CN106784952A - A kind of method that utilization can expand the electricity production decontamination of continuous stream microbiological fuel cell - Google Patents
A kind of method that utilization can expand the electricity production decontamination of continuous stream microbiological fuel cell Download PDFInfo
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- 239000000446 fuel Substances 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title claims abstract description 27
- 230000005611 electricity Effects 0.000 title claims abstract description 25
- 238000005202 decontamination Methods 0.000 title claims abstract description 9
- 230000003588 decontaminative effect Effects 0.000 title claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 title description 4
- 230000002906 microbiologic effect Effects 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 230000000813 microbial effect Effects 0.000 claims abstract description 24
- 239000010865 sewage Substances 0.000 claims abstract description 20
- 244000005700 microbiome Species 0.000 claims abstract description 8
- 239000005416 organic matter Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 16
- 239000004020 conductor Substances 0.000 claims description 12
- 239000011810 insulating material Substances 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- 239000012528 membrane Substances 0.000 claims description 8
- 238000007789 sealing Methods 0.000 claims description 8
- 238000006555 catalytic reaction Methods 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 239000003575 carbonaceous material Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims description 2
- 230000009471 action Effects 0.000 abstract description 2
- 239000010405 anode material Substances 0.000 abstract description 2
- 239000010406 cathode material Substances 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 108091006146 Channels Proteins 0.000 description 38
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000002154 agricultural waste Substances 0.000 description 2
- 239000004035 construction material Substances 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 102000010637 Aquaporins Human genes 0.000 description 1
- 108010063290 Aquaporins Proteins 0.000 description 1
- 241001464837 Viridiplantae Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/16—Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/005—Combined electrochemical biological processes
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- H—ELECTRICITY
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- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
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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
- 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
- Y02E60/50—Fuel cells
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Abstract
本发明公开了一种利用可拓展连续流微生物燃料电池产电除污的方法,预处理水流通过进水口连续流入阳极室,进而流经所有阳极室,水中有机物在微生物催化作用下产生电子和质子,质子以阳极室间流道中的水流为载体迁移至阳极室,通过小孔涌进阴极室,使得阳极室组与阴极室组在装置内部电性连通,电子通过阳极室底部外接线路通道流经负载到达阴极,并使燃料电池装置在净化污水的同时产生电能。本发明可以根据实际需求进行无限扩充,阴极和阳极材料及其安装形式可以根据要求进行变换,使污水得以净化,同时产电。
The invention discloses a method for electricity generation and decontamination using an expandable continuous flow microbial fuel cell. The pretreated water flows continuously into the anode chamber through the water inlet, and then flows through all the anode chambers. The organic matter in the water generates electrons and protons under the action of microorganisms. , the protons migrate to the anode chamber with the water flow in the flow channel between the anode chambers as the carrier, and rush into the cathode chamber through the small hole, so that the anode chamber group and the cathode chamber group are electrically connected inside the device, and the electrons flow through the external circuit channel at the bottom of the anode chamber The load reaches the cathode and enables the fuel cell device to generate electricity while purifying sewage. The invention can be infinitely expanded according to actual needs, and the cathode and anode materials and their installation forms can be changed according to requirements, so that sewage can be purified and electricity can be generated at the same time.
Description
技术领域technical field
本发明涉及一种利用可拓展连续流微生物燃料电池产电除污的方法。The invention relates to a method for electricity generation and decontamination using an expandable continuous flow microbial fuel cell.
背景技术Background technique
微生物燃料电池是一种利用微生物将有机物中的化学能直接转化成电能的装置。微生物燃料电池的基本工作原理是:在阳极室厌氧环境下,有机物在微生物作用下分解并释放出电子和质子,电子依靠合适的电子传递介体在生物组分和阳极之间进行有效传递,并通过外电路传递到阴极形成电流,而质子通过质子交换膜等中间传递物质传递到阴极,氧化剂( 一般为氧气) 在阴极得到电子被还原并与质子结合成水。微生物燃料电池多采用双室型,即包括阳极室和阴极室,中间常采用质子交换膜隔开。虽然目前随着微生物燃料电池电极和反应器构型的不断改进,其单体能量密度增长迅速,但是仍然存在以下问题:电池能量密度低;可用作底物废水种类较为单一;电池多为间歇式工作,需要不断更换基底;电极材料结构单一,产电微生物量少,不利于能量产生;电池反应器装置结构复杂且不可扩充;各电池组间不能根据需求进行串并联,严重限制其实际推广与应用。A microbial fuel cell is a device that uses microorganisms to directly convert chemical energy in organic matter into electrical energy. The basic working principle of microbial fuel cell is: in the anaerobic environment of the anode chamber, the organic matter is decomposed under the action of microorganisms and releases electrons and protons, and the electrons rely on suitable electron transfer mediators to effectively transfer between the biological components and the anode. And it is transmitted to the cathode through an external circuit to form a current, and the proton is transmitted to the cathode through an intermediate transfer material such as a proton exchange membrane, and the oxidant (usually oxygen) obtains electrons at the cathode and is reduced and combined with the proton to form water. Microbial fuel cells mostly adopt a double-chamber type, that is, including an anode chamber and a cathode chamber, which are often separated by a proton exchange membrane. Although at present, with the continuous improvement of the electrode and reactor configuration of microbial fuel cells, the energy density of its monomers is increasing rapidly, but there are still the following problems: the battery energy density is low; the types of waste water that can be used as substrates are relatively single; most of the batteries are intermittent. The structure of the electrode material is single, and the amount of microorganisms producing electricity is small, which is not conducive to energy production; the structure of the battery reactor device is complex and cannot be expanded; the battery packs cannot be connected in series and parallel according to the demand, which seriously limits its practical application. with application.
发明内容Contents of the invention
本发明的目的是为了克服以上的不足,提供一种利用可拓展连续流微生物燃料电池产电除污的方法。The purpose of the present invention is to overcome the above disadvantages and provide a method for electricity generation and decontamination using an expandable continuous flow microbial fuel cell.
本发明的技术方案是:一种利用可拓展连续流微生物燃料电池产电除污的方法,包括相间排布的阳极室和阴极室,阳极室内或阴极室内可安装不同材料电极,阳极室之间相通,阴极室之间相通,其中至少一组阳极室与阴极室之间相通,通道中均设有滤网,阳极室和阴极室外壳侧壁分别开有进水口和出水口,用于输入和排出有机污水,各阴、阳极室底部安装有导电线路,连通各阴阳极室与外负载,阴极室与外界空气连通,促进阴极反应,阳极和阴极电极皆为导电材料,电极浸没于流水中,阳极室外接导线连接为一体,与阴极室外接导线构成串联外接电路,预处理水流通过进水口连续流入阳极室,进而流经所有阳极室,水中有机物在微生物催化作用下产生电子和质子,质子以阳极室间流道中的水流为载体迁移至阳极室,通过小孔涌进阴极室,使得阳极室组与阴极室组在装置内部电性连通,电子通过阳极室底部外接线路通道流经负载到达阴极,并使燃料电池装置在处理污水的同时产生电能。该方法中的阳极室和阴极室皆为大小相等的正方体、相间排布并组合构成一个长方体装置,阳极室数目大于等于阴极室数目。The technical solution of the present invention is: a method for electricity generation and decontamination using an expandable continuous flow microbial fuel cell, comprising anode chambers and cathode chambers arranged alternately, electrodes of different materials can be installed in the anode chamber or cathode chamber, and the anode chambers The cathode chambers communicate with each other, at least one group of anode chambers communicates with the cathode chambers, filters are provided in the channels, and the side walls of the anode chamber and the cathode chamber are respectively provided with water inlets and water outlets for input and The organic sewage is discharged. Conductive lines are installed at the bottom of each cathode and anode chamber, connecting each cathode and anode chamber with the external load, and the cathode chamber is connected with the outside air to promote the cathode reaction. Both the anode and cathode electrodes are conductive materials, and the electrodes are immersed in running water. The connecting wires outside the anode chamber are connected as a whole, forming a series connection circuit with the connecting wires outside the cathode chamber. The pretreated water flows into the anode chamber continuously through the water inlet, and then flows through all the anode chambers. The water flow in the flow channel between the anode chambers migrates to the anode chamber as a carrier, and flows into the cathode chamber through small holes, so that the anode chamber group and the cathode chamber group are electrically connected within the device, and the electrons flow through the load through the external circuit channel at the bottom of the anode chamber to reach the cathode , and make the fuel cell device generate electricity while treating sewage. The anode chambers and cathode chambers in the method are cubes of equal size, arranged alternately and combined to form a cuboid device, and the number of anode chambers is greater than or equal to the number of cathode chambers.
本发明还公开了一种正多边形可拓展空气阴极微生物燃料电池装置,包括相装置外壳、装置密封盖及相间排布的阳极室和阴极室,阳极室内或阴极室内安装不同材料电极,阳极室间或阴极室间通过带滤网的流道连通,各流道旁设有挡板,各挡板可上下活动,阳极室间流道与阴极室间流道上下错开设置,其中至少一组处于装置最外侧相邻的阳极室与阴极室之间通过带挡板的小孔连通,各挡板可上下活动,小孔可以通过安装质子交换膜阻隔阳极液与阴极液,与之相对的一组处于装置最外侧相邻的阳极室和阴极室外壳侧壁分别开有进水口和出水口,用于输入和排出有机污水,装置外壳在各阴阳极室底部安装有导电线路,连通各阴阳极室与外负载,阳极室外接导线连接为一体,与阴极室外接导线进行串联构成外接电路,装置密封盖在阴极室上方开有小孔,使得阴极室与外界空气连通,促进阴极反应。The invention also discloses a regular polygon expandable air cathode microbial fuel cell device, which includes a phase device casing, a device sealing cover, and an anode chamber and a cathode chamber arranged alternately. Electrodes of different materials are installed in the anode chamber or cathode chamber, and the anode chamber or The cathode chambers are connected through flow passages with filter screens, and baffles are arranged beside each flow passage, and each baffle can move up and down. The adjacent anode chamber and cathode chamber on the outside are connected through small holes with baffles. Each baffle can move up and down. The small holes can block the anolyte and catholyte by installing a proton exchange membrane. The opposite group is in the device The side walls of the anode chamber and cathode chamber adjacent to the outermost side are respectively provided with a water inlet and a water outlet for inputting and discharging organic sewage. The device casing is equipped with conductive lines at the bottom of each cathode and anode chamber to connect each cathode and anode chamber with the outside. The load and the external wires outside the anode are connected as a whole, and connected in series with the external wires outside the cathode chamber to form an external circuit. The sealing cover of the device has a small hole above the cathode chamber, so that the cathode chamber communicates with the outside air and promotes the cathode reaction.
阳极室和阴极室皆为大小相等的正多边形棱柱、二者相间排布并组合构成一个多边形棱柱装置,装置可以适应不同形状场地,阳极室数目大于等于所述阴极室数目。阳极室间或阴极室间通过带滤网的流道连通,各流道旁设有挡板,各挡板可上下活动,阳极室间流道与阴极室间流道上下错开设置。至少一组处于装置最外侧相邻的阳极室与阴极室之间通过带挡板的小孔连通,各挡板可上下活动,小孔可以通过安装质子交换膜阻隔阳极液与阴极液。若阳极室侧壁和底部基底材料皆为绝缘材料,底层设有导线接口,连接阳极电极和外电路。若阳极室侧壁材料为绝缘材料,底部基底材料上层为导电材料,则下层为绝缘材料,导线接口贯穿底部上下层,连接阳极电极和外电路。阴极室底层设有导线接口,连接阳极电极和外电路。阳极和阴极电极为碳刷、碳布、碳纸、活性炭颗粒等碳基材料,或是具有较好生物相容性的导电材料,或是生物阴极,电极浸没于流水中,电极最小单位的最小直径大于流道滤网最大口径。阳极室外接导线可以连接为一体,与阴极室外接导线构成串联外接电路。电池装置也可以将相邻阴阳极外接导线连接构成单一电池组,并将多个单一电池组并联得到最大外接电路电流。所述电池装置可以将相邻阴阳极室外接导线通过外电路连接构成单一电池组,并可以将多个单一电池组进行自由串并联,以达到不同输出效果。有机污水作为基底材料可以选用生活污水、工业废水和农业废弃物。Both the anode chamber and the cathode chamber are regular polygonal prisms of equal size, and they are arranged alternately and combined to form a polygonal prism device. The device can adapt to different shapes of sites, and the number of anode chambers is greater than or equal to the number of cathode chambers. The anode chambers or cathode chambers are connected through flow channels with filter screens, and baffles are arranged beside each flow channel, and each baffle plate can move up and down, and the flow channels between the anode chambers and the flow channels between the cathode chambers are staggered up and down. At least one group of adjacent anode chambers and cathode chambers on the outermost side of the device are connected through small holes with baffles, each baffle can move up and down, and the small holes can block anolyte and catholyte by installing a proton exchange membrane. If both the side wall of the anode chamber and the base material of the bottom are insulating materials, the bottom layer is provided with a wire interface to connect the anode electrode and the external circuit. If the material of the side wall of the anode chamber is insulating material, the upper layer of the bottom base material is conductive material, the lower layer is insulating material, and the wire interface runs through the upper and lower layers of the bottom to connect the anode electrode and the external circuit. The bottom layer of the cathode chamber is provided with a wire interface to connect the anode electrode and the external circuit. The anode and cathode electrodes are carbon-based materials such as carbon brushes, carbon cloth, carbon paper, and activated carbon particles, or conductive materials with good biocompatibility, or biological cathodes. The electrodes are immersed in running water, and the smallest unit of the electrode is the smallest The diameter is larger than the maximum diameter of the flow channel filter. The external lead wires outside the anode can be connected as a whole to form a series external circuit with the external lead wires outside the cathode. The battery device can also connect adjacent cathode and anode external wires to form a single battery pack, and multiple single battery packs can be connected in parallel to obtain the maximum external circuit current. The battery device can form a single battery pack by connecting adjacent cathode and anode external wires through an external circuit, and can freely connect multiple single battery packs in series and parallel to achieve different output effects. Organic sewage can be used as the base material for domestic sewage, industrial wastewater and agricultural waste.
本发明与现有技术相比的有益效果是:1)采用连续流工作模式,结构简单,不需要人工更换基底材料,大大降低电池内阻和制造维护成本,提高能源利用效率和电池能量密度;2) 以生活污水、工业废水、农业废弃物或禽畜废弃物等各类有机污水为基质,在净化污水的同时产生电能;3) 以具有较好生物相容性的导电材料或者绿色植物为电极材料,不仅价格低廉,而且产电过程中吸收二氧化碳,排出氧气,促进阴极反应的同时减少污染,是一种清洁能源生产装置;4)电池装置可根据实际应用需求进行尺寸调整,以使得整体外形适应不能形状外部环境,并可无限扩充,实际应用价值大;5)可以将相邻阴阳极外接导线连接构成单一电池组,并可以将多个单一电池组进行自由串并联,以达到不同输出效果。Compared with the prior art, the present invention has the following beneficial effects: 1) Adopting the continuous flow working mode, the structure is simple, the base material does not need to be manually replaced, the internal resistance of the battery and the cost of manufacturing and maintenance are greatly reduced, and the energy utilization efficiency and energy density of the battery are improved; 2) Use various organic sewage such as domestic sewage, industrial wastewater, agricultural waste or livestock waste as the substrate to generate electricity while purifying sewage; 3) Use conductive materials or green plants with good biocompatibility as the substrate The electrode material is not only cheap, but also absorbs carbon dioxide and emits oxygen in the process of electricity generation, and promotes the cathode reaction while reducing pollution. It is a clean energy production device; 4) The size of the battery device can be adjusted according to the actual application requirements, so that the overall The shape adapts to the external environment, and can be expanded infinitely, with great practical application value; 5) The adjacent cathode and anode external wires can be connected to form a single battery pack, and multiple single battery packs can be freely connected in series and parallel to achieve different outputs. Effect.
附图说明:Description of drawings:
图1为本发明中使用的奇数外壳的结构示意图。Fig. 1 is a schematic structural diagram of odd-numbered shells used in the present invention.
图2为本发明中使用的偶数外壳的结构示意图。Fig. 2 is a schematic structural diagram of an even-numbered shell used in the present invention.
图3为发明中阳极室和阴极室均为正三角形棱柱的局部立体结构示意图;Fig. 3 is the partial three-dimensional structure schematic diagram that anode chamber and cathode chamber are regular triangular prisms in the invention;
图4为发明中阳阳极室和阴极室均为正五边形棱柱的结构示意图;Fig. 4 is the structure schematic diagram that anode chamber and cathode chamber are regular pentagonal prisms in the invention;
图1中标号:1-阳极室(a-h)、2-阴极室(a-h)、3-装置外壳、4-阳极室间流道、5-阴极室间流道、6-流道两侧滤网、7-进水口、8-出水口、9-一组阴阳极室间通孔、10-外接线路通道、11-微生物燃料电池装置密封盖、12-密封盖上阴极室上方对应通孔、13-挡板;Labels in Figure 1: 1-anode chamber (a-h), 2-cathode chamber (a-h), 3-device shell, 4-flow channel between anode chambers, 5-flow channel between cathode chambers, 6-filters on both sides of the flow channel , 7-water inlet, 8-water outlet, 9-a group of through holes between cathode and anode chambers, 10-external line channel, 11-microbial fuel cell device sealing cover, 12-corresponding through hole above the cathode chamber on the sealing cover, 13 - baffles;
图中“+”代表阳极室,“-”代表阴极室。"+" in the figure represents the anode chamber, and "-" represents the cathode chamber.
具体实施方式:detailed description:
为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。在本发明的一种实施方式中描述的元素和特征可以与一个或更多个其它实施方式中示出的元素和特征相结合。应当注意,为了清楚的目的,说明中省略了与本发明无关的、本领域普通技术人员已知的部件和处理的表示和描述。基于本发明中的实施例,本领域普通技术人员在没有付出创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are part of the embodiments of the present invention, not all of them. the embodiment. Elements and features described in one embodiment of the present invention may be combined with elements and features shown in one or more other embodiments. It should be noted that representation and description of components and processes that are not related to the present invention and that are known to those of ordinary skill in the art are omitted from the description for the purpose of clarity. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
下面就本实施方式的一种利用可拓展连续流微生物燃料电池产电除污的方法的使用方法进行详细的说明。The following will describe in detail the usage method of a method for electricity generation and decontamination using an expandable continuous flow microbial fuel cell in this embodiment.
[第一实施方式] [first embodiment]
本实施方式的微生物燃料电池装置外壳的一个例子如图1所示,包括阳极室1(a-e)、阴极室2(a-d)、装置外壳3、阳极室间流道4、阴极室间流道5、流道两侧滤网6、进水口7、出水口8、一组阴阳极室间通孔9和外接线路通道10。 An example of the housing of the microbial fuel cell device in this embodiment is shown in Figure 1, including an anode chamber 1 (a-e), a cathode chamber 2 (a-d), a device housing 3, a flow channel 4 between the anode chambers, and a flow channel 5 between the cathode chambers , filter screens 6 on both sides of the flow channel, water inlet 7, water outlet 8, a group of through holes 9 between the cathode and anode chambers and an external circuit channel 10.
阳极室1(a-e)或阴极室2(a-d)皆为大小相等的正方体、相间排布并组合构成一个3×3长方体九宫格的装置外壳3,阳极室数目大于阴极室数目。阳极室1(a-e)间通过流道4连通,所述阴极室2(a-d)间通过流道5连通,阳极室间流道4与阴极室间流道5上下错开设置,阳极室间流道4和阴极室间流道5两侧均设有滤网6,其中处于装置最外侧相邻的阳极室1(b)与阴极室2(a)之间通过小孔9连通,与之相对的一组处于装置最外侧相邻的阳极室1(d)和阴极室2(d)外壳侧壁分别开有进水口7和出水口8,使得电池装置可以连续运行。阳极室侧壁和底部基底材料皆为绝缘材料,底层设有导线接口10,连接阳极电极和外电路。阳极和阴极电极皆为碳刷,构建材料阳极,电极浸没于流水中。阳极室外接导线连接为一体,与阴极室外接导线构成串联外接电路。预处理水流通过进水口7连续流入阳极室1(d),进而流经所有阳极室,水中有机物在微生物催化作用下产生电子和质子,质子以阳极室间流道4中的水流为载体迁移至阳极室1(b),通过小孔9涌进阴极室2(a),使得阳极室组与阴极室组在装置内部电性连通,电子通过阳极室底部外接线路通道10流经负载到达阴极,并使燃料电池装置在处理污水的同时产生电能。装置密封盖对应阴极中心处开有通孔用以连接外界氧气,促进阴极反应。Anode chambers 1 (a-e) or cathode chambers 2 (a-d) are cubes of equal size, arranged alternately and combined to form a 3×3 rectangular parallelepiped nine-square device housing 3, and the number of anode chambers is greater than the number of cathode chambers. The anode chambers 1 (a-e) are connected through the flow channel 4, and the cathode chambers 2 (a-d) are connected through the flow channel 5. The flow channel 4 between the anode chambers and the flow channel 5 between the cathode chambers are staggered up and down, and the flow channel between the anode chambers 4 and both sides of the flow channel between the cathode chambers 5 are provided with filter screens 6, wherein the anode chamber 1 (b) adjacent to the outermost side of the device communicates with the cathode chamber 2 (a) through a small hole 9, and the opposite A group of anode chamber 1(d) and cathode chamber 2(d) adjacent to the outermost side of the device are provided with water inlet 7 and water outlet 8 respectively, so that the battery device can run continuously. Both the side wall of the anode chamber and the base material of the bottom are insulating materials, and the bottom layer is provided with a wire interface 10 for connecting the anode electrode and the external circuit. Both the anode and cathode electrodes are carbon brushes, the construction material is the anode, and the electrodes are immersed in running water. The connecting wire outside the anode is connected as a whole, and forms a series connecting circuit with the connecting wire outside the cathode. The pretreated water flows continuously into the anode chamber 1 (d) through the water inlet 7, and then flows through all the anode chambers. The organic matter in the water generates electrons and protons under the catalysis of microorganisms, and the protons migrate to the The anode chamber 1 (b) flows into the cathode chamber 2 (a) through the small hole 9, so that the anode chamber group and the cathode chamber group are electrically connected within the device, and the electrons flow through the external circuit channel 10 at the bottom of the anode chamber to reach the cathode. And make the fuel cell device generate electricity while treating the sewage. The sealing cover of the device is provided with a through hole corresponding to the center of the cathode to connect the external oxygen to promote the cathode reaction.
由此实施方式可以推导出5×5长方体装置外壳、7×7长方体装置外壳……的结构,此结构统称为奇数外壳。From this embodiment, the structure of a 5×5 cuboid device casing, a 7×7 cuboid device casing, .
[第二实施方式] [Second Embodiment]
本实施方式的微生物燃料电池装置外壳的一个例子的俯视图如图2所示,对于与第一实施方式相同的构成标注相同的符号,并将重复的说明予以省略。 A plan view of an example of the housing of the microbial fuel cell device according to the present embodiment is shown in FIG. 2 , and the same components as those of the first embodiment are given the same reference numerals, and duplicate descriptions are omitted.
阳极室1(a-h)或阴极室2(a-h)皆为大小相等的正方体、相间排布并组合构成一个4*4长方体装置3,阳极室数目等于阴极室数目。阳极室1(a-h)间通过流道4连通,阴极室2(a-h)间通过流道5连通,阳极室间流道4与阴极室间流道5上下错开设置,阳极室间流道4和阴极室间流道5两侧均设有滤网6,其中处于装置最外侧相邻的阳极室1(b)与阴极室2(b)之间通过小孔9连通,与之相对的一组处于装置最外侧相邻的阳极室1(g)和阴极室2(g)外壳侧壁分别开有进水口7和出水口8,使得电池装置可以连续运行。阳极室侧壁材料为绝缘材料,底部基底材料上层为导电材料,下层为绝缘材料,导线接口10贯穿底部上下层,连接阳极电极和外电路。阳极为活性炭颗粒,构建材料阳极,电极浸没于流水中,所述阴极电极为生物阴极,可以产生氧气,促进所在阴极室反应,实现自给自足。电池装置将相邻阴阳极外接导线连接构成单一电池组,即1(a)与2(a)为一组、1(b)与2(b)为一组、1(c)与2(c)为一组……并将a-h组8个单一电池组并联得到最大外接电路电流。Anode chambers 1 (a-h) or cathode chambers 2 (a-h) are cubes of equal size, arranged alternately and combined to form a 4*4 cuboid device 3, the number of anode chambers is equal to the number of cathode chambers. The anode chambers 1 (a-h) are connected through the flow channel 4, and the cathode chambers 2 (a-h) are connected through the flow channel 5. The flow channel 4 between the anode chambers and the flow channel 5 between the cathode chambers are staggered up and down, and the flow channels 4 between the anode chambers and the Filter screens 6 are provided on both sides of the flow channel 5 between the cathode chambers, among which the anode chamber 1 (b) adjacent to the outermost side of the device communicates with the cathode chamber 2 (b) through a small hole 9 , and the opposite group The side walls of the anode chamber 1 (g) and cathode chamber 2 (g) adjacent to the outermost side of the device are respectively provided with a water inlet 7 and a water outlet 8, so that the battery device can run continuously. The material of the side wall of the anode chamber is insulating material, the upper layer of the base material of the bottom is conductive material, and the lower layer is insulating material. The wire interface 10 runs through the upper and lower layers of the bottom to connect the anode electrode and the external circuit. The anode is activated carbon particles, the anode is constructed of materials, and the electrode is immersed in running water. The cathode electrode is a biological cathode, which can generate oxygen, promote the reaction in the cathode chamber, and realize self-sufficiency. The battery device connects adjacent cathode and anode external wires to form a single battery pack, that is, 1(a) and 2(a) form a group, 1(b) and 2(b) form a group, 1(c) and 2(c) form a single battery pack. ) as a group...and connect 8 single battery packs in a-h group in parallel to obtain the maximum external circuit current.
本实施方式装置运行流程与第一实施方式类似,将重复说明予以省略。The operating flow of the device in this embodiment is similar to that in the first embodiment, and repeated descriptions will be omitted.
由此实施方式可以推导出6×6长方体装置外壳、8×8长方体装置外壳……的结构,此结构统称为偶数外壳。From this embodiment, the structures of 6×6 cuboid device casings, 8×8 cuboid device casings, . . .
[第三实施方式][Third Embodiment]
本实施方式的微生物燃料电池装置外壳的一个例子局部示意图如图3所示,包括多个正三角形棱柱的阳极室和正三角形棱柱的阴极室、阳极室间流道、阴极室间流道、各流道挡板和滤网、进水口、出水口、一组阴阳极室间通孔。 A partial schematic diagram of an example of the microbial fuel cell device housing of the present embodiment is shown in Figure 3, including anode chambers of a plurality of regular triangular prisms, cathode chambers of regular triangular prisms, flow channels between anode chambers, flow channels between cathode chambers, and flow channels between the cathode chambers. Channel baffle and filter screen, water inlet, water outlet, a group of through holes between cathode and anode chambers.
阳极室1或阴极室2皆为大小相等的正三角形棱柱,二者相间排布,阳极室1数目大于阴极室2数目。阳极室1内或阴极室2内安装不同材料电极,阳极室1间或阴极室2间通过带滤网6的流道连通,各流道旁设有挡板13,各挡板13可上下活动,阳极室间流道4与阴极室间流道5上下错开设置,其中一组处于装置最外侧相邻的阳极室1与阴极室2之间通过带小孔的挡板13连通,挡板13上的小孔中无质子交换膜阻隔阳极液与阴极液,与之相对的一组处于装置最外侧相邻的阳极室1和阴极室2外壳侧壁分别开有进水口7和出水口8,用于输入和排出有机污水,使得电池装置可以连续运行。装置密封盖在阴极室上方开有小孔,使得阴极室与外界空气连通,促进阴极反应。阳极室侧壁和底部基底材料皆为绝缘材料,底层设有导线接口,连接阳极电极和外电路。阳极和阴极电极皆为碳刷,构建材料阳极,电极浸没于流水中。所有阳极室外接导线连接为一体,与阴极室外接导线构成串联外接电路。预处理水流通过进水口连续流入阳极室,进而流经所有极室,下推挡板阻断所有阳极室间或者阴极室间通道,使得各极室内相关反应得以自我催化进行。一段时间后上拉挡板,使得污水得以连续流通,各极室基底得以更新。连通阳极室与阴极室的带小孔的挡板也随着上述阶段下推或上拉,水中有机物在微生物催化作用下产生电子和质子,质子以阳极室间流道中的水流为载体迁移至阳极室,并通过上拉挡板使得质子涌进阴极室,使得阳极室组与阴极室组在装置内部电性连通,电子通过阳极室底部外接线路通道流经负载到达阴极,并使燃料电池装置在处理污水的同时产生电能。Both the anode chamber 1 and the cathode chamber 2 are regular triangular prisms of equal size, and the two are arranged alternately, and the number of the anode chamber 1 is greater than that of the cathode chamber 2 . Electrodes of different materials are installed in the anode chamber 1 or the cathode chamber 2, and the anode chamber 1 or the cathode chamber 2 are connected through flow passages with filter screens 6, and baffles 13 are arranged beside each flow passage, and each baffle 13 can move up and down, The flow channels 4 between the anode chambers and the flow channels 5 between the cathode chambers are arranged staggered up and down, and one group of adjacent anode chambers 1 and cathode chambers 2 located at the outermost side of the device are communicated through a baffle plate 13 with a small hole. On the baffle plate 13 There is no proton exchange membrane in the small hole to block the anolyte and catholyte, and the side walls of the anode chamber 1 and cathode chamber 2 adjacent to the outermost side of the device are respectively provided with a water inlet 7 and a water outlet 8. It is used to input and discharge organic sewage, so that the battery device can run continuously. The sealing cover of the device has a small hole above the cathode chamber, so that the cathode chamber communicates with the outside air and promotes the cathode reaction. The side wall of the anode chamber and the base material of the bottom are all insulating materials, and the bottom layer is provided with a wire interface to connect the anode electrode and the external circuit. Both the anode and cathode electrodes are carbon brushes, the construction material is the anode, and the electrodes are immersed in running water. All the external conductors outside the anode are connected as a whole, and form a series external circuit with the external conductors outside the cathode. The pretreatment water flow continuously flows into the anode chamber through the water inlet, and then flows through all the pole chambers. Push down the baffle to block all the passages between the anode chambers or the cathode chambers, so that the relevant reactions in each pole chamber can be self-catalyzed. After a period of time, the baffle is pulled up so that the sewage can circulate continuously and the bases of each electrode chamber can be renewed. The baffle with small holes connecting the anode chamber and the cathode chamber is also pushed down or pulled up with the above-mentioned stages, and the organic matter in the water generates electrons and protons under the catalysis of microorganisms, and the protons migrate to the anode with the water flow in the flow channel between the anode chambers as the carrier. chamber, and the protons rush into the cathode chamber by pulling up the baffle, so that the anode chamber group and the cathode chamber group are electrically connected inside the device, and the electrons flow through the external line channel at the bottom of the anode chamber to reach the cathode through the load, and make the fuel cell device in Generating electricity while treating sewage.
[第四实施方式][Fourth Embodiment]
本实施方式的微生物燃料电池装置外壳的一个例子的俯视图如图4所示,对于与第一实施方式相同的构成标注相同的符号,并将重复的说明予以省略。 A plan view of an example of the housing of the microbial fuel cell device according to the present embodiment is shown in FIG. 4 , and the same components as those of the first embodiment are given the same reference numerals, and duplicate descriptions are omitted.
阳极室1或阴极室2皆为大小相等的正五边形棱柱相间排布,阳极室数目等于阴极室数目。阳极室间或阴极室间通过带滤网的流道连通,各流道旁设有挡板13,各挡板13可上下活动,阳极室间流道4与阴极室间流道5上下错开设置,其中多组阳极室1与阴极室2之间通过带小孔的挡板13连通,各挡板13可上下活动,挡板上的小孔中通过安装质子交换膜阻隔阳极液与阴极液,与之相对的一组处于装置最外侧相邻的阳极室和阴极室外壳侧壁分别开有进水口7和出水口8,用于输入和排出有机污水,使得电池装置可以连续运行。阳极室侧壁材料为绝缘材料,底部基底材料上层为导电材料,下层为绝缘材料,导线接口贯穿底部上下层,连接阳极电极和外电路。阳极为活性炭颗粒构建材料阳极,,电极浸没于流水中,阴极电极为生物阴极,可以产生氧气,促进所在阴极室反应,实现自给自足。预处理水流通过进水口连续流入阳极室,进而流经所有阳极室,水中有机物在微生物催化作用下产生电子和质子,质子以阳极室间流道中的水流为载体迁移至阳极室,再通过质子交换膜涌进阴极室,使得阳极室组与阴极室组在装置内部电性连通,电子通过阳极室底部外接线路通道流经负载到达阴极,并使燃料电池装置在处理污水的同时产生电能。本发明可以将相邻阴阳极外接导线连接构成单一电池组,并可以将多个单一电池组进行自由串并联,以达到不同输出效果。The anode chambers 1 and cathode chambers 2 are regular pentagonal prisms of equal size arranged alternately, and the number of anode chambers is equal to the number of cathode chambers. The anode chambers or cathode chambers are connected through flow passages with filter screens, and baffles 13 are arranged beside each flow passage, and each baffle 13 can move up and down, and the flow passages 4 between the anode chambers and the flow passages 5 between the cathode chambers are staggered up and down. Among them, multiple groups of anode chambers 1 and cathode chambers 2 are connected through baffle plates 13 with small holes, and each baffle plate 13 can move up and down. The small holes on the baffle plates are installed with proton exchange membranes to block the anolyte and catholyte. The opposite group of adjacent anode chamber and cathode chamber casing side walls on the outermost side of the device are respectively provided with water inlet 7 and water outlet 8 for input and discharge of organic sewage, so that the battery device can run continuously. The material of the side wall of the anode chamber is insulating material, the upper layer of the base material of the bottom is conductive material, and the lower layer is insulating material, and the wire interface runs through the upper and lower layers of the bottom to connect the anode electrode and the external circuit. The anode is an anode of activated carbon particles, the electrode is immersed in running water, and the cathode electrode is a biological cathode, which can generate oxygen and promote the reaction in the cathode chamber to achieve self-sufficiency. The pretreated water flows continuously into the anode chamber through the water inlet, and then flows through all the anode chambers. The organic matter in the water generates electrons and protons under the catalysis of microorganisms. The membrane pours into the cathode chamber, so that the anode chamber group and the cathode chamber group are electrically connected inside the device, and the electrons flow through the external circuit channel at the bottom of the anode chamber through the load to reach the cathode, and make the fuel cell device generate electricity while treating sewage. The invention can form a single battery pack by connecting the external wires of adjacent cathodes and anodes, and can freely connect a plurality of single battery packs in series and parallel to achieve different output effects.
本发明结构简单,可以根据实际需求进行无限扩充,阴极和阳极材料及其安装形式可以根据要求进行变换,各阴阳极室间外电路的任意连通可以利用流道挡板得以实现,使污水得以净化,同时产电。The invention has a simple structure and can be infinitely expanded according to actual needs. The cathode and anode materials and their installation forms can be changed according to requirements. The arbitrary connection of the external circuits between the cathode and anode chambers can be realized by using the flow channel baffle, so that the sewage can be purified. , while generating electricity.
最后应说明的是:虽然以上已经详细说明了本发明及其优点,但是应当理解在不超出由所附的权利要求所限定的本发明的精神和范围的情况下可以进行各种改变、替代和变换。而且,本发明的范围不仅限于说明书所描述的过程、设备、手段、方法和步骤的具体实施例。本领域内的普通技术人员从本发明的公开内容将容易理解,根据本发明可以使用执行与在此所述的相应实施例基本相同的功能或者获得与其基本相同的结果的、现有和将来要被开发的过程、设备、手段、方法或者步骤。因此,所附的权利要求旨在在它们的范围内包括这样的过程、设备、手段、方法或者步骤。Finally, it should be noted that although the present invention and its advantages have been described in detail above, it should be understood that various changes, substitutions and modifications can be made without departing from the spirit and scope of the present invention defined by the appended claims. transform. Moreover, the scope of the present invention is not limited to the specific embodiments of the procedures, devices, means, methods and steps described in the specification. Those of ordinary skill in the art will readily appreciate from the disclosure of the present invention that existing and future devices that perform substantially the same function or obtain substantially the same results as the corresponding embodiments described herein can be used in accordance with the present invention. The developed process, device, means, method or steps. Accordingly, the appended claims are intended to include within their scope such processes, means, means, methods or steps.
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CN110323478A (en) * | 2019-08-06 | 2019-10-11 | 烟台大学 | A kind of integral type multistage microbiological fuel cell group |
CN113471501A (en) * | 2021-06-28 | 2021-10-01 | 太原理工大学 | Series continuous flow microbial fuel cell system, preparation method thereof and application thereof in degrading nitrobenzene wastewater |
CN113471501B (en) * | 2021-06-28 | 2022-07-08 | 太原理工大学 | Series continuous flow microbial fuel cell system, preparation method thereof and application thereof in degrading nitrobenzene wastewater |
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