CN115282744A - Natural Gas Recovery Unit - Google Patents
Natural Gas Recovery Unit Download PDFInfo
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- CN115282744A CN115282744A CN202210931003.1A CN202210931003A CN115282744A CN 115282744 A CN115282744 A CN 115282744A CN 202210931003 A CN202210931003 A CN 202210931003A CN 115282744 A CN115282744 A CN 115282744A
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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
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/18—Spraying or sprinkling
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Abstract
Description
技术领域technical field
本发明涉及天然气技术领域,尤其涉及天然气回收装置。The invention relates to the technical field of natural gas, in particular to a natural gas recovery device.
背景技术Background technique
天然气回收装置是用于统一回收未液气化分离的天然气以达到对未分离的天然气进行二次回收利用的效果,但是现有的天然气回收装置通常需要多个气液分离装置进行多次的分离,这样不仅提高了天然气回收装置整体的成本,同时多个气液分离装置进行多次的分离也加大的分离的时间,降低了回收的效率。因此,如何提供一种天然气回收装置是本领域技术人员亟需解决的问题。The natural gas recovery device is used to uniformly recover the unseparated natural gas to achieve the effect of secondary recovery and utilization of the unseparated natural gas, but the existing natural gas recovery device usually requires multiple gas-liquid separation devices for multiple separations , This not only increases the overall cost of the natural gas recovery device, but also increases the separation time for multiple gas-liquid separation devices and reduces the recovery efficiency. Therefore, how to provide a natural gas recovery device is an urgent problem to be solved by those skilled in the art.
发明内容Contents of the invention
本发明的一个目的在于提出天然气回收装置,本发明提高了天然气气液分离效率,同时新型设计的气液分离器无需多组进行多次分离,降低了天然气回收装置整体的成本,同时减少了分离的时间,提高了回收的效率。One object of the present invention is to propose a natural gas recovery device. The present invention improves the separation efficiency of natural gas and liquid. At the same time, the newly designed gas-liquid separator does not need multiple groups for multiple separations, which reduces the overall cost of the natural gas recovery device and reduces the separation rate. time, improving the efficiency of recycling.
根据本发明实施例的一种天然气回收装置,包括用于天然气混料进入的第一天然气进气管和多个串联设置的气液分离器,所述第一天然气进气管的出料端与气液分离器的进料口连通设置,所述气液分离器侧方设置有制冷装置,所述气液分离器底部开设有出液口,所述出液口与出液管连通设置,所述气液分离器侧方开设有出气口且所述出气口与第一出气管连通设置。A natural gas recovery device according to an embodiment of the present invention includes a first natural gas inlet pipe for mixing natural gas and a plurality of gas-liquid separators arranged in series, the discharge end of the first natural gas inlet pipe is connected to the gas-liquid The feed port of the separator is connected, the side of the gas-liquid separator is provided with a refrigeration device, the bottom of the gas-liquid separator is provided with a liquid outlet, and the liquid outlet is connected to the liquid outlet pipe. An air outlet is opened on the side of the liquid separator, and the air outlet is communicated with the first air outlet pipe.
可选的,所述第一天然气进气管上法兰安装有第一开关阀,所述第一天然气进气管与第二天然气进气管连通设置,且所述第一天然气进气管与第二天然气进气管底部均安装有管道减震器。Optionally, a first switch valve is installed on the flange of the first natural gas intake pipe, the first natural gas intake pipe communicates with the second natural gas intake pipe, and the first natural gas intake pipe communicates with the second natural gas intake pipe. Pipe shock absorbers are installed at the bottom of the trachea.
可选的,所述出液管上法兰安装有自动疏水阀。Optionally, an automatic drain valve is installed on the upper flange of the liquid outlet pipe.
可选的,所述第一出气管通过三通阀与第二出气管和第三出气管连通设置,所述第二出气管上法兰安装有第二开关阀,所述第三出气管上法兰安装有安全阀。Optionally, the first air outlet pipe is communicated with the second air outlet pipe and the third air outlet pipe through a three-way valve, the second switch valve is installed on the flange of the second air outlet pipe, and the third air outlet pipe is The flange is fitted with a safety valve.
可选的,所述第一出气管上依次安装有止回阀和筒式过滤器,安装所述筒式过滤器两端的第一出气管上连通安装有分流管,所述分流管上法兰安装有压差变送器。Optionally, a check valve and a cartridge filter are sequentially installed on the first air outlet pipe, and a shunt pipe is installed on the first air outlet pipe at both ends of the cartridge filter, and the upper flange of the shunt pipe A differential pressure transmitter is installed.
可选的,所述气液分离器包括分离主体和竖向安装在分离主体内的多根喷料管,所述喷料管顶端与第二天然气进气管连通设置。Optionally, the gas-liquid separator includes a separation body and a plurality of spray pipes vertically installed in the separation body, and the top ends of the spray pipes are arranged in communication with the second natural gas inlet pipe.
可选的,所述喷料管包括料管本体,所述料管本体侧面连通安装有出料端口向上开设的侧出料管,所述侧出料管的出料端口上安装有喷淋头。Optionally, the spray pipe includes a pipe body, the side of the pipe body is communicated with a side discharge pipe with a discharge port opened upward, and a spray head is installed on the discharge port of the side discharge pipe .
可选的,所述分离主体上侧设置有驱动电机,所述驱动电机的输出端轴上套设有驱动带轮,位于所述分离主体上外部的喷料管上均套设有驱动带轮,多个所述驱动带轮通过驱动皮带传动连接。Optionally, a driving motor is provided on the upper side of the separation main body, and a driving pulley is sleeved on the output end shaft of the driving motor, and a driving pulley is sleeved on the spray pipes located outside the separation main body. , a plurality of said driving pulleys are connected through a driving belt transmission.
可选的,所述喷料管顶端与第二天然气进气管通过联轴器连接。Optionally, the top end of the spray pipe is connected to the second natural gas inlet pipe through a coupling.
可选的,所述分离主体壁内开设有第一导风槽,所述制冷装置与导风槽连通设置,位于所述侧出料管的出料端口上方的分离主体内部均安装有倾斜设置的折流板,所述折流板内开设有第二导风槽,所述第一导风槽与第二导风槽连通设置。Optionally, a first air guide groove is provided in the wall of the separation main body, and the refrigeration device is connected with the air guide groove, and the inside of the separation main body above the discharge port of the side discharge pipe is equipped with inclined devices. The baffle plate is provided with a second air guide groove inside the baffle plate, and the first air guide groove is communicated with the second air guide groove.
本发明的有益效果是:The beneficial effects of the present invention are:
本发明对未分离的天然气进行二次回收分离,喷淋头起到对天然气发散喷出的效果,喷淋头与折流板的设置起到对天然气全方面立体高效的气液分离,气液分离器内设置的叠式倾斜设置的折流板避免了液体回流,提高了天然气气液分离效率,同时新型设计的气液分离器无需多组进行多次分离,降低了天然气回收装置整体的成本,同时减少了分离的时间,提高了回收的效率。The invention performs secondary recovery and separation on the unseparated natural gas, the spray head has the effect of diverging and spraying the natural gas, and the arrangement of the spray head and the baffle plate can achieve three-dimensional and efficient gas-liquid separation of the natural gas in all aspects, and the gas-liquid The stacked inclined baffles installed in the separator avoid liquid backflow and improve the efficiency of gas-liquid separation of natural gas. At the same time, the newly designed gas-liquid separator does not need multiple groups for multiple separations, which reduces the overall cost of the natural gas recovery device. , while reducing the separation time and improving recovery efficiency.
附图说明Description of drawings
在附图中:In the attached picture:
图1为本发明提出的天然气回收装置的结构示意图;Fig. 1 is the structural representation of the natural gas recovery device that the present invention proposes;
图2为本发明提出的天然气回收装置中气液分离器的结构示意图;Fig. 2 is the structural representation of gas-liquid separator in the natural gas recovery device that the present invention proposes;
图3为本发明提出的天然气回收装置中气液分离器内部风向的流向图;Fig. 3 is the flow diagram of the internal wind direction of the gas-liquid separator in the natural gas recovery device proposed by the present invention;
图4为本发明提出的天然气回收装置中联轴器的结构示意图;Fig. 4 is the structural representation of coupling in the natural gas recovery device that the present invention proposes;
图5为本发明提出的天然气回收装置中喷料管的结构示意图。Fig. 5 is a schematic structural view of the injection pipe in the natural gas recovery device proposed by the present invention.
图中:1-第一天然气进气管、2-气液分离器、3-第一开关阀、4-管道减震器、5-压力表、6-第二天然气进气管、7-出液管、8-自动疏水阀、9-第一出气管、10-第二出气管、11-三通阀、12-第二开关阀、13-安全阀、14-第三出气管、15-止回阀、16-筒式过滤器、17-分流管、18-压差变送器、19-制冷装置;In the figure: 1-first natural gas inlet pipe, 2-gas-liquid separator, 3-first switch valve, 4-pipeline shock absorber, 5-pressure gauge, 6-second natural gas inlet pipe, 7-liquid outlet pipe , 8-automatic steam trap, 9-first air outlet pipe, 10-second air outlet pipe, 11-three-way valve, 12-second switch valve, 13-safety valve, 14-third air outlet pipe, 15-check Valve, 16-Cylinder filter, 17-Split pipe, 18-Pressure differential transmitter, 19-Refrigeration device;
21-分离主体、22-驱动电机、23-驱动皮带、24-出气口、25-出液口、26-喷料管、261-料管本体、262-侧出料管、263-喷淋头、27-折流板、28-联轴器、29-驱动带轮。21-Separation main body, 22-Drive motor, 23-Drive belt, 24-Air outlet, 25-Liquid outlet, 26-Spray pipe, 261-Main pipe body, 262-Side discharge pipe, 263-Spray head , 27-baffle plate, 28-coupling, 29-drive pulley.
具体实施方式Detailed ways
参考图1-2,一种天然气回收装置,包括用于天然气混料进入的第一天然气进气管1和多个串联设置的气液分离器2,第一天然气进气管1的出料端与气液分离器2的进料口连通设置,气液分离器2侧方设置有制冷装置19,气液分离器2底部开设有出液口25,出液口25与出液管7连通设置,气液分离器2侧方开设有出气口24,出气口24与第一出气管9连通设置。Referring to Fig. 1-2, a natural gas recovery device includes a first natural gas inlet pipe 1 for mixing natural gas and a plurality of gas-
多个串联设置的气液分离器2起到对天然气多级分离的作用,基于本发明的气液分离器2的分离效率,气液分离器2的设置数量可以为1-3个,本实施例中选用3个。A plurality of gas-
第一天然气进气管1上法兰安装有第一开关阀3,第一天然气进气管1与第二天然气进气管6连通设置,且第一天然气进气管1与第二天然气进气管6底部均安装有管道减震器4,出液管7上法兰安装有自动疏水阀8。The flange on the first natural gas inlet pipe 1 is equipped with a first on-off
第一出气管9通过三通阀11与第二出气管10和第三出气管14连通设置,第二出气管10上法兰安装有第二开关阀12,第三出气管14上法兰安装有安全阀13。The first air outlet pipe 9 communicates with the second
第一出气管9上依次安装有止回阀15和筒式过滤器16,安装筒式过滤器16两端的第一出气管9上连通安装有分流管17,分流管17上法兰安装有压差变送器18。A
参考图4,气液分离器2包括分离主体1,分离主体1内竖向安装有多根喷料管26,喷料管26顶端与第二天然气进气管6连通设置,喷料管26顶端与第二天然气进气管6通过联轴器28连接。Referring to Fig. 4, the gas-
联轴器28由上联轴器和下联轴器两个部分组成,上联轴器和下联轴器分别用来连通第二天然气进气管6和喷料管26,使喷料管26在转动的同时第二天然气进气管6能对其进行天然气的传送并且还具有缓冲和提高轴系动态性能的作用。
参考图5,喷料管26包括料管本体261,料管本体261侧面连通安装有出料端口向上开设的侧出料管262,侧出料管262的出料端口上安装有喷淋头263,喷淋头263起到对天然气发散喷出的效果,喷淋头263和折流板27的设置起到对天然气全方面立体高效的气液分离。With reference to Fig. 5, the
平行设置的多根料管本体261和1个驱动电机22组成1组出料机构且出料机构设置为1-4组,侧出料管262和折流板27的设置起到对天然气全方面立体高效的气液分离。A plurality of
分离主体1上侧设置有驱动电机22,驱动电机22的输出端轴上套设有驱动带轮29,位于分离主体21上外部的喷料管26上均套设有驱动带轮29,多个驱动带轮29通过驱动皮带传动连接。The upper side of the separation main body 1 is provided with a
参考图3,分离主体21壁内开设有第一导风槽,制冷装置19与导风槽连通设置,位于侧出料管262的出料端口上方的分离主体1内部均安装有倾斜设置的折流板27,折流板27内开设有第二导风槽,第一导风槽与第二导风槽连通设置,制冷装置19可以为半导体制冷装置,制冷装置19的作用是将冷气导通至分离主体21和折流板27内。With reference to Fig. 3, the separation
当天然气从侧出料管262出料端喷出与内部制冷的折流板27接触时,天然气中的液体发生凝聚,同时料管本体261此时在转动在离心力的作用下沿折流板27底部表面形成水珠,沿着倾斜设置的折流板27向分离主体21底部的出液口25出液,叠式倾斜设置的折流板27避免了液体回流,提高了天然气气液分离效率。When the natural gas is ejected from the discharge end of the
为了实时的监控所有管道上的天然气压力保证整体流程的安全性,第一天然气进气管1、第二天然气进气管6和第一出气管9上均安装有压力表5,压力表5能实时的显示第一天然气进气管1、第二天然气进气管6和第一出气管9上不同阶段的天然气的压力。In order to monitor the natural gas pressure on all pipelines in real time to ensure the safety of the overall process, a
可以理解的是,本发明中的自动疏水阀8、三通阀11、安全阀13、止回阀15、筒式过滤器16、压差变送器18、制冷装置19和驱动电机22的驱动方式可以采用外接电源线的方式进行驱动,自动疏水阀8、三通阀11、安全阀13、止回阀15、筒式过滤器16、压差变送器18、制冷装置19和驱动电机22的控制可以采用主控系统进行编程控制,其控制原理为现有控制技术能实现的。自动疏水阀8、三通阀11、安全阀13、止回阀15、筒式过滤器16、压差变送器18、制冷装置19和驱动电机22的型号不限于单一的类型可以为市场上现有适合与本发明的类型。It can be understood that the driving of the
实施方式:Implementation method:
未液气化分离的天然气通过第一天然气进气管1进入,通过第二天然气进气管6的导通进入气液分离器2内,启动驱动电机22带动喷料管26转动,天然气从侧出料管262出料端喷出与内部制冷的折流板27接触,天然气中的液体发生凝聚同时料管本体261此时在转动在离心力的作用下沿折流板27底部表面形成水珠,沿着倾斜设置的折流板27向分离主体21底部的出液口25出液,分离后的天然气从出气口24导出经过筒式过滤器16过滤后导出。The natural gas that has not been liquefied and gasified and separated enters through the first natural gas inlet pipe 1, enters the gas-
本发明对未分离的天然气进行二次回收分离,喷淋头263起到对天然气发散喷出的效果,喷淋头263和折流板27的设置起到对天然气全方面立体高效的气液分离,气液分离器2内设置的叠式倾斜设置的折流板27避免了液体回流,提高了天然气气液分离效率,同时新型设计的气液分离器2无需多组进行多次分离,降低了天然气回收装置整体的成本,同时减少了分离的时间,提高了回收的效率。The present invention performs secondary recovery and separation on the unseparated natural gas, the
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Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5630328A (en) * | 1995-09-22 | 1997-05-20 | Consolidated Natural Gas Service Company, Inc. | Natural gas conditioning facility |
| CN101818088A (en) * | 2009-12-15 | 2010-09-01 | 江苏工业学院 | Efficient continuous preparation method and device for natural gas hydrate |
| CN101967413A (en) * | 2010-06-07 | 2011-02-09 | 杭州福斯达实业集团有限公司 | Method and device for liquefying natural gas via refrigeration of single mixed refrigerant |
| CN102455112A (en) * | 2010-10-18 | 2012-05-16 | 袁俊海 | Natural gas liquefaction process by propane precooling mixed refrigerant |
| CN103194286A (en) * | 2013-04-08 | 2013-07-10 | 西北化工研究院 | Methanation method for synthesizing substitute natural gas by using industrial hydrocarbon exhaust gas |
| CN104128106A (en) * | 2013-05-02 | 2014-11-05 | 厦门大学 | Novel swirl dispersing device |
| WO2015005791A1 (en) * | 2013-07-11 | 2015-01-15 | Vitality Vector B.V. | Device and method for extracting various components from ambient air or from a vapor-gas mixture, and a system for cooling air, heating air, desalination of water and/or purification of water |
| CN105038887A (en) * | 2015-08-15 | 2015-11-11 | 重庆联合机器制造有限公司 | Gas-liquid condensing separator |
| CN206715497U (en) * | 2017-03-09 | 2017-12-08 | 中国海洋石油总公司 | A kind of underwater combined type natural gas gas-liquid separation device |
| CN107726729A (en) * | 2016-08-11 | 2018-02-23 | 中石化洛阳工程有限公司 | A kind of liquefied natural gas condensation method and device again |
| CN207294704U (en) * | 2017-09-18 | 2018-05-01 | 夏晓明 | A kind of natural-gas separator |
| CN208667598U (en) * | 2018-08-10 | 2019-03-29 | 杰瑞(天津)石油工程技术有限公司 | A kind of novel natural gas light ends unit |
| CN110496420A (en) * | 2019-08-16 | 2019-11-26 | 新榕能源(福建)有限公司 | A continuous oil-water separation equipment |
| CN209704656U (en) * | 2019-04-16 | 2019-11-29 | 李福军 | Heat U-shaped tower tube multiphase flow boosting turbine efficient circulation power generator |
| CN210237556U (en) * | 2019-07-02 | 2020-04-03 | 泸州太昌能源有限公司 | Novel natural gas-liquid separation device |
| CN212154738U (en) * | 2020-03-09 | 2020-12-15 | 上海焱晶燃烧设备检测有限公司 | Integrated device for oil-gas separation and condensate conveying |
| CN214244332U (en) * | 2021-01-05 | 2021-09-21 | 西安石油大学 | Gas field gas-liquid separator |
| CN215311171U (en) * | 2021-03-02 | 2021-12-28 | 中国石油大学(华东) | A new type of gas-liquid separation device |
| CN215427725U (en) * | 2021-02-20 | 2022-01-07 | 厚成科技(南通)有限公司 | High-efficient vapour and liquid separator |
| RU2768410C1 (en) * | 2021-05-26 | 2022-03-24 | Александр Семенович Дубовик | Centrifugal gas-liquid separator |
-
2022
- 2022-08-04 CN CN202210931003.1A patent/CN115282744A/en active Pending
Patent Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5630328A (en) * | 1995-09-22 | 1997-05-20 | Consolidated Natural Gas Service Company, Inc. | Natural gas conditioning facility |
| CN101818088A (en) * | 2009-12-15 | 2010-09-01 | 江苏工业学院 | Efficient continuous preparation method and device for natural gas hydrate |
| CN101967413A (en) * | 2010-06-07 | 2011-02-09 | 杭州福斯达实业集团有限公司 | Method and device for liquefying natural gas via refrigeration of single mixed refrigerant |
| CN102455112A (en) * | 2010-10-18 | 2012-05-16 | 袁俊海 | Natural gas liquefaction process by propane precooling mixed refrigerant |
| CN103194286A (en) * | 2013-04-08 | 2013-07-10 | 西北化工研究院 | Methanation method for synthesizing substitute natural gas by using industrial hydrocarbon exhaust gas |
| CN104128106A (en) * | 2013-05-02 | 2014-11-05 | 厦门大学 | Novel swirl dispersing device |
| WO2015005791A1 (en) * | 2013-07-11 | 2015-01-15 | Vitality Vector B.V. | Device and method for extracting various components from ambient air or from a vapor-gas mixture, and a system for cooling air, heating air, desalination of water and/or purification of water |
| CN105038887A (en) * | 2015-08-15 | 2015-11-11 | 重庆联合机器制造有限公司 | Gas-liquid condensing separator |
| CN107726729A (en) * | 2016-08-11 | 2018-02-23 | 中石化洛阳工程有限公司 | A kind of liquefied natural gas condensation method and device again |
| CN206715497U (en) * | 2017-03-09 | 2017-12-08 | 中国海洋石油总公司 | A kind of underwater combined type natural gas gas-liquid separation device |
| CN207294704U (en) * | 2017-09-18 | 2018-05-01 | 夏晓明 | A kind of natural-gas separator |
| CN208667598U (en) * | 2018-08-10 | 2019-03-29 | 杰瑞(天津)石油工程技术有限公司 | A kind of novel natural gas light ends unit |
| CN209704656U (en) * | 2019-04-16 | 2019-11-29 | 李福军 | Heat U-shaped tower tube multiphase flow boosting turbine efficient circulation power generator |
| CN210237556U (en) * | 2019-07-02 | 2020-04-03 | 泸州太昌能源有限公司 | Novel natural gas-liquid separation device |
| CN110496420A (en) * | 2019-08-16 | 2019-11-26 | 新榕能源(福建)有限公司 | A continuous oil-water separation equipment |
| CN212154738U (en) * | 2020-03-09 | 2020-12-15 | 上海焱晶燃烧设备检测有限公司 | Integrated device for oil-gas separation and condensate conveying |
| CN214244332U (en) * | 2021-01-05 | 2021-09-21 | 西安石油大学 | Gas field gas-liquid separator |
| CN215427725U (en) * | 2021-02-20 | 2022-01-07 | 厚成科技(南通)有限公司 | High-efficient vapour and liquid separator |
| CN215311171U (en) * | 2021-03-02 | 2021-12-28 | 中国石油大学(华东) | A new type of gas-liquid separation device |
| RU2768410C1 (en) * | 2021-05-26 | 2022-03-24 | Александр Семенович Дубовик | Centrifugal gas-liquid separator |
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