RU2016134819A - Способ и система для обработки текучей среды обратного притока, выходящей с площадки скважины - Google Patents

Способ и система для обработки текучей среды обратного притока, выходящей с площадки скважины Download PDF

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RU2016134819A
RU2016134819A RU2016134819A RU2016134819A RU2016134819A RU 2016134819 A RU2016134819 A RU 2016134819A RU 2016134819 A RU2016134819 A RU 2016134819A RU 2016134819 A RU2016134819 A RU 2016134819A RU 2016134819 A RU2016134819 A RU 2016134819A
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stream
carbon
carbon dioxide
rich
liquid
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RU2016134819A
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RU2016134819A3 (ru
RU2687600C2 (ru
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Кеннет Л. БУРГЕРЗ
Рэймонд Ф. ДРНЕВИЧ
Миниш М. ШАХ
Дэвид Р. ТОМПСОН
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Праксайр Текнолоджи, Инк.
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
    • 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
    • C—CHEMISTRY; METALLURGY
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    • 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
    • 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
    • C10L3/104—Carbon dioxide
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/164—Injecting CO2 or carbonated water
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34—Arrangements for separating materials produced by the well
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34—Arrangements for separating materials produced by the well
    • E21B43/35—Arrangements for separating materials produced by the well specially adapted for separating solids
    • 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
    • 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
    • F25J3/0266—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
    • 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
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/0605—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 feed stream
    • F25J3/061—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
    • F25J3/06—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
    • 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
    • F25J3/06—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
    • 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
    • C10L2290/02—Combustion or pyrolysis
    • 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
    • C10L2290/06—Heat exchange, direct or indirect
    • 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
    • C10L2290/48—Expanders, e.g. throttles or flash tanks
    • 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
    • C10L2290/543—Distillation, fractionation or rectification for separating fractions, components or impurities during preparation or upgrading of a fuel
    • 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
    • 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
    • C10L2290/56—Specific details of the apparatus for preparation or upgrading of a fuel
    • C10L2290/567—Mobile or displaceable apparatus
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/25—Methods for stimulating production
    • E21B43/26—Methods for stimulating production by forming crevices or fractures
    • E21B43/2605—Methods for stimulating production by forming crevices or fractures using gas or liquefied gas
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
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    • E21B43/40—Separation associated with re-injection of separated materials
    • 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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    • 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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    • F25J2205/80—Processes or apparatus using other separation and/or other processing means using membrane, i.e. including a permeation step
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    • F25J2270/00—Refrigeration techniques used
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    • F25J2270/00—Refrigeration techniques used
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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
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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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Claims (29)

1. Способ обработки текучей среды обратного притока, выходящей с площадки скважины после стимуляции подземного пласта, включающий:
обработку текучей среды обратного притока, выходящей с площадки скважины, и разделение текучей среды обратного притока на богатый углекислым газом поток и обедненный углекислым газом поток, при этом богатый углекислым газом поток далее обрабатывается для образования жидкого продукта углекислого газа, в то время как обедненный углекислым газом поток используется в обработке ниже по потоку, чтобы способствовать образованию указанного жидкого продукта углекислого газа;
продолжение разделения текучей среды обратного притока на богатый углекислым газом поток и обедненный углекислым газом поток, до тех пор, пока концентрация углекислого газа в газе обратного притока не уменьшится до значения, выбранного в диапазоне примерно 50-80 мол.% концентрации углекислого газа, после чего поток обратного притока с пониженной концентрацией углекислого газа продолжает разделяться на богатый углекислым газом поток, который сбрасывается или направляется на факел, и на богатые углеводородами потоки продукта.

2. Способ по п.1, дополнительно включающий в себя предварительную обработку текучей среды обратного притока перед разделением.

3. Способ по п.2, в котором в процессе предварительной обработки удаляется любое из перечисленного: вода, твердые частицы, жидкие углеводороды, сероводород или их сочетание.

4. Способ по п.1, дополнительно включающий в себя: направление богатого углекислым газом потока в установку охлаждения, где богатый углекислым газом поток охлаждается до температуры в диапазоне от примерно -40°F до +5°F (от -40°С до -15°С).

5. Способ по п.4, дополнительно включающий в себя: понижение давления на богатом углекислом газе потоке, выходящем из установки охлаждения, до давления, находящегося в диапазоне 60-500 фунт/кв. дюйм изб. (0,4-3,4 МПа изб.), и температуры, находящейся в диапазоне примерно от -70°F до 20°F (от -56,7°С до -6,7°С).

6. Способ по п.5, дополнительно включающий в себя: разделение богатого углекислым газом потока при давлении в диапазоне 60-500 фунт/кв. дюйм изб. (0,4-3,4 МПа изб.), на первый жидкий поток преимущественно углекислого газа и первый газообразный поток, обогащенный метаном.

7. Способ по п.6, дополнительно включающий в себя: нагревание первого жидкого потока преимущественно углекислого газа и осуществление дополнительного разделения на второй поток жидкого продукта углекислого газа, дополнительно обедненный метаном, и второй газофазный поток, обогащенный метаном.

8. Способ по п.7, дополнительно включающий в себя: использование одного или обоих из первого и второго газофазных потоков, обогащенных метаном, вместе с обедненным углекислым газом потоком в установке охлаждения.

9. Способ по п.1, в котором текучая среда обратного притока, имеющая концентрацию примерно 95 мол.% и более углекислого газа, направляется в установку охлаждения, без предварительного разделения на богатый углекислым газом поток и обедненный углекислым газом поток.

10. Способ обработки текучей среды обратного притока с площадки скважины при осуществлении работы в двух режимах, включающий в себя:
обработку газа обратного притока, выходящего с площадки скважины, при которой в первом режиме газ обратного притока разделяется на богатый углекислым газом поток и обедненный углекислым газом поток, и богатый углекислым газом поток далее обрабатывается и используется для образования жидкого продукта углекислого газа, в то время как обедненный углекислым газом поток необязательно используется в другой части процесса или, в другом случае, сжигается на факеле до тех пор, пока уровень концентрации углекислого газа в текучей среде обратного притока, выходящей с площадки скважины, не уменьшится до заданного значения в диапазоне примерно 50-80 мол.%; и
после этого переключение во второй режим, в котором текучая среда обратного притока разделяется на богатый углекислым газом поток, и богатый углекислым газом поток сбрасывается или направляется на факел, тогда как обедненный углекислым газом поток, богатый углеводородами, извлекается в виде газообразных и жидких продуктов.

11. Система обработки текучей среды обратного притока, выходящей с площадки скважины после стимуляции подземного пласта, включает в себя:
установку предварительной обработки для приема и обработки текучей среды обратного притока с площадки скважины и для удаления любого из перечисленного: воды, твердых частиц, жидких углеводородов, сероводорода или их сочетания;
мембранную установку ниже по потоку от установки предварительной обработки для приема из нее предварительно обработанной текучей среды обратного притока и разделения предварительно обработанной текучей среды обратного притока на богатый углекислым газом поток пермеата и обедненный углекислым газом поток ретентата;
установку охлаждения пермеата для приема богатого углекислым газом потока пермеата и понижения температуры потока до значения, находящегося в диапазоне от примерно -40°F до 20°F (от -40°С до -6,7°С); и
фазовый сепаратор для приема охлажденного богатого углекислым газом потока пермеата из установки охлаждения пермеата и разделения потока на первый жидкий поток преимущественно углекислого газа и первый газообразный поток, обогащенный метаном.

12. Система по п.11, дополнительно содержащая второй фазовый сепаратор для приема первого жидкого потока преимущественно углекислого газа и дополнительного разделения на второй поток жидкого продукта углекислого газа и второй газофазный поток, обогащенный метаном.

13. Система по п.11, дополнительно содержащая клапан понижения давления, расположенный между установкой охлаждения и фазовым сепаратором, для снижения давления к диапазону примерно 60-500 фунт/кв. дюйм изб. (0,4-3,4 МПа изб.), и понижения температуры богатого углекислым газом потока пермеата.

14. Система по п.11, дополнительно содержащая холодильную установку в сообщении с установкой охлаждения, обеспечивающую дополнительное охлаждение для установки охлаждения.

15. Система по п.12, дополнительно содержащая теплообменник, расположенный между фазовыми сепараторами, для нагревания первого жидкого потока преимущественно углекислого газа, направляемого во второй фазовый сепаратор.

16. Система по п.11, дополнительно содержащая коллектор, в котором обедненный углекислым газом поток ретентата смешивается с первым и вторым газофазными потоками с образованием охлажденного технологического потока, который направляется в установку охлаждения.

17. Система по п.11, в которой вся система или ее части являются мобильными.

18. Система по п.11, в которой фазовый сепаратор выбирают из одного устройства, которое имеет две или более ступени разделения, из сосуда или колонны с тарелками и нагревателями, дистилляционной колонны с ребойлером, или их сочетания.

19. Система по п.11, в которой обедненный углекислым газом поток ретентата, первый и второй газофазные потоки, по отдельности или в любом сочетании, направляются в установку охлаждения.

20. Система по п.17, в которой части системы, расположенные ниже по потоку от мембраны, исключаются из работы после переключения во второй режим, в котором текучая среда обратного притока разделяется на богатый углекислым газом поток, и богатый углекислым газом поток сбрасывается или направляется на факел, тогда как обедненный углекислым газом поток, богатый углеводородами, извлекается в виде продукта.

21. Система по п.11, в которой мембранная установка представлена полиэфирэфиркетонной (PEEK) мембраной.
RU2016134819A 2014-01-28 2015-01-07 Способ обработки текучей среды обратного притока, выходящей с площадки скважины RU2687600C2 (ru)

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Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9937464B2 (en) * 2013-05-10 2018-04-10 Arstroma Co., Ltd. Device for separating carbon dioxide using silicone separation film and method for manufacturing same
US9580996B2 (en) * 2014-05-27 2017-02-28 General Electric Company Modular assembly for processing a flowback composition stream and methods of processing the same
US11473838B2 (en) * 2015-12-18 2022-10-18 Baker Hughes Holdings Llc Flow management and CO2-recovery apparatus and method of use
US9889401B2 (en) * 2015-12-18 2018-02-13 General Electric Company Flow management and CO2-recovery apparatus and method of use
FR3052240B1 (fr) * 2016-06-02 2020-02-21 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede de liquefaction de dioxyde de carbone issu d'un courant de gaz naturel
FR3052239B1 (fr) * 2016-06-02 2020-02-21 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede de liquefaction de gaz naturel et de dioxyde de carbone
CA3049885A1 (en) * 2017-01-10 2018-07-19 Cameron Solutions, Inc. Carbon dioxide and hydrogen sulfide recovery system using a combination of membranes and low temperature cryogenic separation processes
MY193428A (en) * 2019-03-14 2022-10-12 Ngltech Sdn Bhd System for recovering natural gas liquid from low pressure source at low temperatures
US20230082135A1 (en) * 2021-09-08 2023-03-16 Uop Llc Apparatuses and processes for the recovery of carbon dioxide streams
US20240066434A1 (en) * 2022-08-30 2024-02-29 Saudi Arabian Oil Company Surface carbon capture and storage

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4441900A (en) * 1982-05-25 1984-04-10 Union Carbide Corporation Method of treating carbon-dioxide-containing natural gas
US4762543A (en) 1987-03-19 1988-08-09 Amoco Corporation Carbon dioxide recovery
US5964923A (en) 1996-02-29 1999-10-12 Membrane Technology And Research, Inc. Natural gas treatment train
DE10229232A1 (de) 2002-06-28 2004-01-29 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Membrantrennverfahren zur Anreicherung wenigstens einer Gaskomponente in einem Gasstrom
US6648944B1 (en) 2003-01-28 2003-11-18 Membrane Technology And Research, Inc. Carbon dioxide removal process
US6955704B1 (en) 2003-10-28 2005-10-18 Strahan Ronald L Mobile gas separator system and method for treating dirty gas at the well site of a stimulated well
US7124605B2 (en) 2003-10-30 2006-10-24 National Tank Company Membrane/distillation method and system for extracting CO2 from hydrocarbon gas
US20060162924A1 (en) 2005-01-26 2006-07-27 Dominion Oklahoma Texas Exploration & Production, Inc. Mobile gas separation unit
WO2008122556A2 (en) * 2007-04-04 2008-10-16 Shell Internationale Research Maatschappij B.V. Method and apparatus for separating one or more c2+ hydrocarbons from a mixed phase hydrocarbon stream
GB0816432D0 (en) * 2008-09-08 2008-10-15 Iris Forskningsinvest As Process
US20100232985A1 (en) 2009-03-10 2010-09-16 Generon Igs, Inc. Fuel gas conditioning with membrane separation
US8231785B2 (en) 2009-05-12 2012-07-31 Uop Llc Staged membrane system for gas, vapor, and liquid separations
US8454724B2 (en) 2010-06-30 2013-06-04 Uop Llc Flexible system to remove carbon dioxide from a feed natural gas
WO2012048078A1 (en) 2010-10-06 2012-04-12 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Carbon dioxide removal process
US8575414B2 (en) 2010-12-17 2013-11-05 Uop Llc Membrane system for natural gas upgrading
US9133700B2 (en) 2012-11-30 2015-09-15 General Electric Company CO2 fracturing system and method of use
CN102981292B (zh) 2012-12-07 2015-11-25 深圳市华星光电技术有限公司 断线修补方法、断线修补装置及断线修补结构
US9545599B2 (en) 2013-02-28 2017-01-17 Generon Igs, Inc. Hybrid membrane system for gas streams with condensable hydrocarbons
US20140262285A1 (en) * 2013-03-12 2014-09-18 Rustam H. Sethna Methods for fraccing oil and gas wells
CN103470223B (zh) * 2013-09-23 2015-11-25 中国矿业大学(北京) 一种化石能源低碳共采的方法和系统

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