitting of the feed stream, e.g. for treating or cooling in different ways
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- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
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- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/902—Details about the refrigeration cycle used, e.g. composition of refrigerant, arrangement of compressors or cascade, make up sources, use of reflux exchangers etc.
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Abstract
1. Способ удаления кислотных газов, в частности диоксида углерода и сероводорода, из богатой углеводородом фракции, в частности природного газа, где- богатую углеводородом фракцию (1) охлаждают и частично конденсируют (Е1-Е4), и- получающуюся при этом обогащенную диоксидом углерода жидкую фракцию (5) путем ректификации (Т1) разделяют на богатую диоксидом углерода жидкую фракцию (7) и обедненную диоксидом углерода газовую фракцию (6),отличающийся тем, что- богатую углеводородом фракцию (1) с помощью замкнутого многоступенчатого холодильного цикла, в котором доля диоксида углерода в хладагенте составляет более чем 99,5%, охлаждают (Е1-Е4) до температуры, близкой к температуре тройной точки для диоксида углерода (-56,6°С),- ректификационная колонна (Т1) работает при давлении от 40 до 65 бар, и- обогрев кипятильника (Е5) ректификационной колонны (Т1) осуществляют с помощью конденсирующегося частичного потока хладагента (28) холодильного цикла, давление в котором находится на пригодном для этой цели уровне.2. Способ по п. 1, отличающийся тем, что богатая углеводородом фракция (1) не охлаждается (Е1-Е4) ниже температуры -55°С, предпочтительно -52°С.3. Способ по п. 1 или 2, отличающийся тем, что ректификационная колонна работает при давлении от 50 до 60 бар.4. Способ по п. 1 или 2, отличающийся тем, что охлаждение (Е1-Е4) богатой углеводородом фракции с помощью холодильного цикла происходит исключительно в двухходовых теплообменниках.5. Способ по п. 1 или 2, отличающийся тем, что частичный поток хладагента (28), применяемый для обогрева кипятильника (Е5) ректификационной колонны (Т1), находится под давлением, превышающим рабочее давление в ректификационной колонне (Т1) на величину от 1 до 15 бар, предпочтительно от 3 до 10 бар.6. Способ по п. 1 или 2, от
Claims (10)
1. Способ удаления кислотных газов, в частности диоксида углерода и сероводорода, из богатой углеводородом фракции, в частности природного газа, где
- богатую углеводородом фракцию (1) охлаждают и частично конденсируют (Е1-Е4), и
- получающуюся при этом обогащенную диоксидом углерода жидкую фракцию (5) путем ректификации (Т1) разделяют на богатую диоксидом углерода жидкую фракцию (7) и обедненную диоксидом углерода газовую фракцию (6),
отличающийся тем, что
- богатую углеводородом фракцию (1) с помощью замкнутого многоступенчатого холодильного цикла, в котором доля диоксида углерода в хладагенте составляет более чем 99,5%, охлаждают (Е1-Е4) до температуры, близкой к температуре тройной точки для диоксида углерода (-56,6°С),
- ректификационная колонна (Т1) работает при давлении от 40 до 65 бар, и
- обогрев кипятильника (Е5) ректификационной колонны (Т1) осуществляют с помощью конденсирующегося частичного потока хладагента (28) холодильного цикла, давление в котором находится на пригодном для этой цели уровне.
2. Способ по п. 1, отличающийся тем, что богатая углеводородом фракция (1) не охлаждается (Е1-Е4) ниже температуры -55°С, предпочтительно -52°С.
3. Способ по п. 1 или 2, отличающийся тем, что ректификационная колонна работает при давлении от 50 до 60 бар.
4. Способ по п. 1 или 2, отличающийся тем, что охлаждение (Е1-Е4) богатой углеводородом фракции с помощью холодильного цикла происходит исключительно в двухходовых теплообменниках.
5. Способ по п. 1 или 2, отличающийся тем, что частичный поток хладагента (28), применяемый для обогрева кипятильника (Е5) ректификационной колонны (Т1), находится под давлением, превышающим рабочее давление в ректификационной колонне (Т1) на величину от 1 до 15 бар, предпочтительно от 3 до 10 бар.
6. Способ по п. 1 или 2, отличающийся тем, что полученная путем ректификации (Т1), богатая диоксидом углерода жидкая фракция (7) применяется для охлаждения сжатого хладагента, при этом для того, чтобы избежать (частичного) испарения этой жидкой фракции (7), ее давление после используемого для охлаждения теплообменника (Е14) повышают до значения, превышающего давление в точке кипения (Р2).
7. Способ по п. 1 или 2, отличающийся тем, что по меньшей мере один боковой кипятильник (Е8) ректификационной колонны (Т1) обогревают с помощью частичного потока хладагента (29) холодильного цикла, давление в котором находится на необходимом для этой цели уровне, где это давление по меньшей мере на 8 бар, предпочтительно на 12 бар лежит ниже давления в проходящем через кипятильник (Е5) частичном потоке хладагента (28).
8. Способ по п. 1 или 2, где богатую углеводородом фракцию (1) до ее охлаждения (Е1-Е4) подвергают сушке (А), отличающийся тем, что богатую углеводородом фракцию перед этой сушкой предварительно охлаждают частичным потоком хладагента (30) холодильного цикла.
9. Способ по п. 1 или 2, отличающийся тем, что отводимый из работающего при самом низком уровне температур теплообменника (Е4) частичный поток хладагента (27) перед его испарением (С1) подогревают (Е7).
10. Способ по п. 1 или 2, отличающийся тем, что полученную при частичной конденсации обедненную диоксидом углерода газовую фракцию (3) подают на последующий процесс удаления диоксида углерода, предпочтительно на мембранный процесс, процесс аминной промывки и/или промывки метанолом.
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WO2017051021A1 (en) | 2015-09-24 | 2017-03-30 | Linde Aktiengesellschaft | Method for cooling, liquefying or processing a gas and corresponding refrigerant mixture |
US10173389B2 (en) * | 2015-12-15 | 2019-01-08 | Bloom Energy Corporation | Carbon dioxide shielded natural gas line and method of using thereof |
CN105571269B (zh) * | 2015-12-16 | 2017-10-27 | 中国海洋石油总公司 | 含高氮氧氢的煤层气低温精馏液化分离回收***及方法 |
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US5983663A (en) * | 1998-05-08 | 1999-11-16 | Kvaerner Process Systems, Inc. | Acid gas fractionation |
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