CN201809207U - Novel electrolysis reactor - Google Patents
Novel electrolysis reactor Download PDFInfo
- Publication number
- CN201809207U CN201809207U CN2010205035822U CN201020503582U CN201809207U CN 201809207 U CN201809207 U CN 201809207U CN 2010205035822 U CN2010205035822 U CN 2010205035822U CN 201020503582 U CN201020503582 U CN 201020503582U CN 201809207 U CN201809207 U CN 201809207U
- Authority
- CN
- China
- Prior art keywords
- electrolysis reactor
- novel electrolysis
- novel
- frame
- plates
- 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
Links
Images
Abstract
The utility model discloses a novel electrolysis reactor, which comprises negative plates, positive plates, insulating rubber, a frame, a connecting bar and an adjusting device. The negative plates and the positive plates are inserted into the middle of the frame in mutually spaced manner, and fixed to a side rail in the middle of the frame, so that an upper water trough is formed at the upper portion of the frame, a lower water trough is formed at the lower portion of the frame, the insulating rubber is clamped between each adjacent two of the negative plate and the positive plate, and the adjusting device is connected to the outer ends of the negative plates and the positive plates. The novel electrolysis reactor has the advantages that the novel electrolysis reactor adopting the technical scheme is quite simple in equipment and operation and low in occupied area, electromechanical processes are available at normal temperature and pressure, the energy efficiency is high, operation cost is lower as sodium chloride is used as electrolyte, the novel electrolysis reactor has high corrosion resistance, the plates are semi-permanent and durable, no chemical sludge is generated in electrolysis process, treatment expense for the technical sludge is avoided, the labor intensity is low, organic pollutant in wastewater is degraded into carbon dioxide, water and simple organic matters, the oxidation efficiency is high, and no or rare secondary pollution is generated.
Description
Technical field
The utility model belongs to a kind of sewage disposal technology, particularly a kind of novel electrolysis reactor that is used to dispose of sewage.
Background technology
The senior bioreactor technology of present several membrane separation technique and composite membrane, handling waste water with the combination between them is current recovering and using technology of water with fastest developing speed.Along with the improvement of membrane module and the decline of mould material cost, also just accelerating this trend.Nanofiltration in the membrane separation technique (NF) and reverse osmosis (OR) technology can be carried out effective desalination to waste water, guarantee that effluent quality is also more stable.Selecting reliable, economic, stable reuse treatment process for use, is that enterprise increases the water cycle amount, improves the key of waste water recycling.
When application of membrane separation technology is in waste water recycling, the ratio of desalinization height, can further reduce COD, the BOD of reuse water and colourity etc., and can remove inorganic salts in the reuse water, overcome the advantages such as accumulation problem of inorganic salts and difficult degradation pollutent in the production system, can reach colourless and low salinity through the reverse osmosis water outlet.But pollutent separated spissated process because the essence of membrane separation technique only is one; say that in essence it does not remove function to pollutent; do not have decomposition and inversion removal effect to pollutent; like this when obtaining a large amount of reuse waters; also produced and comprised a large amount of films and handle the most salinities in the water inlet and the high salt concentrated solution of remaining organic pollution materials; must could discharge after up to standard through handling; now except entering the good method that sewage work handles does not have other; this will certainly increase the burden and the difficulty of sewage work; too high salinity may also can produce detrimentally affect to sewage work's treatment effect; membrane technique is the widespread use in the reuse water again, and the processing of its concentrated solution is that present membrane separation technique realizes industrialization; the biggest obstacle that mass-producing is used.
To the processing of the concentrated liquid of membrane sepn, consider recovery and reuse usually to useful component, reduce their pollutions to the discharging environment; Secondly membrane sepn concentrate liquid processing also must in conjunction with, rely on treatment technologies such as traditional biochemistry, materialization, decompose, remove all contaminations, only in this way just can avoid membrane sepn to concentrate liquid to discharging the pollution that water body causes.But the composition of its high salt utilizes that conventional biochemistry, physical chemistry method are handled technically, all is to be difficult to directly reach discharging standards on the running cost.
Summary of the invention
The purpose of this utility model is in order to address the above problem, to have designed a kind of novel electrolysis reactor.
Realize that the above-mentioned purpose the technical solution of the utility model is, a kind of novel electrolysis reactor, comprise negative plate, positive plate, electro-insulating rubber, framework, union lever and setting device, the middle part of the insertion framework of negative plate and positive plate space, and be fixed on the slide rail of frame mid portion, make the top of framework form upper flume, lower flume is formed at the bottom, accompany electro-insulating rubber between the adjacent cathode-anode plate, the outer end of cathode-anode plate is connected with setting device.
Above-mentioned negative plate and anode plate design reticulate, and improve electrolytic efficiency to increase contact area.
The shaped design of above-mentioned electro-insulating rubber becomes the rectangular box that is complementary with cathode-anode plate, effectively stops the electric current contact between adjacent plate.
Setting device is made up of connective bar and compression set, and compression set is fixedly connected on the splicing ear at cathode-anode plate two ends on the connective bar that has slide rail, convenient distance of regulating between the two-plate.
Upper flume is connected to circulating line and discharge tube, helps improving electrolytic utilization ratio; Lower flume is connected to circulating line and inlet channel, conveniently draws water the cyclic utilization rate height.
Volume pump is housed on inlet channel, rises to waste water in the electrolyzer and control the water yield.
Recycle pump is housed on circulating line, guarantees that the waste water in the tank fully contacts with electrode.
The beneficial effects of the utility model are, adopt the electrolysis reactor equipment of above-mentioned technical scheme and operate fairly simplely, and floor space is little; Electrochemical process generally just can carry out at normal temperatures and pressures, the energy efficiency height; As ionogen, working cost is lower with sodium-chlor; The equipment corrosion resistance nature is strong, and battery lead plate is semipermanent, and is durable in use; No chemical sludge produces in the electrolytic process, and the processing costs of chemical sludge does not take place, and labour intensity is low; Organic pollutant in the waste water will be degraded to carbonic acid gas, water and simple organic, and the oxidation efficiency height does not have or seldom produces secondary pollution.
Description of drawings
Fig. 1 is the structural representation of novel electrolyzer described in the utility model;
Among the figure, 1, upper flume; 2, negative plate; 3, connective bar; 4, positive plate; 5, lower flume; 6, electro-insulating rubber; 7, volume pump; 8, recycle pump; 9, drainage pipeline; 10, inlet channel; 11, compression set; 12, splicing ear; 13, framework; 14, circulating line; 15, slide rail.
Embodiment
Specifically describe of the present utility model below in conjunction with accompanying drawing, as Fig. 1 is the structural representation of novel electrolyzer described in the utility model, as shown in the figure, the middle part of the insertion framework (13) of negative plate (2) and positive plate (4) space, and be fixed on the slide rail (15) of frame mid portion, make the top of framework form upper flume (1), lower flume (5) is formed at the bottom.Cathode-anode plate is designed to netted, accompanies electro-insulating rubber (6) between the adjacent cathode-anode plate, electro-insulating rubber be shaped as rectangular box with cathode-anode plate coupling.The splicing ear at cathode-anode plate two ends (12) is fixedly connected on the connective bar (3) that has slide rail by compression set (11).Upper flume is connected to circulating line (14) and discharge tube (9), and lower flume is connected to circulating line and inlet channel (10).Volume pump (7) is housed on the inlet channel, recycle pump (8) is housed on the circulating line.
During work, by volume pump by inlet channel with in the waste water suction lower flume, start recycle pump then the waste water in the lower flume imported upper flume endlessly by circulating line.Under the effect of gravity, the water in the upper flume flows downward, and fully contacts by electrolyte layers and electrode to reach electrolytic purpose.
Technique scheme has only embodied the optimal technical scheme of technical solutions of the utility model; those skilled in the art to some part wherein some changes that may make all embodied principle of the present utility model, belong within the protection domain of the present utility model.
Claims (8)
1. novel electrolysis reactor, comprise negative plate (2), positive plate (4), electro-insulating rubber (6), framework (13) and setting device, it is characterized in that, the middle part of the insertion framework of negative plate and positive plate space, and be fixed on the slide rail (15) of frame mid portion, make the top of framework form upper flume (1), lower flume (5) is formed at the bottom, accompany electro-insulating rubber between the adjacent cathode-anode plate, the outer end of cathode-anode plate is connected with setting device.
2. novel electrolysis reactor according to claim 1 is characterized in that negative plate and anode plate design reticulate.
3. novel electrolysis reactor according to claim 1 is characterized in that, the shaped design of electro-insulating rubber becomes the rectangular box that is complementary with cathode-anode plate.
4. novel electrolysis reactor according to claim 1 is characterized in that, setting device is made up of connective bar (3) and compression set (11), and compression set is fixedly connected on the splicing ear (12) at cathode-anode plate two ends on the connective bar that has slide rail.
5. novel electrolysis reactor according to claim 1 is characterized in that, upper flume is connected to circulating line (14) and discharge tube (9).
6. novel electrolysis reactor according to claim 1 is characterized in that, lower flume is connected to circulating line and inlet channel (10).
7. novel electrolysis reactor according to claim 6 is characterized in that, volume pump (7) is housed on the water inlet pipe.
8. according to claim 5 or 6 described novel electrolysis reactors, it is characterized in that, recycle pump (8) is housed on the circulating line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205035822U CN201809207U (en) | 2010-08-25 | 2010-08-25 | Novel electrolysis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205035822U CN201809207U (en) | 2010-08-25 | 2010-08-25 | Novel electrolysis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201809207U true CN201809207U (en) | 2011-04-27 |
Family
ID=43892146
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205035822U Expired - Fee Related CN201809207U (en) | 2010-08-25 | 2010-08-25 | Novel electrolysis reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201809207U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288185A (en) * | 2013-05-20 | 2013-09-11 | 江苏通瑞环保科技发展有限公司 | Method for heavy metal ion wastewater treatment based on outer circulation electrocoagulation technology |
| CN103613175A (en) * | 2013-11-22 | 2014-03-05 | 江苏科技大学 | Electric flocculation water treatment technology for retarding pole plate passivation |
-
2010
- 2010-08-25 CN CN2010205035822U patent/CN201809207U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288185A (en) * | 2013-05-20 | 2013-09-11 | 江苏通瑞环保科技发展有限公司 | Method for heavy metal ion wastewater treatment based on outer circulation electrocoagulation technology |
| CN103288185B (en) * | 2013-05-20 | 2015-07-01 | 江苏通瑞环保科技发展有限公司 | Method for heavy metal ion wastewater treatment based on outer circulation electrocoagulation technology |
| CN103613175A (en) * | 2013-11-22 | 2014-03-05 | 江苏科技大学 | Electric flocculation water treatment technology for retarding pole plate passivation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106277591B (en) | Landfill leachate nanofiltration concentrate processing method | |
| CN204727706U (en) | A kind of film electrical coupling system of Sewage advanced treatment | |
| CN202576160U (en) | Municipal sewage treatment and regeneration recycling device | |
| CN104944646B (en) | Wastewater advanced treatment method coupling membrane and electricity | |
| CN207435111U (en) | A kind of electrochemical process-submerged membrane separation integrated water processing device | |
| CN102120678B (en) | Sewage recycling device based on electrolysis and membrane biological reactor technology and method thereof | |
| US10384968B2 (en) | Ternary sewage treatment method integrating microbial fuel cells with anaerobic acidification and forward osmosis membrane | |
| CN101792199A (en) | Sewage treatment technique | |
| CN102260013A (en) | Device and method for preparing recycled water on basis of electrolysis and double-membrane technology | |
| CN202576161U (en) | Sewage treatment and regenerative cycle utilization plant | |
| CN105154908B (en) | Bipolar Membrane method reclaims lithium hydroxide technique from solution | |
| CN105084631B (en) | A kind of handling process of resin regeneration waste water | |
| CN202246327U (en) | Improved electric Fenton wastewater treatment equipment | |
| CN201809207U (en) | Novel electrolysis reactor | |
| CN107224999A (en) | A kind of resin desorption liquid method of disposal based on electrodialytic technique | |
| CN111186966A (en) | Leachate treatment device and process for garbage transfer station | |
| CN102923888B (en) | A kind of method of electrochemical treatment PVC centrifugation mother liquor | |
| CN115448525A (en) | High-salinity mine water recycling treatment process | |
| CN202046959U (en) | Reclaimed water reusing equipment | |
| CN212610147U (en) | Electroplating wastewater treatment recycling device | |
| CN204384936U (en) | A kind of multiple-unit integrated form electrolyzer | |
| CN211471140U (en) | Wastewater treatment device for PVB resin production | |
| CN202358982U (en) | System and pretreatment system for electrochemical treatment of PVC (Polyvinyl Chloride) centrifugal mother liquor | |
| CN111620502A (en) | Method and device for recycling soda water produced by nanofiltration of printing and dyeing wastewater | |
| CN206970371U (en) | A kind of casing processes sewage-treatment plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANDONG KANGCHENG PETROCHEMICAL TECHNOLOGY CO., L Free format text: FORMER OWNER: BEIJING SKTD TECHNOLOGY DEVELOPMENT CO., LTD. Effective date: 20150506 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 100036 HAIDIAN, BEIJING TO: 266100 QINGDAO, SHANDONG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20150506 Address after: 266100 No. 175, Zhuzhou Road, Laoshan District, Shandong, Qingdao Patentee after: SHANDONG KANGCHENG PETROCHEMICAL TECHNOLOGY CO., LTD. Address before: 100036, No. 103, building 15, Zhongyu business garden, 42 Fu Cheng Road, Beijing, Haidian District, B Patentee before: Beijing SKTD Co., Ltd. |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160525 Address after: 100000, room 4, floor 151, building 13, 411 Jiuxianqiao Road, Beijing, Chaoyang District Patentee after: Beijing SKTD Co., Ltd. Address before: 266100 No. 175, Zhuzhou Road, Laoshan District, Shandong, Qingdao Patentee before: SHANDONG KANGCHENG PETROCHEMICAL TECHNOLOGY CO., LTD. |
|
| 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: 20110427 Termination date: 20180825 |