CN103882470A - Transparent-tube type brine electrolyzer - Google Patents

Transparent-tube type brine electrolyzer Download PDF

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Publication number
CN103882470A
CN103882470A CN201410152179.2A CN201410152179A CN103882470A CN 103882470 A CN103882470 A CN 103882470A CN 201410152179 A CN201410152179 A CN 201410152179A CN 103882470 A CN103882470 A CN 103882470A
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CN
China
Prior art keywords
outer tube
electrolyzer
transparent
plate
transparent tubular
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Pending
Application number
CN201410152179.2A
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Chinese (zh)
Inventor
逯艳英
刘波
韩严
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.)
Qingdao Sunrui Marine Environment Engineering Co Ltd
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Qingdao Sunrui Marine Environment Engineering 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.)
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Application filed by Qingdao Sunrui Marine Environment Engineering Co Ltd filed Critical Qingdao Sunrui Marine Environment Engineering Co Ltd
Priority to CN201410152179.2A priority Critical patent/CN103882470A/en
Publication of CN103882470A publication Critical patent/CN103882470A/en
Pending legal-status Critical Current

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Abstract

The invention relates to a transparent-tube type brine electrolyzer. The shape of the electrolyzer is of a transparent-tube type structure, and the electrolyzer comprises an outer tube and flange covers installed at the both ends of the outer tube respectively, wherein an electrolyzer cavity is formed in the outer tube, a plurality of partition plates are uniformly installed in the electrolyzer cavity, a unit electrolysis chamber is formed between two adjacent partition plates, an anode plate and a cathode plate are installed in each of the unit electrolysis chambers, the anode plate and the cathode plate are spaced and oppositely arranged, and a gap, through which an electrolyte passes, is formed between the partition plates and the outer tube; a water inlet and a water outlet are formed in the upper side and lower side of the both ends of the outer tube respectively. The transparent-tube type brine electrolyzer disclosed by the invention has the following advantages: instantaneous separation between hydrogen and the electrolyte is ensured during an electrolysis process, the electrolytic current efficiency is increased, and the energy consumption is greatly reduced; a fully-transparent housing design is used, so that the reaction condition in the electrolyzer and the scaling degree of the pole plates can be conveniently observed, acid pickling can be carried out in time, and the heating of the electrolyzer and the burn-out faults of the pole plates due to precipitate blockages between the anode plate and the cathode plate are avoided.

Description

Transparent tubular type saline electrolysis groove
Technical field
The invention belongs to water-treatment technology field, in fuel-burning power plant and petroleum chemical plant water coolant, naval vessel, swimming pool sterilization, drinking water disinfection, oil field reinjection water processing, Hospital Sewage Treatment, foodstuffs industry disinfection, wastewater treatment, bleaching and dyeing aspect the water treatments such as color treatments and have a wide range of applications.
 
Background technology
Current electrolysis produces clorox and prevents that for water treatment system biological growth from breeding by the mode of generally approving and applying, the domestic Type B saline electrolysis groove that has at present the two auspicious developments in Qingdao, for vertical structure, maximum production is 2,5Kg/h, is shown in patent " net-type transparent electrolytic bath ", the patent No.: ZL99201387.9, the saline electrolysis groove that other producers provide is on the market also vertical structure, and the drawback of existence is:
A, existing product list groove output are lower, can not meet the demand of the engineering project of the large-scale processing water yield, and output of the present invention can be from little adjustable to 40Kg/h greatly to 1Kg/h.
B, existing apparatus structure By Electrolysis product hydrogen can not separate with pole plate immediately, and current efficiency is low, and the present invention just separates hydrogen in electrolyzer from electrolytic solution, has greatly improved the electrolytic efficiency of electrode, energy efficient.
C, currently available products can not be observed inner reaction condition, often there is the fault of quick-fried groove, pole plate scaling loss to occur, the present invention selects transparent organic glass pipe as shell, end flange is also transparent acrylic, response situation and pole plate scaling degree in energy clear view groove, in time pickling, has avoided between anode and cathode precipitation to stop up and the electrolyzer heating causing, the occurrence probability of pole plate over-heated fault.
 
Summary of the invention
For overcoming the defect of prior art, the invention provides a kind of transparent tubular type saline electrolysis groove.Technical scheme of the present invention is: a kind of transparent tubular type saline electrolysis groove, this electrolyzer profile is transparent tubular structure, comprise outer tube and be arranged on respectively the blind flange at outer tube two ends, in described outer tube, form electrolyzer cavity, in this electrolyzer cavity, several dividing plates are installed uniformly, forming unit tank room between adjacent two dividing plates, in each unit tank room, positive plate and negative plate are all installed, described positive plate and negative plate spacing distance are also oppositely arranged, and form the gap that electrolysis liquid passes through between dividing plate and outer tube; Conductive anode rod penetrates to outer tube inside from a blind flange wherein, and this conductive anode rod is connected with the positive plate in outer tube; Negative electrode conducting rod penetrates to outer tube inside from another blind flange, and this negative electrode conducting rod is connected with the negative plate in outer tube; Be respectively arranged with water-in and water outlet at the upper and lower sides at outer tube two ends.
The end of described outer tube is provided with end flanges, together with this end flanges is bolted with blind flange.
On described dividing plate, be provided with ventilating pit.
Described negative plate or positive plate are made by titanium matrix.
Described outer tube is docked and forms successively by several unit pipes.
On the joint of described adjacent two unit pipes, be respectively arranged with end flanges, between two end flanges, gasket be installed, and be bolted together.
 
Advantage of the present invention is: the present invention has guaranteed that in electrolytic process hydrogen moment separates with electrolytic solution, has improved Faradaic current efficiency, greatly reduces energy consumption; Adopt the shell design of all-transparent, be convenient to observe response situation and pole plate scaling degree in groove, pickling in time, has avoided precipitation between anode and cathode to stop up and the electrolyzer heating, the pole plate over-heated fault that cause.
 
Accompanying drawing explanation
Fig. 1 is agent structure schematic diagram of the present invention.
 
Embodiment
Further describe the present invention below in conjunction with specific embodiment, advantage and disadvantage of the present invention will be more clear along with description.But these embodiment are only exemplary, scope of the present invention are not formed to any restriction.It will be understood by those skilled in the art that lower without departing from the spirit and scope of the present invention and can the details of technical solution of the present invention and form be modified or be replaced, but these modifications and replacement all fall within the scope of protection of the present invention.
Referring to Fig. 1, the present invention relates to a kind of transparent tubular type saline electrolysis groove, this electrolyzer profile is transparent tubular structure, comprise outer tube 7 and be arranged on respectively the blind flange 1 at outer tube 7 two ends, the described interior formation electrolyzer of outer tube 7 cavity, several dividing plates 8 are installed in this electrolyzer cavity uniformly, forming unit tank room 3 between adjacent two dividing plates 8, interior positive plate 4 and the negative plate 5 of being all provided with of each unit tank room 3, described positive plate 4 and negative plate 5 spacing distances are also oppositely arranged, and between dividing plate 8 and outer tube 7, form the gap that electrolysis liquid passes through; Conductive anode rod 6 penetrates to outer tube 7 inside from a blind flange 2 wherein, and this conductive anode rod 6 is connected with the positive plate 4 in outer tube 7; Negative electrode conducting rod 9 penetrates to outer tube 7 inside from another blind flange 2, and this negative electrode conducting rod 9 is connected with the negative plate 5 in outer tube 7; Be respectively arranged with water-in 15 and water outlet 16 at the upper and lower sides at outer tube 7 two ends.On described dividing plate 8, be provided with the ventilating pit passing through for hydrogen.Wherein, between negative electrode conducting rod and conductive anode rod and blind flange 1, do insulation processing.
The end of described outer tube 7 is provided with end flanges 2, together with this end flanges 2 is bolted with blind flange 1.
Described negative plate 5 or positive plate 4 are made by titanium matrix.
Described outer tube 7 is docked and forms successively by several unit pipes; On the joint of described adjacent two unit pipes, be respectively arranged with end flanges, between two end flanges, gasket be installed, and be bolted together.

Claims (6)

1. a transparent tubular type saline electrolysis groove, it is characterized in that, this electrolyzer profile is transparent tubular structure, comprise outer tube and be arranged on respectively the blind flange at outer tube two ends, in described outer tube, form electrolyzer cavity, in this electrolyzer cavity, several dividing plates are installed uniformly, forming unit tank room between adjacent two dividing plates, in each unit tank room, positive plate and negative plate are all installed, described positive plate and negative plate spacing distance are also oppositely arranged, and form the gap that electrolysis liquid passes through between dividing plate and outer tube; Conductive anode rod penetrates to outer tube inside from a blind flange wherein, and this conductive anode rod is connected with the positive plate in outer tube; Negative electrode conducting rod penetrates to outer tube inside from another blind flange, and this negative electrode conducting rod is connected with the negative plate in outer tube; Be respectively arranged with water-in and water outlet at the upper and lower sides at outer tube two ends.
2. transparent tubular type saline electrolysis groove according to claim 1, is characterized in that, the end of described outer tube is provided with end flanges, together with this end flanges is bolted with blind flange.
3. transparent tubular type saline electrolysis groove according to claim 1, is characterized in that, on described dividing plate, is provided with ventilating pit.
4. transparent tubular type saline electrolysis groove according to claim 1, is characterized in that, described negative plate or positive plate are made by titanium matrix.
5. according to the transparent tubular type saline electrolysis groove described in claim 2-4 any one claim, it is characterized in that, described outer tube is docked and forms successively by several unit pipes.
6. transparent tubular type saline electrolysis groove according to claim 5, is characterized in that, on the joint of described adjacent two unit pipes, is respectively arranged with end flanges, between two end flanges, gasket is installed, and is bolted together.
CN201410152179.2A 2014-04-16 2014-04-16 Transparent-tube type brine electrolyzer Pending CN103882470A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410152179.2A CN103882470A (en) 2014-04-16 2014-04-16 Transparent-tube type brine electrolyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410152179.2A CN103882470A (en) 2014-04-16 2014-04-16 Transparent-tube type brine electrolyzer

Publications (1)

Publication Number Publication Date
CN103882470A true CN103882470A (en) 2014-06-25

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CN201410152179.2A Pending CN103882470A (en) 2014-04-16 2014-04-16 Transparent-tube type brine electrolyzer

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105112933A (en) * 2015-09-22 2015-12-02 苏州市铂瑞工业材料科技有限公司 High-yielding chlorine electrolysis device
CN108193223A (en) * 2018-02-11 2018-06-22 广东卓信环境科技股份有限公司 A kind of hypochlorite production system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4511440A (en) * 1983-12-22 1985-04-16 Allied Corporation Process for the electrolytic production of fluorine and novel cell therefor
CN87202871U (en) * 1987-03-10 1987-12-31 铁道部专业设计院 Tube type electrolytic tank with sodium hypochlorate generator
CN2260890Y (en) * 1996-06-28 1997-08-27 华北石油技工学校新技术开发研究所 Electric sterilizing device for oil-field back-injected waste water
CN2359298Y (en) * 1999-02-09 2000-01-19 中国船舶工业总公司第七研究院第七二五研究所 Net-type transparent electrolytic bath
CN102583662A (en) * 2012-02-24 2012-07-18 浙江工业大学 Screen plunger piston flow electrolyzing device and method for treating organic wastewater

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4511440A (en) * 1983-12-22 1985-04-16 Allied Corporation Process for the electrolytic production of fluorine and novel cell therefor
CN87202871U (en) * 1987-03-10 1987-12-31 铁道部专业设计院 Tube type electrolytic tank with sodium hypochlorate generator
CN2260890Y (en) * 1996-06-28 1997-08-27 华北石油技工学校新技术开发研究所 Electric sterilizing device for oil-field back-injected waste water
CN2359298Y (en) * 1999-02-09 2000-01-19 中国船舶工业总公司第七研究院第七二五研究所 Net-type transparent electrolytic bath
CN102583662A (en) * 2012-02-24 2012-07-18 浙江工业大学 Screen plunger piston flow electrolyzing device and method for treating organic wastewater

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105112933A (en) * 2015-09-22 2015-12-02 苏州市铂瑞工业材料科技有限公司 High-yielding chlorine electrolysis device
CN105112933B (en) * 2015-09-22 2017-10-10 苏州市铂瑞工业材料科技有限公司 A kind of high yield chlorine electrolysis unit
CN108193223A (en) * 2018-02-11 2018-06-22 广东卓信环境科技股份有限公司 A kind of hypochlorite production system
CN108193223B (en) * 2018-02-11 2023-12-15 广东卓信环境科技股份有限公司 Hypochlorite production system

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Application publication date: 20140625