CN204251447U - Separate micro-electrolysis device - Google Patents
Separate micro-electrolysis device Download PDFInfo
- Publication number
- CN204251447U CN204251447U CN201420713964.6U CN201420713964U CN204251447U CN 204251447 U CN204251447 U CN 204251447U CN 201420713964 U CN201420713964 U CN 201420713964U CN 204251447 U CN204251447 U CN 204251447U
- Authority
- CN
- China
- Prior art keywords
- stage
- reaction tower
- inlet pipe
- water inlet
- reaction
- 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
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000012856 packing Methods 0.000 claims abstract description 9
- 230000003197 catalytic effect Effects 0.000 claims abstract description 6
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims abstract description 4
- 238000005273 aeration Methods 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 230000007547 defect Effects 0.000 abstract description 6
- 238000010517 secondary reaction Methods 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 17
- 238000000034 method Methods 0.000 description 7
- 238000005553 drilling Methods 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
本实用新型公开了一种分体式撬装微电解装置。塔体内部都设置有两级反应塔、两级进水管和两级进气管。一级进水管通过提升泵与一级反应塔内的布水管相连，二级进水管与二级反应塔内的布水管相连；曝气风机分别通过一级进气主管和二级进气主管与一、二级反应塔内的布气管相连；提升泵上设置有进水口，管道上设置有加药管。所述的两级反应塔内设置有填料支撑板，填料支撑板上设置有铁碳催化填料层。水流向为下进上出。本实用新型克服了移动撬装上进行Fe/C微电解反应受高度的限制和搬迁运输的不便等缺陷。
The utility model discloses a split-type skid-mounted micro-electrolysis device. Two-stage reaction towers, two-stage water inlet pipes and two-stage air inlet pipes are arranged inside the tower body. The primary water inlet pipe is connected to the water distribution pipe in the primary reaction tower through the lifting pump, and the secondary water inlet pipe is connected to the water distribution pipe in the secondary reaction tower; The air distribution pipes in the first and second reaction towers are connected; the lift pump is provided with a water inlet, and the pipeline is provided with a dosing pipe. The two-stage reaction tower is provided with a packing support plate, and an iron-carbon catalytic packing layer is provided on the packing support plate. The water flow direction is bottom in and top out. The utility model overcomes the defects such as the limitation of the height of the Fe/C micro-electrolysis reaction on the mobile skid and the inconvenience of relocation and transportation.
Description
Technical field
The utility model relates to a kind of micro-electrolysis device, is specifically related to a kind of separate micro-electrolysis device.
Background technology
Traditional Fe/C micro-electrolysis reaction device build fixed sewage work (station) in, is not particularly limited the height of Fe/C micro-electrolysis reaction tower, and under normal circumstances, higher height is conducive to carrying out smoothly of the residence time and reaction.Touch more than 5m3/h for process rule, want to obtain better treatment effect, its tower height must not lower than 6m.But, the skid of movable type uses Fe/C electrolysis process, due to the restriction of the factors such as transport and scene, will below 2.5m be limited in the height of Fe/C reaction tower.Therefore, in order to meet needed for Fe/C micro-electrolysis reaction the conditions such as the convenience of the abundant and movable and skid-mounted resettlement transport of the residence time, contact reacts, spy has created " micro-electrolysis reaction device of separate three-dimensional arrangement ".
Utility model content
Because the above-mentioned defect of prior art, the utility model provides a kind of separate micro-electrolysis device, the catalytic oxidation technique formed under the acting in conjunction of efficient Fe/C micro-electrolysis stuffing and Femon reagent etc., can more than 80% be reached to the organic cod clearance in well-drilling waste water, overcome other Fe/C technique to the defect of the organic cod clearance in well-drilling waste water low (being generally no more than 50%); Overcome movable and skid-mounted on carry out the defect such as inconvenience of Fe/C micro-electrolysis reaction by the restriction of height and resettlement transport.
For achieving the above object, the utility model provides a kind of separate micro-electrolysis device, comprise tower body, two-stage reaction tower, two-stage water inlet pipe and two-stage inlet pipe, tower body inside is all provided with two-stage reaction tower, two-stage water inlet pipe and two-stage inlet pipe, one-level water inlet pipe is connected with the water distributor in first order reaction tower by lift pump, and secondary water inlet pipe is connected with the water distributor in second order reaction tower; Aeration fan is connected with the gas distribution pipe in first order reaction tower, second order reaction tower with secondary inlet supervisor respectively by one-level air inlet supervisor; Lift pump is provided with water-in, pipeline is provided with chemical feed pipe.
As preferably, in described two-stage reaction tower, be provided with packing support plate, packing support plate be provided with iron carbon catalytic filler layer.
The beneficial effects of the utility model: (1), tower height degree are down to 2.5m from 6m or higher, can carry out Fe/C micro-electrolysis reaction smoothly in the skid of movable type, are convenient to resettlement transport.
(2) extended residence time needed for Fe/C micro-electrolysis reaction, contact reacts, can be made more abundant.
(3), convenient midway adjust ph, extend light electrolysis in acid (when pH value is between 4 ~ 6, reaction efficiency the is higher) reaction times, make micro-electrolysis reaction more fully, more thorough.More traditional its reaction efficiency of Fe/C weak electrolysis mechanism carries more than 20%.
Be described further below with reference to the technique effect of accompanying drawing to design of the present utility model, concrete structure and generation, to understand the purpose of this utility model, characteristic sum effect fully.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
With reference to Fig. 1, this embodiment is by the following technical solutions: separate micro-electrolysis device, comprise tower body, two-stage reaction tower, two-stage water inlet pipe and two-stage inlet pipe, tower body 1 inside is all provided with two-stage reaction tower, two-stage water inlet pipe and two-stage inlet pipe, one-level water inlet pipe 20 is connected with the water distributor 10 in first order reaction tower 2 by lift pump 19, and secondary water inlet pipe 4 is connected with the water distributor 10 in second order reaction tower 6; Aeration fan 8 is connected with the gas distribution pipe 11 in first order reaction tower, second order reaction tower with secondary inlet supervisor 5 respectively by one-level air inlet supervisor 3; Lift pump 19 is provided with water-in 20, pipeline is provided with chemical feed pipe 21.
It should be noted that in described two-stage reaction tower and be provided with packing support plate 13, packing support plate 13 is provided with iron carbon catalytic filler layer 12, above secondary water inlet pipe 4 end, is provided with rising pipe 7.
The catalytic oxidation technique that this embodiment is formed under the acting in conjunction of efficient Fe/C micro-electrolysis stuffing and Femon reagent etc., can more than 80% be reached to the organic cod clearance in well-drilling waste water, overcome other Fe/C technique to the defect of the organic cod clearance in well-drilling waste water low (being generally no more than 50%); Overcome movable and skid-mounted on carry out the defect such as inconvenience of Fe/C micro-electrolysis reaction by the restriction of height and resettlement transport.
The tower height degree of this embodiment is down to 2.5m from 6m or higher, can carry out Fe/C micro-electrolysis reaction smoothly in the skid of movable type, is convenient to resettlement transport.Extended residence time needed for Fe/C micro-electrolysis reaction, contact reacts can be made more abundant.Convenient midway adjust ph, extends light electrolysis in acid (when pH value is between 4 ~ 6, reaction efficiency the is higher) reaction times, make micro-electrolysis reaction more fully, more thorough.More traditional its reaction efficiency of Fe/C weak electrolysis mechanism carries more than 20%.
More than describe preferred embodiment of the present utility model in detail.Should be appreciated that those of ordinary skill in the art just can make many modifications and variations according to design of the present utility model without the need to creative work.Therefore, all technician in the art according to design of the present utility model on the basis of existing technology by the available technical scheme of logical analysis, reasoning, or a limited experiment, all should by the determined protection domain of claims.
Claims (2)
1. separate micro-electrolysis device, it is characterized in that, comprise tower body, two-stage reaction tower, two-stage water inlet pipe and two-stage inlet pipe, tower body (1) inside is all provided with two-stage reaction tower, two-stage water inlet pipe and two-stage inlet pipe, one-level water inlet pipe (20) is connected with the water distributor (10) in first order reaction tower (2) by lift pump (19), and secondary water inlet pipe (4) is connected with the water distributor (10) in second order reaction tower (6); Aeration fan (8) is connected with the gas distribution pipe (11) in first order reaction tower, second order reaction tower with secondary inlet supervisor (5) respectively by one-level air inlet supervisor (3); Lift pump (19) is provided with water-in (20), pipeline is provided with chemical feed pipe (21).
2. separate micro-electrolysis device according to claim 1, it is characterized in that, be provided with packing support plate (13) in described two-stage reaction tower, packing support plate (13) be provided with iron carbon catalytic filler layer (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420713964.6U CN204251447U (en) | 2014-11-25 | 2014-11-25 | Separate micro-electrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420713964.6U CN204251447U (en) | 2014-11-25 | 2014-11-25 | Separate micro-electrolysis device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204251447U true CN204251447U (en) | 2015-04-08 |
Family
ID=52955774
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420713964.6U Expired - Fee Related CN204251447U (en) | 2014-11-25 | 2014-11-25 | Separate micro-electrolysis device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204251447U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106335974A (en) * | 2016-10-23 | 2017-01-18 | 中海油天津化工研究设计院有限公司 | Hardening-preventing and energy-saving microelectrolysis-Fenton reactor |
-
2014
- 2014-11-25 CN CN201420713964.6U patent/CN204251447U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106335974A (en) * | 2016-10-23 | 2017-01-18 | 中海油天津化工研究设计院有限公司 | Hardening-preventing and energy-saving microelectrolysis-Fenton reactor |
| CN106335974B (en) * | 2016-10-23 | 2019-06-28 | 中海油天津化工研究设计院有限公司 | A kind of anti-compaction energy conservation light electrolysis-Fenton reactor |
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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: 20150408 |