CN204058032U - A kind of three-phase overflow micro-electrolysis device - Google Patents
A kind of three-phase overflow micro-electrolysis device Download PDFInfo
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- CN204058032U CN204058032U CN201420411108.5U CN201420411108U CN204058032U CN 204058032 U CN204058032 U CN 204058032U CN 201420411108 U CN201420411108 U CN 201420411108U CN 204058032 U CN204058032 U CN 204058032U
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Abstract
The utility model provides a kind of three-phase overflow micro-electrolysis device, comprises light electrolysis groove, is provided with multiple overflow device in light electrolysis groove, and light electrolysis groove is divided into multiple light electrolysis cell by overflow device, and the bottom of each light electrolysis cell is equipped with gaseous distributer; The bottom of each light electrolysis cell, the below of gaseous distributer is provided with aeration tube and cinder cleaning hole; Described gaseous distributer is porous plate or turbogrid plates.Micro-electrolysis material blocking, passivation of hardening can effectively be avoided or reduce to the utility model, and after micro-electrolysis material surface attachment pollutent, rinse and remove easily, and micro-electrolysis material is changed also easy, makes treatment effect more stable; Overcome the easy short circuit of horizontal reactor current, the deficiency that plant factor is low, and the processing efficiency that can improve waste water.
Description
Technical field
The utility model relates to a kind of micro-electrolysis device, especially relates to a kind of three-phase overflow micro-electrolysis device.
Background technology
Micro electrolysis tech from last century the seventies by since USSR (Union of Soviet Socialist Republics) scientist utility model, theoretical investigation is ripe day by day.Micro-electrolysis method is in waste water treatment process, have applied widely, treatment effect good, use the advantages such as long, the with low cost and convenient operating maintenance of mission, and waste iron filing can be used for raw material, power consumption resource is not needed yet, there is the meaning of the treatment of wastes with processes of wastes against one another, be widely used in the wastewater treatment of the industries such as printing and dyeing, dyestuff, heavy metal, agricultural chemicals, medical oil.And there is Gas distribution inequality, liquid phase and easily produce short circuit, solid phase loadings is large, the wastewater treatment time is long, effect is unstable defect in existing micro-electrolysis device.
Summary of the invention
In order to solve the problems of the technologies described above, the utility model provides the three-phase overflow micro-electrolysis device that a kind of Gas distribution is even, waste water treatment efficiency is high, water treatment effect is stable.
The technical solution adopted in the utility model is: comprise light electrolysis groove, is provided with multiple overflow device in light electrolysis groove, and light electrolysis groove is divided into multiple light electrolysis cell by overflow device, and the bottom of each light electrolysis cell is equipped with gaseous distributer; The bottom of each light electrolysis cell, the below of gaseous distributer is provided with aeration tube and cinder cleaning hole; Described gaseous distributer is porous plate or turbogrid plates.
In above-mentioned three-phase overflow micro-electrolysis device, described light electrolysis groove is the cell body of an open topped structure.
In above-mentioned three-phase overflow micro-electrolysis device, described overflow device comprises multiple overflow plate, and the top of overflow plate is lower than the top of light electrolysis groove, and bottom is arranged in light electrolysis trough floor.
In above-mentioned three-phase overflow micro-electrolysis device, described overflow device comprises multiple overflow plate, and the top of overflow plate is lower than the top of light electrolysis groove, and bottom is arranged in light electrolysis trough floor; Be provided with underflow stream plate between adjacent overflow plate, underflow stream plate top is concordant with light electrolysis groove top, and bottom is arranged on gaseous distributer.
In above-mentioned three-phase overflow micro-electrolysis device, described gaseous distributer is porous plate, and the hole on porous plate is circular port, and diameter is 0.1-15mm.
Compared with prior art, the beneficial effects of the utility model are:
Because the utility model adopts multiple overflow device that light electrolysis groove is divided into multiple light electrolysis cell be interconnected, make waste water successively by each light electrolysis cell, not only increase reaction treatment flow process and the time of micro-electrolysis material, and micro-electrolysis material height in each light electrolysis cell is relatively low, not only the friction of aeration fluidisation is effective to micro-electrolysis material surface erosion, pollutent is not easily attached to micro-electrolysis material surface, make effective life cycle of micro-electrolysis material long, can effectively avoid or reduce the blocking of micro-electrolysis material, to harden passivation, and after micro-electrolysis material surface attachment pollutent, rinse and remove easily, it is also easy that micro-electrolysis material is changed, make treatment effect more stable.And along with the reaction times extends, micro-electrolysis material particle diminishes gradually, enters bottom through gaseous distributer, under the aeration effect of bottom, fine particle can be made to be in fluidized state, to add micro-electrolysis material and the abundant micro-electrolysis reaction of waste water, thus can improve processing efficiency.Micro-electrolysis material height is relatively low simultaneously, and when water inlet and flushing, power consumption is low.Laterally separate flow process, overcome the easy short circuit of horizontal reactor current, the deficiency that plant factor is low.Open topped type, it is more convenient that micro-electrolysis material is changed in filling, and structure is simple, and running maintenance is convenient.It is little that the utility model breaches prior art reactor volume, can not adapt to the deficiency of big yield process.
accompanying drawing explanation
Fig. 1 is the front view of embodiment 1 of the present utility model.
Fig. 2 is the vertical view of embodiment 1 of the present utility model.
Fig. 3 is the front view of embodiment 2 of the present utility model.
Fig. 4 is the vertical view of embodiment 2 of the present utility model.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further described.
Embodiment 1
As shown in Figure 1, 2, embodiment 1 of the present utility model comprises the light electrolysis groove 1 of an open topped, light electrolysis groove 1 is in hollow cuboid cell body, parallelly in light electrolysis groove 1 be provided with multiple overflow plate 2, the top of overflow plate 2 is lower than the top of light electrolysis groove 1, and bottom is arranged on the base plate of light electrolysis groove 1.Be provided with overflow plate 3 between adjacent overflow plate 2, light electrolysis groove 1 is divided into multiple light electrolysis cell by overflow plate 2 and underflow stream plate 3.The bottom of each light electrolysis cell is equipped with gaseous distributer 4, and gaseous distributer 4 is porous plate, and the cross section in the hole on porous plate is rounded, and diameter is 0.1-15mm.Gaseous distributer 4 can also be turbogrid plates.The bottom of each light electrolysis cell, the below of gaseous distributer 4 is provided with aeration tube 5 and cinder cleaning hole 6.Described adjacent underflow stream plate 3 top is concordant with the top of light electrolysis groove 1, and bottom is arranged on gaseous distributer 4.
Because embodiment 1 of the present utility model adopts overflow plate 2 and underflow stream plate 3 that light electrolysis groove 1 is divided into multiple light electrolysis cell be interconnected, make waste water successively by each light electrolysis cell, not only increase reaction treatment flow process and the time of micro-electrolysis material, and micro-electrolysis material height in each light electrolysis cell is relatively low, not only the friction of aeration fluidisation is effective to micro-electrolysis material surface erosion, pollutent is not easily attached to micro-electrolysis material surface, make effective life cycle of micro-electrolysis material long, can effectively avoid or reduce the blocking of micro-electrolysis material, to harden passivation, and after micro-electrolysis material surface attachment pollutent, rinse and remove easily, it is also easy that micro-electrolysis material is changed, make treatment effect more stable.And along with the reaction times extends, micro-electrolysis material particle diminishes gradually, enters bottom through gaseous distributer 4, under the effect of bottom aeration tube, fine particle can be made to be in fluidized state, to add micro-electrolysis material and the abundant micro-electrolysis reaction of waste water, thus can improve processing efficiency.Micro-electrolysis material height is relatively low simultaneously, and when water inlet and flushing, power consumption is low.Laterally separate flow process, overcome the easy short circuit of horizontal reactor current, the deficiency that plant factor is low.Light electrolysis groove 1 is open topped type, and it is more convenient that micro-electrolysis material is changed in filling, and structure is simple, and running maintenance is convenient.It is little that the utility model breaches prior art reactor volume, can not adapt to the deficiency of big yield process.
Embodiment 2
As shown in Figure 3,4, embodiment 2 of the present utility model comprises the light electrolysis groove 1 of an open topped, light electrolysis groove 1 is in hollow cuboid cell body, parallelly in light electrolysis groove 1 be provided with multiple overflow plate 2, the top of overflow plate 2 is lower than the top of light electrolysis groove 1, and bottom is arranged on the base plate of light electrolysis groove 1.Light electrolysis groove 1 is divided into multiple light electrolysis cell by multiple overflow plate 2.The bottom of each light electrolysis cell is equipped with gaseous distributer 4, and gaseous distributer 4 is porous plate, and the cross section, hole on porous plate is rounded, and diameter is 0.1-15mm.Gaseous distributer 4 can also be turbogrid plates.The bottom of each light electrolysis cell, the below of gaseous distributer 4 is provided with aeration tube 5 and cinder cleaning hole 6.
Because embodiment 2 of the present utility model adopts multiple overflow plate 2 that light electrolysis groove 1 is divided into multiple light electrolysis cell be interconnected, make waste water successively by each light electrolysis cell, not only increase reaction treatment flow process and the time of micro-electrolysis material, and micro-electrolysis material height in each light electrolysis cell is relatively low, not only the friction of aeration fluidisation is effective to micro-electrolysis material surface erosion, pollutent is not easily attached to micro-electrolysis material surface, make effective life cycle of micro-electrolysis material long, can effectively avoid or reduce the blocking of micro-electrolysis material, to harden passivation, and after micro-electrolysis material surface attachment pollutent, rinse and remove easily, it is also easy that micro-electrolysis material is changed, make treatment effect more stable.And along with the reaction times extends, micro-electrolysis material particle diminishes gradually, enters bottom through gaseous distributer 4, under the effect of bottom aeration tube, fine particle can be made to be in fluidized state, to add micro-electrolysis material and the abundant micro-electrolysis reaction of waste water, thus can improve processing efficiency.Micro-electrolysis material height is relatively low simultaneously, and when water inlet and flushing, power consumption is low.Laterally separate flow process, overcome the easy short circuit of horizontal reactor current, the deficiency that plant factor is low.Light electrolysis groove 1 is open topped type, and it is more convenient that micro-electrolysis material is changed in filling, and structure is simple, and running maintenance is convenient.It is little that the utility model breaches prior art reactor volume, can not adapt to the deficiency of big yield process.
Claims (4)
1. a three-phase overflow micro-electrolysis device, is characterized in that: comprise light electrolysis groove, is provided with multiple overflow device in light electrolysis groove, and light electrolysis groove is divided into multiple light electrolysis cell by overflow device, and the bottom of each light electrolysis cell is equipped with gaseous distributer; The bottom of each light electrolysis cell, the below of gaseous distributer is provided with aeration tube and cinder cleaning hole; Described gaseous distributer is porous plate or turbogrid plates.
2. three-phase overflow micro-electrolysis device according to claim 1, is characterized in that: described light electrolysis groove is the cell body of an open topped structure.
3. three-phase overflow micro-electrolysis device according to claim 1, is characterized in that: described overflow device comprises multiple overflow plate, and the top of overflow plate is lower than the top of light electrolysis groove, and bottom is arranged in light electrolysis trough floor.
4. three-phase overflow micro-electrolysis device according to claim 1, is characterized in that: described overflow device comprises multiple overflow plate, and the top of overflow plate is lower than the top of light electrolysis groove, and bottom is arranged in light electrolysis trough floor; Be provided with underflow stream plate between adjacent overflow plate, underflow stream plate top is concordant with light electrolysis groove top, and bottom is arranged on gaseous distributer.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420411108.5U CN204058032U (en) | 2014-07-24 | 2014-07-24 | A kind of three-phase overflow micro-electrolysis device |
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| CN201420411108.5U CN204058032U (en) | 2014-07-24 | 2014-07-24 | A kind of three-phase overflow micro-electrolysis device |
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| CN204058032U true CN204058032U (en) | 2014-12-31 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105540959A (en) * | 2016-02-05 | 2016-05-04 | 蓝星环境工程有限公司 | Reactor integrating microelectrolysis and Fenton technology and wastewater treatment method |
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2014
- 2014-07-24 CN CN201420411108.5U patent/CN204058032U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105540959A (en) * | 2016-02-05 | 2016-05-04 | 蓝星环境工程有限公司 | Reactor integrating microelectrolysis and Fenton technology and wastewater treatment method |
| CN105540959B (en) * | 2016-02-05 | 2018-09-21 | 蓝星环境工程有限公司 | A kind of reactor and wastewater treatment method of light electrolysis and Fenton Integration ofTechnology |
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Address after: 411100, 12, Ping'an Road, Xianfeng Bay, Xianfeng District, Xiangtan, Hunan Patentee after: HUNAN PING'AN ENVIRONMENT PROTECTION CO., LTD. Address before: 411100, Ping'an Road, Yuhu District, Hunan, Xiangtan, 12 Patentee before: HUNAN PING'AN ENVIRONMENTAL PROTECTION CO., LTD. |