CN203728935U - Electrolysis bath - Google Patents

Electrolysis bath Download PDF

Info

Publication number
CN203728935U
CN203728935U CN201420090607.9U CN201420090607U CN203728935U CN 203728935 U CN203728935 U CN 203728935U CN 201420090607 U CN201420090607 U CN 201420090607U CN 203728935 U CN203728935 U CN 203728935U
Authority
CN
China
Prior art keywords
electrolytic
electrolytic pole
barrel
end plate
cylindrical shell
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.)
Expired - Fee Related
Application number
CN201420090607.9U
Other languages
Chinese (zh)
Inventor
董国平
王佳
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.)
SANHE YUBO ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd
Original Assignee
SANHE YUBO ENVIRONMENTAL PROTECTION 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 SANHE YUBO ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd filed Critical SANHE YUBO ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd
Priority to CN201420090607.9U priority Critical patent/CN203728935U/en
Application granted granted Critical
Publication of CN203728935U publication Critical patent/CN203728935U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

An electrolysis bath comprises a barrel, a plurality of electrolytic pole plates located in the barrel, an electrolyte as well as end plates fixedly connected to two sides of the barrel, wherein the plurality of electrolytic pole plates are uniformly and equidistantly stacked and arranged in the barrel along an axis inside the barrel; holes are formed in the same positions of end parts of two edges of each electrolytic pole plate respectively; and the holes in end parts of the plurality of electrolytic pole plates are correspondingly through to form two channels. According to the electrolysis bath, uniform gaps of the pole plates in the barrel is guaranteed, the electrolyte can uniformly flow into each electrolysis chamber, fluctuation of electrical pressure applied to two sides of each end plate can be effectively reduced, and the gas yield is stable, so that the electric energy is saved, and the loss is reduced.

Description

Electrolyzer
Technical field
The utility model belongs to water electrolysis technical field, relates in particular to a kind of electrolyzer.
Background technology
At present, the overall structure patterns that adopt the high pressure low current of electrodes series connection or the low-voltage and high-current of electrode parallel connection in the electrolyzer of water electrolysis generation oxyhydrogen more.The high pressure low current structure formation of electrode series connection is to be connected by multiple tank rooms, and whole electrolytic solution runs through all tank rooms, but the capacity of the electrolytic solution of each tank room distributes and be inhomogeneous.The arrangement of electrolytic pole board position in the tank room of existing electrolyzer, and the quantity in hole and the layout of position on electrolytic pole board is unreasonable, thereby, can cause electrolyzer both sides institute making alive to produce fluctuation, cause aerogenesis not steady, thereby make identical gas production rate can consume more electric energy.
Summary of the invention
In view of this, the purpose of this utility model is to propose a kind of electrolyzer, to solve the irrational problem of topology layout in above-mentioned electrolyzer.
For there is to a basic understanding some aspects of the embodiment disclosing, provide simple summary below.This summary part is not to comment general, neither determine key/critical component or describe the protection domain of these embodiment.Its sole purpose is to present some concepts by simple form, the preamble using this as following detailed description.
The utility model provides a kind of electrolyzer, comprise cylindrical shell, be positioned at multiple electrolytic pole boards, the ionogen of cylindrical shell and be fixedly connected on the end plate of cylindrical shell both sides, multiple described electrolytic pole boards along the uniform equally spaced stacked arrangement of the axis in cylinder in described inner barrel, the same position of the end at two edges of each described electrolytic pole board offers respectively a hole, and the described hole correspondence of two ends of multiple described electrolytic pole boards runs through formation two passes.
In some optional embodiments, between described adjacent two electrolytic pole boards, form a tank room, described multiple electrolytic pole boards form multiple described tank rooms.
In some optional embodiments, electrolytic solution import is set on the end plate of a described side, on the end plate of opposite side, electrolyte outlet is set; A passage in described two passes is just to electrolytic solution import, and another passage is just to electrolyte outlet.
In some optional embodiments, between described adjacent electrolytic pole board, adopt packing ring fixedly to separate.
In some optional embodiments, being shaped as of described packing ring is square circular or oval.
The beneficial effect of above embodiment: this design can make electrolytic solution flow into uniformly each tank room, can effectively reduce the fluctuation of end plate pressure that both sides power up, and makes aerogenesis steady, can not produce and spring up phenomenon, thereby realize saves energy, reduce the wastage, and then reduce costs.
For above-mentioned and relevant object, one or more embodiment comprise below by the feature that describes in detail and particularly point out in the claims.Explanation below and accompanying drawing describe some illustrative aspects in detail, and its instruction is only some modes in the utilizable variety of way of principle of each embodiment.Other benefit and novel features consider the detailed description along with below by reference to the accompanying drawings and become obviously, and the disclosed embodiments are to comprise being equal to of all these aspects and they.
figure of description
Fig. 1 is the schematic diagram of the integrally-built sectional view of electrolyzer of the present utility model;
Fig. 2 is the schematic diagram of electrolyzer explosive view of the present utility model.
Embodiment
For above-mentioned purpose of the present utility model, feature and advantage can be become apparent more, below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
As shown in Figure 1, show electrolyzer one-piece construction schematic diagram of the present utility model.
The structure of this electrolyzer is as follows:
This electrolyzer comprises cylindrical shell 1, electrolytic pole board 2, ionogen 3, packing ring 4 and end plate 5; End plate 5 is fixedly connected on cylindrical shell 1, and end plate 5 can be to be bolted to connection on cylindrical shell 1, or, can be fixedly connected on cylindrical shell 1 by hinge, or other modes, can be fixedly connected on cylindrical shell 1 as long as can realize end plate 5, detachably again simultaneously.Electrolytic pole board 2 is positioned at the inside of cylindrical shell 1, uniform equally spaced stacked arrangement is in cylindrical shell 1, electrolytic pole board 2 relies on end plate 5 extruding at cylindrical shell 1 two ends firm, the same position of the end at two edges of each electrolytic pole board 2 offers respectively a hole, the hole correspondence of two ends of multiple electrolytic pole boards 2 run through form along drum shaft to for electrolytic solution flow into passage 8 and for gas flow out passage 9.Ionogen 3 is flooded with whole electrolyzer, is evenly distributed in around each electrolytic pole board.Between electrolytic pole board 2, adopt packing ring 4 fixedly to separate, packing ring 4 is nylon material, its cross-sectional shape can be square or circular or oval, or the shape that other are feasible, gap between nylon washer 4 is consistent, like this, make to remain certain distance between adjacent electrolytic pole board 2, and can not contact with each other together.
The gap of cylindrical shell internal polar plate is even, can make electrolytic solution flow into uniformly each tank room, can effectively reduce the fluctuation of end plate pressure that both sides power up, make aerogenesis steady, can not produce and spring up phenomenon, thereby realize saves energy, reduce the wastage, and then reduce costs.
As described in Figure 2, show the schematic diagram of explosive view of the present utility model.
Cylindrical shell 1 is to be processed by high-temperature insulation nylon material entirety; The end plate 5 of cylindrical shell 1 both sides adopts 304 stainless steels to make, and it can unload by loosering a bolt, and on the end plate 5 of a side, is provided with electrolytic solution import 6, on the end plate 5 of opposite side, is provided with electrolyte outlet 7; The position in the hole on each electrolytic pole board 2 is the position of corresponding end plate 5 By Electrolysis liquid imports 6 and electrolyte outlet 7 respectively, like this, makes passage 8 in two passes just to electrolytic solution import 6, and another passage 9 is just to electrolyte outlet 7; Electrolytic pole board 2 adopts 304 stainless steels to make, and between adjacent two electrolytic pole boards 2, forms a tank room, and multiple electrolytic pole boards form multiple described tank rooms; The passage 8 that the electrolytic solution that enters cylindrical shell 1 inside in electrolytic solution import 6 forms by the hole under pole plate can flow through each tank room uniformly, and the hydrogen producing in electrolytic process and oxygen are derived electrolyzer by electrolyte outlet to the passage 9 that the hole directly over pole plate forms from bottom to top at tank room.
With reference to the accompanying drawings of preferred embodiment of the present utility model, not thereby limit to interest field of the present utility model above.Allly using any amendment of doing within technical conceive of the present utility model, be equal to and replace and improve, all should be within interest field of the present utility model.

Claims (5)

1. an electrolyzer, comprise cylindrical shell, be positioned at multiple electrolytic pole boards, the ionogen of cylindrical shell and be fixedly connected on the end plate of cylindrical shell both sides, it is characterized in that, multiple described electrolytic pole boards along the uniform equally spaced stacked arrangement of the axis in cylinder in described inner barrel, the same position of the end at two edges of each described electrolytic pole board offers respectively a hole, and the described hole correspondence of two ends of multiple described electrolytic pole boards runs through formation two passes.
2. electrolyzer according to claim 1, is characterized in that, between described adjacent two electrolytic pole boards, forms a tank room, and described multiple electrolytic pole boards form multiple described tank rooms.
3. electrolyzer according to claim 1, is characterized in that, electrolytic solution import is set on the end plate of a described side, on the end plate of opposite side, electrolyte outlet is set; A passage in described two passes is just to electrolytic solution import, and another passage is just to electrolyte outlet.
4. electrolyzer according to claim 1, is characterized in that, between adjacent electrolytic pole board, adopts packing ring fixedly to separate.
5. electrolyzer according to claim 4, is characterized in that, being shaped as of described packing ring cross section is square circular or oval.
CN201420090607.9U 2014-02-28 2014-02-28 Electrolysis bath Expired - Fee Related CN203728935U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420090607.9U CN203728935U (en) 2014-02-28 2014-02-28 Electrolysis bath

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420090607.9U CN203728935U (en) 2014-02-28 2014-02-28 Electrolysis bath

Publications (1)

Publication Number Publication Date
CN203728935U true CN203728935U (en) 2014-07-23

Family

ID=51199021

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420090607.9U Expired - Fee Related CN203728935U (en) 2014-02-28 2014-02-28 Electrolysis bath

Country Status (1)

Country Link
CN (1) CN203728935U (en)

Similar Documents

Publication Publication Date Title
RU2013105469A (en) METHOD OF GAS PRODUCTION AND DEVICE FOR ITS IMPLEMENTATION
CN211972465U (en) Water electrolysis bath polar plate
WO2016169330A1 (en) Multipole saline electrolysis device
CN202107777U (en) Electrolytic bath
CN204434733U (en) Electrolyzer
CN203728935U (en) Electrolysis bath
CN203613299U (en) Electrochemical corrosion device of aluminum foils for capacitor
CN204067077U (en) Aluminium electroloysis Waste Acid From Hua Cheng Foil conductive plate structure
CN201525894U (en) Combined type multi-cathode and multi-anode graphite electrolytic tank
CN204039528U (en) Electrolytic copper foil generator electrolyzer feed liquor distribution pattern
CN202246889U (en) Novel perchlorate electrolytic bath
CN202543338U (en) Improved structure of hydrogen-oxygen generator electrode assembly
CN204898099U (en) Wrap -around compartment aluminium cell of positive pole
MY175986A (en) A water electrolyzer
CN204342891U (en) Low consumption prebaked anode used for aluminium electrolysis
CN103255432A (en) Water electrolysis device
CN205474015U (en) Dull and stereotyped split type high -efficient water electrolysis groove
CN203295616U (en) Water-splitting box
CN202808958U (en) Energy-saving electrolytic cell
CN205474033U (en) Ionic exchange membrane electrolyser
CN105780044A (en) Hydrogen-oxygen generator resisting high pressure and preventing corrosion
CN201530868U (en) Electrolysis bath graphite cathode for producing ammonium peroxodisulfate
CN205474020U (en) Novel ion membrane electrolytic cell
CN201990737U (en) Electrode plate for electrolytic bath
CN102943282A (en) Electrolyte self-circulation medium-pressure water electrolysis hydrogen production system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140723

Termination date: 20200228