CN203923409U - Eddy flow film electrolysis barrel - Google Patents
Eddy flow film electrolysis barrel Download PDFInfo
- Publication number
- CN203923409U CN203923409U CN201420188503.1U CN201420188503U CN203923409U CN 203923409 U CN203923409 U CN 203923409U CN 201420188503 U CN201420188503 U CN 201420188503U CN 203923409 U CN203923409 U CN 203923409U
- Authority
- CN
- China
- Prior art keywords
- membrane
- anode
- support
- press mold
- eddy flow
- 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 - Lifetime
Links
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 22
- 239000012528 membrane Substances 0.000 claims abstract description 57
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000012530 fluid Substances 0.000 claims abstract description 9
- 239000010936 titanium Substances 0.000 claims abstract description 9
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 9
- 239000003014 ion exchange membrane Substances 0.000 claims abstract description 7
- 150000002500 ions Chemical class 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012946 outsourcing Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model provides a kind of eddy flow film electrolysis barrel, comprises upper end cover, bottom shell, anode electrolysis chamber and catholyte chamber; Described anode electrolysis chamber is made up of main housing and the tubular anode titanium sheet being arranged in main housing, and described main housing is provided with anode liquid outlet and anode fluid inlet; It is characterized in that described catholyte chamber adopts ion-exchange membrane structure, comprise membrane support, ionic membrane, press mold support, fastening screw, described membrane support is threaded with bottom shell, ionic membrane overlays on membrane support surface part and overlaps overlapping, press mold support is wrapped in ionic membrane outside, adopt the fixing press mold support of screw rod, in the internal space that ion-exchange membrane structure surrounds, negative electrode is set.It is more convenient that it has realized the better more easily operation that fixing and ionic membrane is changed of eddy flow membrane electrolyser membrane support, alleviated artificial fitting operation amount, improved working efficiency.
Description
Technical field
The utility model relates to a kind of eddy flow film electrolysis barrel.
Background technology
Cyclone electrolytic cell technology is a kind of effective ways for separating and purifying metals, and is applicable to metallurgy industry and carries out the selective electrolysis separation of low concentration solution, complicated solution and purify, and heavy metal ions in wastewater is peeled off.Existing membrane electrolyser intermediate ion film fixed form adopts sheet frame support mostly, and the electrolyte stream flowing mode of this mode is poor compared with eddy flow state, electrolytic efficiency is lower.
Summary of the invention
The purpose of this utility model is to provide a kind of eddy flow film electrolysis barrel, to solve the deficiency in existing membrane electrolyser product.
The utility model is achieved like this, it comprises upper end cover, bottom shell, anode electrolysis chamber and catholyte chamber; Described catholyte chamber is made up of main housing and the cathode titanium sheet being arranged in main housing, and described anode electrolysis chamber is made up of main housing and the tubular anode titanium sheet being arranged in main housing, and described main housing is provided with anode liquid outlet and anode fluid inlet; It is characterized in that described catholyte chamber adopts ion-exchange membrane structure, comprise membrane support, ionic membrane, press mold support, fastening screw, described membrane support is threaded with bottom shell, ionic membrane overlays on membrane support surface, press mold support is wrapped in ionic membrane outside, adopts the fixing press mold support of screw rod, and cathode titanium rod is set in the internal space that ionic membrane surrounds, negative electrode fluid inlet and negative electrode discharge gate are set on described bottom shell, and the top of described membrane support is provided with negative electrode liquid outlet; The upper end of described main housing connects upper end cover, and described upper end cover arranges vapor pipe, anode terminal, cathode terminal, anode terminal jointed anode titanium sheet, and cathode terminal connects cathode titanium rod.
Described membrane support is stephanoporate framework, and membrane support threaded upper end is provided with falling stop limit, prevents that membrane support from coming off, and provides support power.
Described press mold support is stephanoporate framework, and seam crossing adopts screw rod closed tight or unclamp, and seam is provided with sheet rubber in limit.
Described press mold support is half-open to circle, is convenient to the replacing of ionic membrane.
The screw rod quantity of described press mold support is 6, and position is side upper, middle and lower, both sides places.
It is more convenient that the utility model is realized the better more easily operation that fixing and ionic membrane is changed of membrane support of eddy flow film electrolysis barrel, alleviated artificial fitting operation amount, improved working efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model membrane electrolyser.
Fig. 2 is the front view of ion-exchange membrane structure described in the utility model.
Fig. 3 is the vertical view of ion-exchange membrane structure described in the utility model.
Fig. 4 is vertical view of the present utility model.
1. membrane supports, 2. ionic membrane, 3. press mold support, 4. screw rod, 5. cathode titanium rod, 6. upper end cover, 601. vapor pipes, 602. cathode terminals, 603. anode terminals, 7. anode liquid outlet, 8. anode titanium sheet, 9. main housing, 10. negative electrode fluid inlet, 11. negative electrode discharge gates, 12. anode fluid inlets, 13. negative electrode liquid outlets, 14. main housings bottoms, 15. falling stop limits in the drawings.
Embodiment
As shown in Figure 1, Figure 2, Figure 3 and Figure 4, eddy flow membrane electrolyser described in the utility model comprises upper end cover 6, bottom shell 14, anode electrolysis chamber and catholyte chamber, described anode electrolysis chamber is made up of main housing 9 and the anode titanium sheet 8 being arranged in main housing 9, and described main housing 9 is provided with anode liquid outlet 7 and anode fluid inlet 12, described catholyte chamber adopts ion-exchange membrane structure, comprise membrane support 1, ionic membrane 2, press mold support 3, screw rod 4, described membrane support 1 is threaded with main housing bottom 14, ionic membrane 2 overlays on membrane support 1 surface, press mold support 3 is wrapped in ionic membrane 2 outsides, adopt the fixing press mold support 3 of screw rod 4, cathode titanium rod 5 is set in the internal space that ionic membrane 2 surrounds, on described main housing bottom 14, negative electrode fluid inlet 10 and negative electrode discharge gate 11 are set, the bottom of described membrane support 1 is provided with falling stop limit 15 and prevents that press mold support 2 from gliding, the top of described membrane support 1 is provided with negative electrode liquid outlet 13, the upper end of described main housing 9 covers with upper end cover 6, described upper end cover 6 arranges vapor pipe 601 for connecing exhausting system, upper end cover stays the hole of passing of cathode terminal 602 and anode terminal 603, and cathode terminal 602 connects cathode titanium rod 5, anode terminal 603 jointed anode titanium sheets.
Described press mold support 3 seam crossings adopt screw rod 4 closed tight or unclamp, and seam is provided with sheet rubber in limit.
Described press mold support 3 is half-open to circle, is convenient to the replacing of ionic membrane.
The screw rod quantity of described press mold support 3 is 6, and position is side upper, middle and lower, both sides places.
Described membrane support 1 is porous PP stephanoporate framework, membrane support 1 bottom is connected with the interior tooth of bottom shell 14 by outer tooth, after membrane support 1 outsourcing last layer ionic membrane 2, waste liquid in electrolyzer can be divided into cathode and anode tank room, ionic membrane 2 can stop the intercommunication of cathode and anode liquid, but allows specific ion to exchange through ionic membrane 2; Outside ionic membrane 2, install stephanoporate framework PP press mold support 3 additional, compress ionic membrane 2, prevent that loosening in electrolysis and discharge opeing process, breakage from causing anode and cathode liquid to mix; Upper end cover 6 is used for sealing cathode and anode electrolysis cylinder, reduces waste gas uncontrollable discharge, improves workshop condition, and upper end cover 6 is provided with vapor pipe 601 reserved cathode terminal 602 and anode terminal 603 through hole.
Claims (5)
1. an eddy flow film electrolysis barrel, comprises upper end cover, bottom shell, anode electrolysis chamber and catholyte chamber; Described anode electrolysis chamber is made up of main housing and the tubular anode titanium sheet being arranged in main housing, and described main housing is provided with anode liquid outlet and anode fluid inlet; It is characterized in that described catholyte chamber adopts ion-exchange membrane structure, comprise membrane support, ionic membrane, press mold support, fastening screw, described membrane support is threaded with bottom shell, ionic membrane overlays on membrane support surface, press mold support is wrapped in ionic membrane outside, adopts the fixing press mold support of screw rod, and cathode titanium rod is set in the internal space that ionic membrane surrounds, negative electrode fluid inlet and negative electrode discharge gate are set on described bottom shell, and the top of described membrane support is provided with negative electrode liquid outlet; The upper end of described main housing connects upper end cover, and described upper end cover arranges vapor pipe, anode terminal, cathode terminal, anode terminal jointed anode titanium sheet, and cathode terminal connects cathode titanium rod.
2. eddy flow film electrolysis barrel according to claim 1, is characterized in that described membrane support is stephanoporate framework, and membrane support threaded upper end is provided with falling stop limit.
3. eddy flow film electrolysis barrel according to claim 1 and 2, is characterized in that described press mold support is stephanoporate framework, and seam crossing adopts screw rod closed tight or unclamp, and seam is provided with sheet rubber in limit.
4. eddy flow film electrolysis barrel according to claim 3, is characterized in that described press mold support is for half-open to circle.
5. eddy flow film electrolysis barrel according to claim 4, the screw rod quantity that it is characterized in that described press mold support is 6, position is side upper, middle and lower, both sides places.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420188503.1U CN203923409U (en) | 2014-04-18 | 2014-04-18 | Eddy flow film electrolysis barrel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420188503.1U CN203923409U (en) | 2014-04-18 | 2014-04-18 | Eddy flow film electrolysis barrel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203923409U true CN203923409U (en) | 2014-11-05 |
Family
ID=51819264
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420188503.1U Expired - Lifetime CN203923409U (en) | 2014-04-18 | 2014-04-18 | Eddy flow film electrolysis barrel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203923409U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104726901A (en) * | 2015-03-31 | 2015-06-24 | 浙江科菲科技股份有限公司 | Diaphragm swirl-flow electrolyzer |
| CN104921255A (en) * | 2015-06-25 | 2015-09-23 | 广西大学 | Electric-field-induced free radical microorganism inactivation method |
-
2014
- 2014-04-18 CN CN201420188503.1U patent/CN203923409U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104726901A (en) * | 2015-03-31 | 2015-06-24 | 浙江科菲科技股份有限公司 | Diaphragm swirl-flow electrolyzer |
| CN104921255A (en) * | 2015-06-25 | 2015-09-23 | 广西大学 | Electric-field-induced free radical microorganism inactivation method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: No. 281, Jingjiu Avenue, Jinggangshan economic and Technological Development Zone, Ji'an City, Jiangxi Province 343100 Patentee after: Jiangxi hongban Technology Co.,Ltd. Address before: 343000 No. 281 Jingjiu Avenue, Jinggangshan National Economic and Technological Development Zone, Ji'an City, Jiangxi Province Patentee before: RED BOARD (JIANGXI) Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141105 |
|
| CX01 | Expiry of patent term |