CN108588747A - A kind of constant gradient spaced electrodes electrolysis unit - Google Patents

A kind of constant gradient spaced electrodes electrolysis unit Download PDF

Info

Publication number
CN108588747A
CN108588747A CN201810712988.2A CN201810712988A CN108588747A CN 108588747 A CN108588747 A CN 108588747A CN 201810712988 A CN201810712988 A CN 201810712988A CN 108588747 A CN108588747 A CN 108588747A
Authority
CN
China
Prior art keywords
electrode
electrolytic cell
baffle
electrolysis device
electrode plate
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
Application number
CN201810712988.2A
Other languages
Chinese (zh)
Inventor
傅士盛
尉婕
王常海
王涛
王安睿
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG RIXIN ELECTRICAL EQUIPMENT Co Ltd
Original Assignee
SHANDONG RIXIN ELECTRICAL EQUIPMENT Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHANDONG RIXIN ELECTRICAL EQUIPMENT Co Ltd filed Critical SHANDONG RIXIN ELECTRICAL EQUIPMENT Co Ltd
Priority to CN201810712988.2A priority Critical patent/CN108588747A/en
Publication of CN108588747A publication Critical patent/CN108588747A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/24Halogens or compounds thereof
    • C25B1/26Chlorine; Compounds thereof
    • C25B1/265Chlorates
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The invention discloses a kind of constant gradient spaced electrodes electrolysis units, relate generally to tap water, sewage sterilizer technical field, including electrolytic cell, it is equipped with baffle in the electrolytic cell, electrode plate is equipped on the baffle, the electrode plate spacing is arranged using form wide at the top and narrow at the bottom, in inverted trapezoidal, lower end spacing 1mm, upper end spacing 2mm, connecting rod is equipped on the baffle, to fixed plate electrode.It has transparent organic glass electrolytic cell, and internal structure can be high-visible, is more advantageous to the maintaining of electrode, increases service life.Electrode plate spacing gradually increases from bottom to top, and current density continuously decreases from bottom to top.It is arranged by this technique, more meets electrolysis rule, to reach raising electrolytic efficiency, energy-saving purpose.

Description

一种等梯度间距电极电解装置An Equal Gradient Spacing Electrode Electrolysis Device

技术领域technical field

本发明主要涉及自来水、污水杀菌消毒设备技术领域,具体是一种等梯度间距电极电解装置。The invention mainly relates to the technical field of tap water and sewage sterilization and disinfection equipment, in particular to an electrode electrolysis device with equal gradient spacing.

背景技术Background technique

电解次氯酸钠设备在生产过程中,需要一定浓度和流量的食盐水作为原料,经电极电解后生成一定浓度的次氯酸钠溶液。电极电解装置的性能决定了电解效率的高低。目前现有技术中,均采用电极板等间距的方式组成电解装置,电流在极板上均匀分布。原料在压力的作用下从电解装置下部向上流动,随着电解的进行,单位密度的电流产生的次氯酸钠产量减少,因此在电解装置上部造成了部分电能的浪费,电解效率较低。In the production process of electrolytic sodium hypochlorite equipment, salt water with a certain concentration and flow rate is required as a raw material, and a certain concentration of sodium hypochlorite solution is generated after electrolysis by electrodes. The performance of the electrode electrolysis device determines the level of electrolysis efficiency. In the current prior art, the electrolysis device is composed of electrode plates at equal intervals, and the current is evenly distributed on the electrode plates. Under the action of pressure, the raw material flows upward from the lower part of the electrolysis device. As the electrolysis proceeds, the output of sodium hypochlorite produced by the current per unit density decreases, so part of the electric energy is wasted in the upper part of the electrolysis device, and the electrolysis efficiency is low.

发明内容Contents of the invention

鉴于现有技术中存在的不足和缺陷,本发明的目的在于提供能够提电解效率,节约能源,提高利用率的一种等梯度间距电极电解装置。In view of the deficiencies and defects in the prior art, the purpose of the present invention is to provide an electrolysis device with equal gradient spacing electrodes that can improve electrolysis efficiency, save energy, and improve utilization.

为了解决上述技术问题,本发明采用如下技术方案:一种等梯度间距电极电解装置,包括电解槽,在所述电解槽内设有挡板,在所述挡板上设有电极板,所述电极板间距采用上宽下窄的形式设置,呈倒梯形,下端间距1mm,上端间距2mm,在所述挡板上设有连接杆,用以固定电极板。In order to solve the above-mentioned technical problems, the present invention adopts the following technical scheme: an electrode electrolysis device with equal gradient intervals, comprising an electrolytic cell, a baffle plate is arranged in the electrolytic cell, an electrode plate is arranged on the baffle plate, the The distance between the electrode plates is set in the form of a wide top and a narrow bottom, which is an inverted trapezoid, with a distance of 1 mm between the lower ends and 2 mm between the upper ends. A connecting rod is provided on the baffle to fix the electrode plates.

作为本发明的进一步改进,所述电解槽为具有透明的有机玻璃电解槽,内部结构能够清晰可见,更有利于电极的维护保养,增加使用寿命。As a further improvement of the present invention, the electrolytic cell is a transparent plexiglass electrolytic cell, and the internal structure can be clearly seen, which is more conducive to the maintenance of the electrodes and increases the service life.

作为本发明的进一步改进,所述挡板采用氟橡胶材质。As a further improvement of the present invention, the baffle is made of fluorine rubber.

作为本发明的进一步改进,连接杆采用PVDF材质As a further improvement of the present invention, the connecting rod is made of PVDF material

作为本发明的进一步改进,电极板采用钛材质,横向排列布置。As a further improvement of the present invention, the electrode plates are made of titanium and arranged in a horizontal arrangement.

作为本发明的进一步改进,每片电极板厚度1mm,面积3dm2,每个电解槽可安装50-500 片。As a further improvement of the present invention, each electrode plate has a thickness of 1 mm and an area of 3 dm2, and 50-500 plates can be installed in each electrolyzer.

与现有技术相比,本发明具有的有益效果为:它具有透明的有机玻璃电解槽,内部结构能够清晰可见,更有利于电极的维护保养,增加使用寿命。电极板间距自下而上逐渐增大,电流密度自下而上逐渐降低。按此工艺进行布置,更符合电解规律,从而达到提高电解效率,节能降耗的目的。Compared with the prior art, the invention has the beneficial effects that it has a transparent plexiglass electrolytic cell, and the internal structure can be clearly seen, which is more conducive to the maintenance of the electrodes and increases the service life. The distance between the electrode plates increases gradually from bottom to top, and the current density gradually decreases from bottom to top. Arranging according to this process is more in line with the law of electrolysis, so as to achieve the purpose of improving electrolysis efficiency, saving energy and reducing consumption.

附图说明Description of drawings

下面结合附图和具体实施方式对本发明作进一步的说明:Below in conjunction with accompanying drawing and specific embodiment the present invention will be further described:

图1为本发明一种等梯度间距电极电解装置的结构示意图;Fig. 1 is the structural representation of a kind of equal gradient spacing electrode electrolysis device of the present invention;

图2为本发明一种等梯度间距电极电解装置电极板的结构示意图。Fig. 2 is a structural schematic diagram of an electrode plate of an electrode electrolysis device with equal gradient spacing according to the present invention.

图中:1、电解槽;2、挡板;3、电极板;4、连接杆。In the figure: 1. Electrolyzer; 2. Baffle plate; 3. Electrode plate; 4. Connecting rod.

值得注意的是,在本发明的描述中,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。此外,术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。It is worth noting that in the description of the present invention, the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. The indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, or in a specific orientation. construction and operation, therefore, should not be construed as limiting the invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.

在本发明的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that unless otherwise specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection. Connected, or integrally connected; it can be mechanically connected or electrically connected; it can be directly connected or indirectly connected through an intermediary, and it can be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention in specific situations.

具体实施方式Detailed ways

为了本发明的技术方案和有益效果更加清楚明白,下面结合附图和具体实施例对本发明进行进一步的详细说明,应当理解,此处所描述的具体实施方式仅用于理解本发明,并不用于限定本发明,本领域普通技术人员在没有做出创造性劳动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 technical solutions and beneficial effects of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments. It should be understood that the specific embodiments described here are only for understanding the present invention and are not intended to limit In 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.

图1为本发明一种等梯度间距电极电解装置的结构示意图,包括电解槽1,在所述电解槽1内设有挡板2,在所述挡板2上设有电极板3,所述电极板3间距采用上宽下窄的形式设置,呈倒梯形,下端间距1mm,上端间距2mm,在所述挡板2上设有连接杆4,用以固定电极板。Fig. 1 is the structural representation of a kind of equal gradient pitch electrode electrolysis device of the present invention, comprises electrolytic cell 1, is provided with baffle plate 2 in described electrolytic cell 1, is provided with electrode plate 3 on described baffle plate 2, described The distance between the electrode plates 3 is set in the form of a wide top and a narrow bottom, which is an inverted trapezoid, with a distance between the lower ends of 1mm and the distance between the upper ends of 2mm. A connecting rod 4 is provided on the baffle plate 2 to fix the electrode plates.

优选的,所述电解槽1为具有透明的有机玻璃电解槽,内部结构能够清晰可见,更有利于电极的维护保养,增加使用寿命。Preferably, the electrolytic cell 1 is a transparent plexiglass electrolytic cell, and the internal structure can be clearly seen, which is more conducive to the maintenance of the electrodes and increases the service life.

优选的,所述挡板2采用氟橡胶材质。Preferably, the baffle plate 2 is made of fluorine rubber.

优选的,连接杆4采用PVDF材质Preferably, the connecting rod 4 is made of PVDF

优选的,电极板3采用钛材质,横向排列布置。Preferably, the electrode plates 3 are made of titanium and arranged in a horizontal arrangement.

优选的,每片电极板3厚度1mm,面积1.5dm2,每个电解槽可安装50-500片。Preferably, each electrode plate 3 has a thickness of 1 mm and an area of 1.5 dm 2 , and each electrolytic cell can contain 50-500 plates.

它具有透明的有机玻璃电解槽1,内部结构能够清晰可见,更有利于电极的维护保养,增加使用寿命。电极板3间距自下而上逐渐增大,电流密度自下而上逐渐降低。按此工艺进行布置,更符合电解规律,从而达到提高电解效率,节能降耗的目的。It has a transparent plexiglass electrolytic cell 1, and the internal structure can be clearly seen, which is more conducive to the maintenance of the electrode and increases the service life. The distance between the electrode plates 3 gradually increases from bottom to top, and the current density gradually decreases from bottom to top. Arranging according to this process is more in line with the law of electrolysis, so as to achieve the purpose of improving electrolysis efficiency, saving energy and reducing consumption.

通过对电极板3间距的布置,电极板3间距采用上部2.0mm,下部1mm的间距进行均匀分布,采用上宽下窄的极板布置方式,有利于电解过程中氢气的排出,电解过程更加安全。电极板3采用1mm厚钛板,每片电极板3面积1.5dm2,电解槽1安装109片电极板3。电流密度自下而上逐渐降低,更加符合电解规律。极大的提高了电解效率,用来电解食盐生产次氯酸钠溶液,每公斤有效氯耗电约4Kw.h,比传统电解方法降低电能消耗约10%。By arranging the spacing of the electrode plates 3, the spacing of the electrode plates 3 is evenly distributed with a spacing of 2.0mm at the upper part and 1mm at the lower part. The arrangement of the electrode plates with a wide top and a narrow bottom is conducive to the discharge of hydrogen during the electrolysis process, and the electrolysis process is safer. . The electrode plate 3 is made of 1 mm thick titanium plate, and the area of each electrode plate 3 is 1.5 dm 2 , and 109 electrode plates 3 are installed in the electrolytic cell 1 . The current density gradually decreases from bottom to top, which is more in line with the law of electrolysis. The efficiency of electrolysis is greatly improved, and it is used to electrolyze table salt to produce sodium hypochlorite solution. The power consumption per kilogram of available chlorine is about 4Kw.h, which is about 10% lower than the traditional electrolysis method.

Claims (6)

1.一种等梯度间距电极电解装置,其特征在于:包括电解槽,在所述电解槽内设有挡板,在所述挡板上设有电极板,所述电极板间距采用上宽下窄的形式设置,呈倒梯形,下端间距1mm,上端间距2mm,在所述挡板上设有连接杆,用以固定电极板。1. An electrode electrolysis device with equal gradient spacing, characterized in that: it comprises an electrolytic cell, a baffle plate is provided in the electrolytic cell, and an electrode plate is arranged on the baffle plate, and the distance between the electrode plates adopts an upper width and a lower width. The narrow form is arranged in an inverted trapezoidal shape, with a distance between the lower ends of 1mm and the distance between the upper ends of 2mm. A connecting rod is arranged on the baffle to fix the electrode plate. 2.根据权利要求1所述的一种等梯度间距电极电解装置,其特征在于,所述电解槽为具有透明的有机玻璃电解槽,内部结构能够清晰可见,更有利于电极的维护保养,增加使用寿命。2. A kind of equal-gradient electrode electrolysis device according to claim 1, characterized in that, the electrolytic cell is a transparent plexiglass electrolytic cell, and the internal structure can be clearly seen, which is more conducive to the maintenance of the electrodes, increasing service life. 3.根据权利要求1所述的一种等梯度间距电极电解装置,其特征在于,所述挡板采用氟橡胶材质。3 . The electrode electrolysis device with equal gradient spacing according to claim 1 , wherein the baffle plate is made of fluorine rubber. 4 . 4.根据权利要求1所述的一种等梯度间距电极电解装置,其特征在于,连接杆采用PVDF材质。4 . The electrode electrolysis device with equal gradient spacing according to claim 1 , wherein the connecting rod is made of PVDF material. 5.根据权利要求1所述的一种等梯度间距电极电解装置,其特征在于,电极板采用钛材质,横向排列布置。5 . The electrode electrolysis device with equal gradient spacing according to claim 1 , wherein the electrode plates are made of titanium and arranged in a horizontal arrangement. 6 . 6.根据权利要求1所述的一种等梯度间距电极电解装置,其特征在于,每片电极板厚度1mm,面积1.5dm2,每个电解槽可安装50-500片。6 . The electrode electrolysis device with equal gradient spacing according to claim 1 , wherein each electrode plate has a thickness of 1 mm and an area of 1.5 dm 2 , and 50-500 plates can be installed in each electrolytic cell.
CN201810712988.2A 2018-06-29 2018-06-29 A kind of constant gradient spaced electrodes electrolysis unit Pending CN108588747A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810712988.2A CN108588747A (en) 2018-06-29 2018-06-29 A kind of constant gradient spaced electrodes electrolysis unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810712988.2A CN108588747A (en) 2018-06-29 2018-06-29 A kind of constant gradient spaced electrodes electrolysis unit

Publications (1)

Publication Number Publication Date
CN108588747A true CN108588747A (en) 2018-09-28

Family

ID=63634896

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810712988.2A Pending CN108588747A (en) 2018-06-29 2018-06-29 A kind of constant gradient spaced electrodes electrolysis unit

Country Status (1)

Country Link
CN (1) CN108588747A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113044936A (en) * 2021-05-17 2021-06-29 北京华舜伟业环保科技有限公司 Electric flocculation electrode plate group
CN115074769A (en) * 2022-05-06 2022-09-20 同济大学 Large-area electrode support body structure of alkaline water electrolytic cell

Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52144377A (en) * 1976-05-27 1977-12-01 Mitsui Eng & Shipbuild Co Ltd Electrolytic cell
IT7922318A0 (en) * 1979-05-03 1979-05-03 Oronzio De Nora Impianti PROCEDURE FOR IMPROVING THE TRANSPORT OF MATTER TO AN ELECTRODE AND RELATED HYDRODYNAMIC MEANS
US4714534A (en) * 1986-06-20 1987-12-22 Olin Corporation Electrolytic halogenator device
JPH08290168A (en) * 1995-04-21 1996-11-05 Toto Ltd Device for electrolyzing running water containing chloride ion and electrolytic method
US5605611A (en) * 1994-10-14 1997-02-25 Oriental Sangyo Co., Ltd. Carbon dioxide-generating electrode apparatus
CN2322979Y (en) * 1997-12-12 1999-06-09 张敬录 Oxygen producer for electrolysis of water
CN203947165U (en) * 2014-04-14 2014-11-19 蓝星(北京)化工机械有限公司 A kind ofly be applicable to the novel electrolytic bath that acrylonitrile electrolysis is prepared adiponitrile
JP2015172251A (en) * 2015-05-20 2015-10-01 三菱重工環境・化学エンジニアリング株式会社 Seawater electrolysis system and seawater electrolysis method
WO2015200147A1 (en) * 2014-06-24 2015-12-30 Chemetics Inc. Narrow gap, undivided electrolysis cell
KR20160038370A (en) * 2014-09-30 2016-04-07 주식회사 케이피에너지 Water electrolysis device
US20160186337A1 (en) * 2014-09-19 2016-06-30 Kabushiki Kaisha Toshiba Electrolytic device and electrode
CN106148993A (en) * 2015-04-24 2016-11-23 王树岩 A kind of multipole saline electrolyzer
CN106986482A (en) * 2017-05-05 2017-07-28 孝感双华应用科技开发有限公司 A kind of photoelectrochemical degradation waste plant
WO2018041059A1 (en) * 2016-08-30 2018-03-08 江苏永冠给排水设备有限公司 Improved full-automatic sodium hypochlorite generator system and implementation method
CN208501116U (en) * 2018-06-29 2019-02-15 山东新日电气设备有限公司 A kind of constant gradient spaced electrodes electrolysis unit

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52144377A (en) * 1976-05-27 1977-12-01 Mitsui Eng & Shipbuild Co Ltd Electrolytic cell
IT7922318A0 (en) * 1979-05-03 1979-05-03 Oronzio De Nora Impianti PROCEDURE FOR IMPROVING THE TRANSPORT OF MATTER TO AN ELECTRODE AND RELATED HYDRODYNAMIC MEANS
US4714534A (en) * 1986-06-20 1987-12-22 Olin Corporation Electrolytic halogenator device
US5605611A (en) * 1994-10-14 1997-02-25 Oriental Sangyo Co., Ltd. Carbon dioxide-generating electrode apparatus
JPH08290168A (en) * 1995-04-21 1996-11-05 Toto Ltd Device for electrolyzing running water containing chloride ion and electrolytic method
CN2322979Y (en) * 1997-12-12 1999-06-09 张敬录 Oxygen producer for electrolysis of water
CN203947165U (en) * 2014-04-14 2014-11-19 蓝星(北京)化工机械有限公司 A kind ofly be applicable to the novel electrolytic bath that acrylonitrile electrolysis is prepared adiponitrile
WO2015200147A1 (en) * 2014-06-24 2015-12-30 Chemetics Inc. Narrow gap, undivided electrolysis cell
US20160186337A1 (en) * 2014-09-19 2016-06-30 Kabushiki Kaisha Toshiba Electrolytic device and electrode
KR20160038370A (en) * 2014-09-30 2016-04-07 주식회사 케이피에너지 Water electrolysis device
CN106148993A (en) * 2015-04-24 2016-11-23 王树岩 A kind of multipole saline electrolyzer
JP2015172251A (en) * 2015-05-20 2015-10-01 三菱重工環境・化学エンジニアリング株式会社 Seawater electrolysis system and seawater electrolysis method
WO2018041059A1 (en) * 2016-08-30 2018-03-08 江苏永冠给排水设备有限公司 Improved full-automatic sodium hypochlorite generator system and implementation method
CN106986482A (en) * 2017-05-05 2017-07-28 孝感双华应用科技开发有限公司 A kind of photoelectrochemical degradation waste plant
CN208501116U (en) * 2018-06-29 2019-02-15 山东新日电气设备有限公司 A kind of constant gradient spaced electrodes electrolysis unit

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
中国科学院金属研究所 等: "钢中非金属夹杂物的鉴定及图谱", 31 July 1981, 黑龙江科学技术出版社, pages: 200 - 196 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113044936A (en) * 2021-05-17 2021-06-29 北京华舜伟业环保科技有限公司 Electric flocculation electrode plate group
CN115074769A (en) * 2022-05-06 2022-09-20 同济大学 Large-area electrode support body structure of alkaline water electrolytic cell
WO2023213054A1 (en) * 2022-05-06 2023-11-09 同济大学 Large-area electrode support body structure of alkaline water electrolytic cell

Similar Documents

Publication Publication Date Title
CN203807570U (en) Electrolytic bath
CN102465311A (en) Manufacturing system and method for sodium hypochlorite
CN108588747A (en) A kind of constant gradient spaced electrodes electrolysis unit
CN106757122A (en) For electrolysis water without spacing diaphragm-free electrolysis device
CN211170913U (en) Water tank and electrolytic bath integrated electrolytic device
CN207659531U (en) A kind of javelle water process units
CN208501116U (en) A kind of constant gradient spaced electrodes electrolysis unit
CN211645405U (en) A device for electrolyzing water to produce hydrogen and oxygen
CN105063653A (en) Electrolysis power-saving method in manganese peroxide preparation process
CN205420566U (en) Ionic exchange membrane electrolyser
CN112111753A (en) A series-type SPE pure water electrolyzer and its diversion net and diversion ring
CN201545915U (en) Gas-liquid self-flow circulation hydrogen electrolysis device
CN207998643U (en) A kind of acidic oxidized electric potential water electrolytic cell that can improve electrolysis performance
CN205152349U (en) Energy -conserving water electrolysis hydrogen device
CN206428041U (en) Anode and cathode synergy electrochemical reaction appts in a kind of barrier film system
CN108004567A (en) A kind of metal material is prepared with continuous electric level electrolytic cell
TW201514345A (en) Electrolysis device and method
CN224001140U (en) Electrochemical degradation waste water device
CN201106068Y (en) Chlorate electrolyser
CN202925128U (en) Online impurity removal device for electrolytic-method coarsened nickel foil production system
CN205556792U (en) Zero pole span electrolysis trough
CN201214684Y (en) Water electrolysis separation to produce hydrogen and oxygen device
CN209636327U (en) Cyclic electrolysis device
US20200141012A1 (en) Multi-Tank Hydrogen-Oxygen Separation Reactor
CN207828420U (en) A kind of electrochemistry electrolytic cell

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

Application publication date: 20180928

RJ01 Rejection of invention patent application after publication