WO2021097791A1 - 一种井口气净化系统 - Google Patents

一种井口气净化系统 Download PDF

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Publication number
WO2021097791A1
WO2021097791A1 PCT/CN2019/120167 CN2019120167W WO2021097791A1 WO 2021097791 A1 WO2021097791 A1 WO 2021097791A1 CN 2019120167 W CN2019120167 W CN 2019120167W WO 2021097791 A1 WO2021097791 A1 WO 2021097791A1
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gas
membrane separator
filter
separator
dehydration
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PCT/CN2019/120167
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English (en)
French (fr)
Inventor
杨锦祥
牛虎勋
林树青
张立艳
刘曌
李丹
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杰瑞(天津)石油工程技术有限公司
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Priority to PCT/CN2019/120167 priority Critical patent/WO2021097791A1/zh
Publication of WO2021097791A1 publication Critical patent/WO2021097791A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • 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
    • B01D53/22—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 diffusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • 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
    • B01D53/26—Drying gases or vapours
    • 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

Definitions

  • the invention relates to the technical field of wellhead gas purification, in particular to a wellhead gas purification system.
  • Natural gas produced from wellheads generally contains saturated water, which is a harmful component in natural gas.
  • the presence of natural gas saturated water reduces the transmission capacity of gas pipelines and reduces the calorific value of natural gas.
  • saturated water When natural gas is compressed or the temperature drops, saturated water will precipitate out of the gas stream to form liquid water, hydrates, etc., and in severe cases, it will block valves, pipelines and equipment.
  • the presence of heavy hydrocarbons makes the hydrocarbon dew point of natural gas higher.
  • the temperature and pressure of natural gas change heavy hydrocarbon components in natural gas will separate out to form a liquid phase, which will easily cause freezing and blockage when the temperature is lower than the ambient temperature.
  • the condensate combines with the acid gas in natural gas, which is easy to affect downstream The pipelines, valves and other equipment cause corrosion.
  • the traditional dehydration process includes cooling method, solid adsorption method and solvent absorption method, while the dehydrocarbon process is mainly low temperature separation method and solvent absorption method.
  • the field of natural gas purification uses one or a combination of the above-mentioned processes to remove saturated water and heavy hydrocarbons from natural gas.
  • the existing process has the problems of complicated process, large area and high operating cost.
  • the purpose of the present invention overcomes the shortcomings of the prior art and provides a wellhead gas purification system, which adopts a series of membrane separation devices to achieve dehydration and heavy hydrocarbon removal through a dehydration membrane separator and a heavy hydrocarbon removal membrane separator, respectively, and the entire wellhead gas purification
  • the system is simple in structure, easy to assemble, easy to skid-mounted, small in area, no additional materials and reagent consumption, and low operating cost.
  • a wellhead gas purification system including a filter, a compressor, an air cooler, a gas-liquid separator, a dehydration membrane separator and a heavy hydrocarbon membrane separator, the filter
  • One end of the filter is connected to the wellhead gas pipeline
  • the outlet of the filter is connected to the inlet of the compressor
  • the outlet of the compressor is connected to one end of the air cooler
  • the other end of the air cooler Connected to the inlet of the gas-liquid separator
  • the gas outlet of the gas-liquid separator is connected to the inlet of the dehydration membrane separator
  • the gas outlet of the dehydration membrane separator is connected to the heavy hydrocarbon membrane separator connection.
  • the permeate side outlet of the dehydration membrane separator is connected to the inlet of the filter.
  • outlet of the permeate side of the heavy hydrocarbon membrane separator is connected to the inlet of the filter.
  • the filters, compressors, air coolers, gas-liquid separators, dehydration membrane separators and heavy hydrocarbon membrane separators can be skid-mounted on 1-2 skid seats according to the size of the equipment.
  • the present invention has the beneficial effects of adopting series-connected membrane separation devices, dehydrating and removing heavy hydrocarbons through a dehydration membrane separator and a heavy hydrocarbon removal membrane separator, respectively, and the entire wellhead gas purification system has a simple structure and assembly Convenient, easy to skid-mounted, small footprint, no additional material and reagent consumption, and low operating cost.
  • Fig. 1 is a schematic diagram of the structure of the present invention.
  • a wellhead gas purification system includes a filter 1, a compressor 2, an air cooler 3, a gas-liquid separator 4, a dehydration membrane separator 5 and a heavy hydrocarbon membrane separator 6, so One end of the filter 1 is connected to a wellhead gas pipeline, the outlet of the filter 1 is connected to the inlet of the compressor 2, and the outlet of the compressor 2 is connected to one end of the air cooler 3. , The other end of the air cooler 3 is connected to the inlet of the gas-liquid separator 4, the gas outlet of the gas-liquid separator 4 is connected to the inlet of the dehydration membrane separator 5, the dehydration membrane separator The gas outlet of 5 is connected to the heavy hydrocarbon membrane separator 6.
  • the wellhead gas purification system is simple in structure, convenient to assemble, easy to be skid-mounted, small in area, no additional material and reagent consumption, and low operating cost.
  • the permeate side outlet of the dehydration membrane separator 5 is connected to the inlet of the filter 1.
  • the outlet of the permeate side of the heavy hydrocarbon membrane separator 6 is connected to the inlet of the filter 1.
  • the filter 1, the compressor 2, the air cooler 3, the gas-liquid separator 4, the dehydration membrane separator 5 and the heavy hydrocarbon membrane separator 6 can be skid-mounted on 1-2 skid seats according to the size of the equipment .

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

一种井口气净化系统，包括过滤器（1）、压缩机（2）、空冷器（3）、气液分离器（4）、脱水膜分离器（5）和脱重烃膜分离器（6），过滤器（1）的一端与井口气管线接通，过滤器（1）的出气口与压缩机（2）的进气端连接，压缩机（2）的出气端与空冷器（3）的一端连接，空冷器（3）的另一端与气液分离器（4）的接入口连接，气液分离器（4）的出气口与脱水膜分离器（5）的入口连接，脱水膜分离器（5）的出气口与脱重烃膜分离器（6）连接；采用串联的膜分离装置，通过脱水膜分离器（5）和脱重烃膜分离器（6）分别实现脱水和脱重烃，整个井口气净化系统结构简单，组装方便，易橇装，占地面积小，无额外材料和试剂消耗，运行成本低。

Description

一种井口气净化系统 技术领域
本发明涉及井口气净化技术领域，具体涉及一种井口气净化系统。
背景技术
自井口采出的天然气一般都含有饱和水，它是天然气中的有害成分。天然气饱和水的存在，减少了输气管道的输送能力，降低了天然气的热值。当天然气被压缩或者温度下降时，饱和水会从气流中析出形成液态水，水合物等，严重时还会堵塞阀门、管道及设备。同样，重烃的存在，使得天然气的烃露点较高。在天然气的温度、压力发生变化时，天然气中的重烃组分就会析出形成液相，低于环境温度时容易造成冻堵，另一方面凝液与天然气中的酸性气体结合，容易对下游的管线、阀门及其他设备造成腐蚀。
传统的脱水工艺包括冷却法、固体吸附法和溶剂吸收法，脱烃工艺则主要是低温分离法和溶剂吸收法。目前天然气净化领域都是采用上述的一种或者多种工艺的组合，将饱和水及重烃从天然气中脱除。现有工艺存在流程复杂、占地面积大，运行费用高的问题。
发明内容
本发明的目的克服现有技术的不足，提供一种井口气净化系统，采用串联的膜分离装置，通过脱水膜分离器和脱重烃膜分离器分别实现脱水和脱重烃，整个井口气净化系统结构简单，组装方便，易橇装，占地面积小，无额外材料和试剂消耗，运行成本低。
本发明的目的是通过以下技术措施达到的：一种井口气净化系统，包括过滤器、压缩机、空冷器、气液分离器、脱水膜分离器和脱重烃膜分离器， 所述过滤器的一端与井口气管线接通，所述过滤器的出气口与所述压缩机的进气端连接，所述压缩机的出气端与所述空冷器的一端连接，所述空冷器的另一端与所述气液分离器的接入口连接，所述气液分离器的出气口与所述脱水膜分离器的入口连接，所述脱水膜分离器的出气口与所述脱重烃膜分离器连接。
进一步地，所述脱水膜分离器渗透侧出口连接过滤器的入口。
进一步地，所述脱重烃膜分离器渗透侧出口连接过滤器的入口。
进一步地，所述过滤器、压缩机、空冷器、气液分离器、脱水膜分离器和脱重烃膜分离器，可根据设备的大小尺寸橇装到1-2个橇座上。
与现有技术相比，本发明的有益效果是：采用串联的膜分离装置，通过脱水膜分离器和脱重烃膜分离器分别实现脱水和脱重烃，整个井口气净化系统结构简单，组装方便，易橇装，占地面积小，无额外材料和试剂消耗，运行成本低。
下面结合附图和具体实施方式对本发明作详细说明。
附图说明
图1是本发明的结构示意图。
其中，1.过滤器，2.压缩机，3.空冷器，4.气液分离器，5.脱水膜分离器，6.脱重烃膜分离器。
具体实施方式
实施例，如图1所示，一种井口气净化系统，包括过滤器1、压缩机2、空冷器3、气液分离器4、脱水膜分离器5和脱重烃膜分离器6，所述过滤器1的一端与井口气管线接通，所述过滤器1的出气口与所述压缩机2的进气 端连接，所述压缩机2的出气端与所述空冷器3的一端连接，所述空冷器3的另一端与所述气液分离器4的接入口连接，所述气液分离器4的出气口与所述脱水膜分离器5的入口连接，所述脱水膜分离器5的出气口与所述脱重烃膜分离器6连接。本井口气净化系统结构简单，组装方便，易橇装，占地面积小，无额外材料和试剂消耗，运行成本低。
所述脱水膜分离器5渗透侧出口连接过滤器1的入口。
所述脱重烃膜分离器6渗透侧出口连接过滤器1的入口。
所述过滤器1、压缩机2、空冷器3、气液分离器4、脱水膜分离器5和脱重烃膜分离器6，可根据设备的大小尺寸橇装到1-2个橇座上。
工作原理：
(1)井口气进入过滤器1除去夹带的液体及固体颗粒；
(2)去除杂质的天然气进入压缩机2进行增压；
(3)增压后的天然气进入空冷器3进行冷却；
(4)冷却后的天然气进入气液分离器4进行气液分离；
(5)去除凝液的天然气进入脱水膜分离器5进行脱水；
(6)脱水后的天然气进入脱重烃膜分离器6进一步脱去重烃；
(7)脱除水和重烃的净化气去往外输管道。
(8)脱水膜分离器和脱重烃膜分离器的渗透气接入过滤器1的入口。
本行业的技术人员应该了解，本发明不受上述实施例的限制，上述实施例和说明书中描述的只是说明本发明的原理，在不脱离本发明精神和范围的前提下，本发明还会有各种变化和改进，这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。

Claims (4)

  1. 一种井口气净化系统，其特征在于：包括过滤器、压缩机、空冷器、气液分离器、脱水膜分离器和脱重烃膜分离器，所述过滤器的一端与井口气管线接通，所述过滤器的出气口与所述压缩机的进气端连接，所述压缩机的出气端与所述空冷器的一端连接，所述空冷器的另一端与所述气液分离器的接入口连接，所述气液分离器的出气口与所述脱水膜分离器的入口连接，所述脱水膜分离器的出气口与所述脱重烃膜分离器连接。
  2. 根据权利要求1所述的井口气净化系统，其特征在于：所述脱水膜分离器渗透侧出口连接过滤器的入口。
  3. 根据权利要求1所述的井口气净化系统，其特征在于：所述脱重烃膜分离器渗透侧出口连接过滤器的入口。
  4. 根据权利要求1所述的井口气净化系统，其特征在于：所述过滤器、压缩机、空冷器、气液分离器、脱水膜分离器和脱重烃膜分离器，可根据设备的大小尺寸橇装到1-2个橇座上。
PCT/CN2019/120167 2019-11-22 2019-11-22 一种井口气净化系统 WO2021097791A1 (zh)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1713949A (zh) * 2002-11-21 2005-12-28 液体空气乔治洛德方法利用和研究的具有监督和管理委员会的有限公司 膜分离方法
CN201692748U (zh) * 2010-06-04 2011-01-05 大连欧科膜技术工程有限公司 有机气体的排放控制与回收装置
WO2015069882A1 (en) * 2013-11-08 2015-05-14 Membrane Technology And Research, Inc Two-step membrane gas separation process with membranes having different selectivities
CN104857811A (zh) * 2015-05-06 2015-08-26 中石化石油工程设计有限公司 油田二氧化碳驱采出气二氧化碳分离回收系统
CN107660250A (zh) * 2015-03-25 2018-02-02 普莱克斯技术有限公司 使用两级膜方法的co2排除方法和系统
CN108424799A (zh) * 2018-05-29 2018-08-21 成都赛普瑞兴科技有限公司 一种采用膜分离净化生产液化天然气的装置及方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1713949A (zh) * 2002-11-21 2005-12-28 液体空气乔治洛德方法利用和研究的具有监督和管理委员会的有限公司 膜分离方法
CN201692748U (zh) * 2010-06-04 2011-01-05 大连欧科膜技术工程有限公司 有机气体的排放控制与回收装置
WO2015069882A1 (en) * 2013-11-08 2015-05-14 Membrane Technology And Research, Inc Two-step membrane gas separation process with membranes having different selectivities
CN107660250A (zh) * 2015-03-25 2018-02-02 普莱克斯技术有限公司 使用两级膜方法的co2排除方法和系统
CN104857811A (zh) * 2015-05-06 2015-08-26 中石化石油工程设计有限公司 油田二氧化碳驱采出气二氧化碳分离回收系统
CN108424799A (zh) * 2018-05-29 2018-08-21 成都赛普瑞兴科技有限公司 一种采用膜分离净化生产液化天然气的装置及方法

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