CN110681176A - An electrically heated gas-liquid separator - Google Patents
An electrically heated gas-liquid separator Download PDFInfo
- Publication number
- CN110681176A CN110681176A CN201911079380.1A CN201911079380A CN110681176A CN 110681176 A CN110681176 A CN 110681176A CN 201911079380 A CN201911079380 A CN 201911079380A CN 110681176 A CN110681176 A CN 110681176A
- Authority
- CN
- China
- Prior art keywords
- flange
- gas
- elliptical head
- liquid
- cylinder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 68
- 238000010438 heat treatment Methods 0.000 claims abstract description 43
- 238000000926 separation method Methods 0.000 claims abstract description 17
- 230000001681 protective effect Effects 0.000 claims abstract description 12
- 239000003792 electrolyte Substances 0.000 claims abstract description 10
- 230000000694 effects Effects 0.000 abstract description 7
- 230000010354 integration Effects 0.000 abstract description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 20
- 239000001257 hydrogen Substances 0.000 description 17
- 229910052739 hydrogen Inorganic materials 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 239000007789 gas Substances 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 10
- 238000005868 electrolysis reaction Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 238000005485 electric heating Methods 0.000 description 4
- 239000003595 mist Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
Images
Classifications
-
- 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
- B01D53/002—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
-
- 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)
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/16—Hydrogen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Metallurgy (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Automation & Control Theory (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
本发明涉及一种可电加热式气液分离器,包括加热组件和和位于加热组件外部的气液分离组件;加热组件包括保护壳体、加热丝、法兰盖及固定法兰;保护壳体包括筒体和椭圆封头,椭圆封头密封在筒体的顶端,筒体的底端连接固定法兰,固定法兰的底面连接有法兰盖,法兰盖下方固定有接线盒,筒体的内部设置有U型的加热丝,加热丝的底端穿过法兰盖进入到接线盒内;气液分离组件包括外部壳体,外部壳体包括从上至下依次布置的上部椭圆封头、中间筒体和下部椭圆封头,其中,上部椭圆封头上方连接有气体出口法兰,中部连接有电解液体进口法兰,保护壳体的大部分穿过下部椭圆封头伸入中间筒体内。本发明集成化程度高,分离效果好。
The invention relates to an electrically heatable gas-liquid separator, comprising a heating component and a gas-liquid separation component located outside the heating component; the heating component comprises a protective casing, a heating wire, a flange cover and a fixing flange; the protective casing It includes a cylinder body and an elliptical head, the elliptical head is sealed at the top of the cylinder, the bottom of the cylinder is connected to a fixed flange, the bottom of the fixed flange is connected with a flange cover, and a junction box is fixed under the flange cover. There is a U-shaped heating wire inside, and the bottom end of the heating wire enters the junction box through the flange cover; the gas-liquid separation component includes an outer casing, and the outer casing includes an upper elliptical head arranged in sequence from top to bottom , the middle cylinder and the lower elliptical head, wherein the upper elliptical head is connected with a gas outlet flange, the middle is connected with an electrolyte liquid inlet flange, and most of the protective shell extends into the middle cylinder through the lower elliptical head . The invention has high integration degree and good separation effect.
Description
技术领域technical field
本发明涉及电解水制氢领域,尤其涉及一种可电加热式气液分离器。The invention relates to the field of hydrogen production by electrolysis of water, in particular to an electrically heated gas-liquid separator.
背景技术Background technique
氢能源因为热值高、清洁无污染并且可以作为能量储存介质而广受欢迎,是一种理想的能源。电解水制氢技术因制出的氢气纯度高,并且可以将其他能源通过电解储存在氢气中而受重视。气液分离器是电解水制氢装置中的关键设备,一方面电解出的氢气和液体的混合物必须通过该设备分离,另一方面电解液体需在该设备中短暂滞留。温度是决定电解水制氢效率的第一因素。实际情况下,在电解水制氢装置开机和运行的过程中往往会出现电解液体温度过低的状况,需要很长时间等待装置升温、运行稳定,这不利于电解水制氢设备的快速反应。Hydrogen energy is popular because of its high calorific value, clean and pollution-free, and can be used as an energy storage medium, making it an ideal energy source. Hydrogen production by electrolysis of water is valued because the hydrogen produced is of high purity and other energy sources can be stored in hydrogen through electrolysis. The gas-liquid separator is the key equipment in the water electrolysis hydrogen production device. On the one hand, the mixture of hydrogen and liquid produced by electrolysis must be separated by this equipment, and on the other hand, the electrolytic liquid needs to stay in the equipment for a short time. Temperature is the first factor that determines the efficiency of hydrogen production from water electrolysis. In practice, the temperature of the electrolytic liquid is often too low during the startup and operation of the electrolytic water hydrogen production device. It takes a long time to wait for the device to heat up and run stably, which is not conducive to the rapid response of the electrolytic water hydrogen production equipment.
因此,开发一种能快速加热升温的气液分离设备具有很重要的实用价值。Therefore, it is of great practical value to develop a gas-liquid separation device that can heat up rapidly.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于,解决现有技术中存在的上述不足之处。The purpose of the present invention is to solve the above-mentioned deficiencies in the prior art.
为实现上述目的,本发明实施例提供了一种可电加热式气液分离器,包括加热组件和和位于加热组件外部的气液分离组件;加热组件包括保护壳体、法兰盖及固定法兰和加热丝;保护壳体包括筒体和椭圆封头,椭圆封头连接在筒体的顶端,筒体的底端连接固定法兰,固定法兰的底面连接有法兰盖,法兰盖下方固定有接线盒,接线盒上设置有接线孔,筒体的内部设置有加热丝,加热丝呈倒U型,加热丝的底端穿过法兰盖进入到接线盒内,加热丝固定在法兰盖上;气液分离组件包括外部壳体,外部壳体包括中间筒体和位于中间筒体上下两端的上部椭圆封头和下部椭圆封头,其中,上部椭圆封头上方连接有气体出口法兰,中间筒体的中部连接有电解液体进口法兰,保护壳体的大部分穿过下部椭圆封头伸入中间筒体内,下部椭圆封头还连接有液体出口法兰。In order to achieve the above purpose, an embodiment of the present invention provides an electrically heatable gas-liquid separator, including a heating assembly and a gas-liquid separation assembly located outside the heating assembly; the heating assembly includes a protective casing, a flange cover and a fixing method. The protective shell includes a cylinder body and an elliptical head, the elliptical head is connected to the top of the cylinder, the bottom of the cylinder is connected to a fixed flange, and the bottom of the fixed flange is connected to a flange cover, the flange cover A junction box is fixed below, a wiring hole is arranged on the junction box, a heating wire is arranged inside the cylinder, and the heating wire is in an inverted U shape. cover the flange; the gas-liquid separation assembly includes an outer casing, the outer casing includes a middle cylinder, an upper elliptical head and a lower elliptical head located at the upper and lower ends of the middle cylinder, wherein the upper elliptical head is connected with a gas outlet Flange, the middle part of the middle cylinder is connected with an electrolytic liquid inlet flange, and most of the protective shell protrudes into the middle cylinder through the lower elliptical head, and the lower elliptical head is also connected with a liquid outlet flange.
在一种可能的实施方式中,上部圆法兰上方通过气体出口管连接气体出口法兰。In a possible embodiment, the upper circular flange is connected to the gas outlet flange through a gas outlet pipe.
在一种可能的进一步实施方式中,中间筒体的中部通过电解液体进口管连接电解液体进口法兰。In a possible further embodiment, the middle part of the intermediate cylinder is connected to the electrolyte liquid inlet flange through the electrolyte liquid inlet pipe.
在一种可能的实施方式中,下部椭圆封头还通过液体出口管连接有液体出口法兰。In a possible embodiment, the lower elliptical head is also connected with a liquid outlet flange through a liquid outlet pipe.
在一种可能的进一步实施方式中,中间筒体的内部还设置有滤网,滤网安装在加热组件外侧,位于电解液体进口管上侧,同时要低于顶部的气体出口管。In a possible further embodiment, a filter screen is also provided inside the intermediate cylinder, and the filter screen is installed outside the heating assembly, located on the upper side of the electrolyte liquid inlet pipe, and is lower than the gas outlet pipe at the top.
优选地,加热丝位于接线盒的部分连接电线,所述电线通过所述接线孔连接电源。Preferably, the part of the heating wire located in the junction box is connected to the electric wire, and the electric wire is connected to the power source through the connection hole.
本发明的有益效果:Beneficial effects of the present invention:
1)集成化程度高。将电加热装置与气液分离装置组合在一起,通过电加热装置直接给电解液体加热,使电解水制氢设备快速升温,并且可通过调整加热丝的加热功率,控制设备温度。1) High degree of integration. The electric heating device is combined with the gas-liquid separation device, and the electrolytic liquid is directly heated by the electric heating device, so that the electrolyzed water hydrogen production equipment can be heated rapidly, and the temperature of the equipment can be controlled by adjusting the heating power of the heating wire.
2)分离效果好。设备内部设有滤网,能将较高温度下形成的氢气中的水雾凝结,提高了气液分离的效果。2) The separation effect is good. There is a filter screen inside the equipment, which can condense the water mist in the hydrogen gas formed at a higher temperature and improve the effect of gas-liquid separation.
附图说明Description of drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其它的附图。In order to illustrate the technical solutions of the embodiments of the present invention more clearly, the following briefly introduces the accompanying drawings used in the description of the embodiments. Obviously, the drawings in the following description are only some embodiments of the present invention. For those of ordinary skill in the art, other drawings can also be obtained from these drawings without any creative effort.
图1为本发明实施例提供的一种可电加热式气液分离器的结构示意图;1 is a schematic structural diagram of an electrically heated gas-liquid separator provided by an embodiment of the present invention;
附图标记说明:Description of reference numbers:
1-气体出口法兰,2-气体出口管,3-上部椭圆封头,4-滤网,5-电解液体进口法兰,6-电解液体进口管,7-中间筒体,8-下部椭圆封头,9-固定法兰,10-法兰盖,11-接线盒,12-接线孔,13-液体出口法兰,14-液体出口管,15-筒体,16-加热丝,17-椭圆封头。1-gas outlet flange, 2-gas outlet pipe, 3-upper oval head, 4-filter screen, 5-electrolyte liquid inlet flange, 6-electrolyte liquid inlet pipe, 7-intermediate cylinder, 8-lower oval Head, 9-Fixed flange, 10-Flange cover, 11-Terminal box, 12-Wiring hole, 13-Liquid outlet flange, 14-Liquid outlet pipe, 15-Cylinder body, 16-Heating wire, 17- Oval head.
具体实施方式Detailed ways
本发明的说明书实施例和权利要求书及附图中的术语“第一”、“第二”等是用于区别类似的对象,而不必用于描述特定的顺序或先后次序。此外,术语“包括”和“具有”以及他们的任何变形,意图在于覆盖不排他的包含,例如,包含了一系列步骤或单元。方法、系统、产品或设备不必限于清楚地列出的那些步骤或单元,而是可包括没有清楚地列出的或对于这些过程、方法、产品或设备固有的其它步骤或单元。The terms "first", "second" and the like in the description embodiments and claims of the present invention and the drawings are used to distinguish similar objects, and are not necessarily used to describe a specific order or sequence. Furthermore, the terms "comprising" and "having" and any variations thereof, are intended to cover non-exclusive inclusion, eg, comprising a series of steps or elements. A method, system, product or device is not necessarily limited to those steps or units expressly listed, but may include other steps or units not expressly listed or inherent to the process, method, product or device.
下面结合附图和实施例,对本发明的技术方案做进一步的详细描述。The technical solutions of the present invention will be described in further detail below with reference to the accompanying drawings and embodiments.
如图1,本发明实施例提供一种可电加热式气液分离器,包括加热组件和和位于加热组件外部的气液分离组件。As shown in FIG. 1 , an embodiment of the present invention provides an electrically heatable gas-liquid separator, which includes a heating component and a gas-liquid separation component located outside the heating component.
加热组件包括保护壳体、法兰盖10及固定法兰9和加热丝16。The heating assembly includes a protective casing, a
保护壳体包括筒体15和椭圆封头17,椭圆封头17连接在筒体15的顶端,筒体15的底端连接固定法兰9,固定法兰9的底面连接有法兰盖10,法兰盖10下方固定有接线盒11,接线盒11上设置有接线孔12,筒体15的内部设置有加热丝16,加热丝16呈倒U型,加热丝16的底端穿过法兰盖10进入到接线盒11内,加热丝16固定在法兰盖10上。The protective shell includes a
气液分离组件包括外部壳体,外部壳体包括中间筒体7和位于中间筒体7上下两端的上部椭圆封头3和下部椭圆封头8,其中,上部椭圆封头3上方通过气体出口管2连接有气体出口法兰1,中间筒体7的中部通过电解液体进口管6连接有电解液体进口法兰5,保护壳体的大部分穿过下部椭圆封头8伸入中间筒体7内,下部椭圆封头8还通过液体出口管14连接有液体出口法兰13。分离出的氢气从顶部的气体出口离开,电解液体从下部的液体出口法兰13离开。The gas-liquid separation assembly includes an outer casing, and the outer casing includes a
在一个示例中,中间筒体7的内部还设置有滤网4,滤网4安装在加热组件外侧,位于电解液体进口管6上侧,同时要低于顶部的气体出口,氢气中所含的水雾经过滤网4过滤,从而凝结落下。In one example, a filter screen 4 is also provided inside the
在一个示例中,电源通过接入加热丝16给设备加热,加热温度可在30℃-100℃范围内调整。In one example, the power supply heats the device by connecting the
保护壳体具有良好的传热效果,并将加热丝16与气体、液体分离,保护加热组件,内部上侧凝结的液体可沿椭圆封头17边缘滑落至设备底部。The protective shell has good heat transfer effect, separates the
在一个示例中,电解液体进口管6高度需通过分离效果计算确定,从电解槽出来的液体从该管进入分离器内部,液体往下走,氢气往上走。In an example, the height of the electrolytic
下面结合附图进一步说明该设备的操作方法:The operation method of the device is further described below in conjunction with the accompanying drawings:
1)提前将电线穿过接线孔12,在接线盒11内与加热丝16连接。1) Pass the wire through the
2)将该设备立直安装于电解水制氢处理框架上,电解液体进口法兰5与电解槽液体出口侧连接,液体出口法兰13与电解槽液体进口侧连接,气体出口法兰1与氢气处理后续设备连接。2) The device is installed upright on the electrolysis water hydrogen production processing frame, the electrolytic liquid inlet flange 5 is connected with the liquid outlet side of the electrolytic cell, the
3)打开电解水制氢装置,使电解液体量到达可加热式气液分离器指定液位,接通加热丝电源,给电解液体加热。3) Turn on the electrolytic water hydrogen production device, make the amount of electrolytic liquid reach the specified liquid level of the heatable gas-liquid separator, connect the heating wire power supply, and heat the electrolytic liquid.
4)接通电解槽电源,开始电解制氢。4) Turn on the power of the electrolyzer and start electrolysis to produce hydrogen.
本发明的优点在于:The advantages of the present invention are:
1)集成化程度高。将电加热装置与气液分离装置组合在一起,通过电加热装置直接给电解液体加热,使电解水制氢设备快速升温,并且可通过调整加热丝的加热功率,控制设备温度。1) High degree of integration. The electric heating device is combined with the gas-liquid separation device, and the electrolytic liquid is directly heated by the electric heating device, so that the electrolyzed water hydrogen production equipment can be heated rapidly, and the temperature of the equipment can be controlled by adjusting the heating power of the heating wire.
2)分离效果好。设备内部设有滤网,能将较高温度下形成的氢气中的水雾凝结,提高了气液分离的效果。2) The separation effect is good. There is a filter screen inside the equipment, which can condense the water mist in the hydrogen gas formed at a higher temperature and improve the effect of gas-liquid separation.
以上的具体实施方式,对本发明的目的、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上仅为本发明的具体实施方式而已,并不用于限定本发明的保护范围,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above specific embodiments further describe the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above are only specific embodiments of the present invention, and are not intended to limit the protection scope of the present invention. Within the spirit and principle of the present invention, any modifications, equivalent replacements, improvements, etc. made should be included within the protection scope of the present invention.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911079380.1A CN110681176A (en) | 2019-11-07 | 2019-11-07 | An electrically heated gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911079380.1A CN110681176A (en) | 2019-11-07 | 2019-11-07 | An electrically heated gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110681176A true CN110681176A (en) | 2020-01-14 |
Family
ID=69115593
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911079380.1A Pending CN110681176A (en) | 2019-11-07 | 2019-11-07 | An electrically heated gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110681176A (en) |
Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002007852A2 (en) * | 2000-07-20 | 2002-01-31 | Proton Energy Systems | Gas/liquid phase separator for electrolysis cell |
| WO2007132035A1 (en) * | 2006-05-16 | 2007-11-22 | Diewersol, S.L. | Equipment and method for obtaining gases by means of the electrolysis of water |
| CN101408358A (en) * | 2007-10-12 | 2009-04-15 | 孔德凯 | Method and equipment for preparing clean energy of low price and high efficiency |
| CN202410249U (en) * | 2011-12-31 | 2012-09-05 | 重庆明珠机电有限公司 | Heating-type liquid-gas separating device |
| CN104388971A (en) * | 2014-10-22 | 2015-03-04 | 苏州竞立制氢设备有限公司 | Comprehensive treatment device for hydrogen manufacturing equipment through water electrolysis |
| CN204478603U (en) * | 2014-12-31 | 2015-07-15 | 广东美的制冷设备有限公司 | Gas-liquid separator and there is its compressor |
| CN105498065A (en) * | 2014-10-16 | 2016-04-20 | 林信湧 | Gas generator |
| CN105624026A (en) * | 2014-12-01 | 2016-06-01 | 中粮集团有限公司 | Low-carbon zero-emission circulating hydrogen preparing device |
| CN106075940A (en) * | 2016-08-24 | 2016-11-09 | 佛山科学技术学院 | Evaporator with central downcomer |
| FR3049876A1 (en) * | 2016-04-12 | 2017-10-13 | Commissariat Energie Atomique | GAS / LIQUID SEPARATION SYSTEM, OUTPUT APPLICATION OF (HIGH-TEMPERATURE WATER) CO-ELECTROLYSIS REACTOR (SOEC) OR FUEL CELL (SOFC) |
| CN108179436A (en) * | 2018-02-23 | 2018-06-19 | 张国强 | A kind of water-electrolytic hydrogen making equipment |
| CN211025197U (en) * | 2019-11-07 | 2020-07-17 | 北京中电丰业技术开发有限公司 | Electric heating type gas-liquid separator |
| CN213589781U (en) * | 2020-09-14 | 2021-07-02 | 北京中电丰业技术开发有限公司 | Gas-liquid separation device |
-
2019
- 2019-11-07 CN CN201911079380.1A patent/CN110681176A/en active Pending
Patent Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002007852A2 (en) * | 2000-07-20 | 2002-01-31 | Proton Energy Systems | Gas/liquid phase separator for electrolysis cell |
| WO2007132035A1 (en) * | 2006-05-16 | 2007-11-22 | Diewersol, S.L. | Equipment and method for obtaining gases by means of the electrolysis of water |
| EP2034053A1 (en) * | 2006-05-16 | 2009-03-11 | Diewersol, S.L. | Equipment and method for obtaining gases by means of the electrolysis of water |
| CN101408358A (en) * | 2007-10-12 | 2009-04-15 | 孔德凯 | Method and equipment for preparing clean energy of low price and high efficiency |
| CN202410249U (en) * | 2011-12-31 | 2012-09-05 | 重庆明珠机电有限公司 | Heating-type liquid-gas separating device |
| CN105498065A (en) * | 2014-10-16 | 2016-04-20 | 林信湧 | Gas generator |
| CN104388971A (en) * | 2014-10-22 | 2015-03-04 | 苏州竞立制氢设备有限公司 | Comprehensive treatment device for hydrogen manufacturing equipment through water electrolysis |
| CN105624026A (en) * | 2014-12-01 | 2016-06-01 | 中粮集团有限公司 | Low-carbon zero-emission circulating hydrogen preparing device |
| CN204478603U (en) * | 2014-12-31 | 2015-07-15 | 广东美的制冷设备有限公司 | Gas-liquid separator and there is its compressor |
| FR3049876A1 (en) * | 2016-04-12 | 2017-10-13 | Commissariat Energie Atomique | GAS / LIQUID SEPARATION SYSTEM, OUTPUT APPLICATION OF (HIGH-TEMPERATURE WATER) CO-ELECTROLYSIS REACTOR (SOEC) OR FUEL CELL (SOFC) |
| CN106075940A (en) * | 2016-08-24 | 2016-11-09 | 佛山科学技术学院 | Evaporator with central downcomer |
| CN108179436A (en) * | 2018-02-23 | 2018-06-19 | 张国强 | A kind of water-electrolytic hydrogen making equipment |
| CN211025197U (en) * | 2019-11-07 | 2020-07-17 | 北京中电丰业技术开发有限公司 | Electric heating type gas-liquid separator |
| CN213589781U (en) * | 2020-09-14 | 2021-07-02 | 北京中电丰业技术开发有限公司 | Gas-liquid separation device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201296751Y (en) | Device for experimentally distilling liquor produced by solid fermentation | |
| CN207659530U (en) | Water electrolysis hydrogen production oxygen unit | |
| CN204756868U (en) | High voltage electrode boiler | |
| CN206199023U (en) | A kind of distillation device of carrying vapour mechanical compress | |
| CN105883950B (en) | A kind of water purifying cup | |
| CN211025197U (en) | Electric heating type gas-liquid separator | |
| CN202881432U (en) | Electroplating heating device | |
| CN110681176A (en) | An electrically heated gas-liquid separator | |
| CN101311318B (en) | Sealing device of solid oxide electrolytic cell for high-temperature electrolytic hydrogen production and sealing method thereof | |
| CN201930645U (en) | Spiral air-lift type steam separator | |
| CN109338392A (en) | A kind of Integrated Processing Unit of hydro-electrolytic hydrogen production device | |
| CN109368896B (en) | Impurity removal device for recovery of dichloromethane | |
| CN207210346U (en) | A kind of gas-liquid separation device | |
| CN207525196U (en) | A kind of deacidifying device convenient for later collection chlorinated paraffin | |
| CN205233344U (en) | Electrolytic negative pressure low temperature boiling milk drying device | |
| CN106479668B (en) | A device for extracting star anise oil with negative pressure circulating water | |
| CN214880202U (en) | System for utilize liquid metal schizolysis natural gas hydrogen manufacturing | |
| CN205990435U (en) | A kind of heat treatment device for aluminum alloy hub | |
| CN209506654U (en) | A kind of storage tank for biodiesel preparation | |
| CN214781579U (en) | Device for recovering hexamethylcyclotrisiloxane in vented hot gas | |
| CN208995147U (en) | A polysilicon reduction furnace | |
| CN208562545U (en) | A kind of household hydrogen gas generation device | |
| CN106433963B (en) | Device for extracting cinnamon oil by using pressure-reducing circulating water | |
| CN208312341U (en) | A kind of high-efficient steam generator based on large area heat transfer | |
| CN222889397U (en) | An oil, gas, natural gas and glycol electric heating dehydration device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200114 |