CN206502646U - Efficient micro-electrolysis reactor - Google Patents
Efficient micro-electrolysis reactor Download PDFInfo
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- CN206502646U CN206502646U CN201621254210.4U CN201621254210U CN206502646U CN 206502646 U CN206502646 U CN 206502646U CN 201621254210 U CN201621254210 U CN 201621254210U CN 206502646 U CN206502646 U CN 206502646U
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- reactor body
- agitating paddle
- water
- inlet pipe
- efficient micro
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Abstract
The utility model belongs to field of waste water treatment, a kind of efficient micro-electrolysis reactor, including reactor body, water intake mechanism, admission gear, rabbling mechanism, charging mechanism and three phase separation mechanism；Admission gear includes being arranged on air chamber, air inlet pipe and the orifice plate of reactor body bottom；Water intake mechanism is arranged on the top of admission gear, and three phase separation mechanism is located in the middle part of reactor body；Rabbling mechanism includes agitating shaft and the first agitating paddle and the second agitating paddle that are arranged on agitating shaft, first agitating paddle is located at the top of water intake mechanism, second agitating paddle is located between water intake mechanism and admission gear, first agitating paddle stirs material in reactor body towards the second agitating paddle, and the second agitating paddle stirs material in reactor body towards the first agitating paddle.Double-stirring machine structure in the application, not only to stir, and avoid the problem of aggregation results in blockage above orifice plate；Admission gear and water intake mechanism can also reach stirring action simultaneously.
Description
Technical field
The utility model belongs to field of waste water treatment, more particularly to a kind of efficient micro-electrolysis reactor.
Background technology
Micro-electrolysis method is to utilize Principles of Metal Erosion, forms the good process that galvanic cell is handled waste water.The technique
Since be born just cause many national attention.Change method to be widely used in printing and dyeing, heavy metal, pharmacy, have a waste water
It is a kind of emerging electrochemical method Deng in sewage disposal, it has using spies such as wide, the simple, high treating effects of technique of scope
Point, particularly with high salinity, high COD and the higher waste water of colourity treatment effect have compared with other techniques it is more obvious excellent
Gesture.
But difficult point arrogant in weak electrolysis mechanism is that iron carbon easily lumps, the problem of easily producing blocking causes processing
Efficiency is low, or even needs shutdown to handle.
Utility model content
The purpose of this utility model is that the light electrolysis for overcoming prior art to exist easily produces the defect of blocking there is provided one kind
Efficient micro-electrolysis reactor.
The utility model solves the technical scheme that its technical problem used：A kind of efficient micro-electrolysis reactor, including
Reactor body, water intake mechanism, admission gear, rabbling mechanism, charging mechanism and three phase separation mechanism；
The admission gear includes the air chamber for being arranged on the reactor body bottom, the air inlet pipe connected with the air chamber
With the orifice plate for separating the air chamber and above-mentioned reactor body inner chamber body；
The water intake mechanism is arranged on the top of the admission gear, and the three phase separation mechanism is located at the reactor sheet
In the middle part of body；The rabbling mechanism includes agitating shaft and the first agitating paddle and the second agitating paddle that are arranged on the agitating shaft, institute
State the first agitating paddle be located at the water intake mechanism top, second agitating paddle be located at the water intake mechanism and it is described enter mechanism of qi
Between structure, first agitating paddle stirs material in the reactor body towards second agitating paddle, and described second stirs
Oar is mixed to stir material in the reactor body towards first agitating paddle.
Further, in a ring, its side is provided with the air inlet being connected with source of the gas, the air inlet pipe to described air inlet pipe
On be provided with the venthole that Open Side Down.The air inlet pipe of annular causes gas more uniform in gas indoor distribution, and venthole
Setting that Open Side Down can be prevented effectively from venthole and directly be entered the blocking such as particle of air inlet chamber by orifice plate, while gas is by hole
Plate enters reactor body, and orifice plate can again be distributed to gas so that gas is distributed more equal in reactor body
It is even, while playing stirring action to material in reactor body, be conducive to avoiding material from luming.
Preferably, described water intake mechanism includes water inlet pipe, water distribution ring, the water distribution ring is arranged on the reactor sheet
In vivo, the water inlet pipe is used to connecting going out of being provided with that Open Side Down on the water distribution ring and external source, described water distribution ring
Water hole.It is similar with admission gear, using annular water distribution ring, be conducive into water uniformly, effectively improving waste water and gas and iron carbon
The uniform contact of material, is conducive to the uniformity and adequacy of micro-electrolysis reaction, and Open Side Down sets and can have for apopore
Effect avoids apopore from being blocked by iron carbon filler particle, caking or flocculate precipitate etc.；Water intake mechanism can be effectively to reaction simultaneously
Material is stirred in device main body.
Preferably, described water intake mechanism also includes inclined tube, described inclined tube one end is connected with the water inlet pipe, the other end
Stretch into the reactor body, and set towards the water distribution ring bottom.Because water intake mechanism is located at the bottom of reactor body
Portion, material easily lumps in bottom precipitation, and generation stopping state is more, can be effectively to water distribution ring using inclined tube when blocking
Bottom position is rinsed, it is to avoid the generation of stopping state；Or interruption opens inclined tube water inlet, and water distribution ring bottom is rushed
Wash, reach the effect of pulse lavage, it is to avoid the blocking of water intake mechanism.
Further, for ease of the water inlet of control water distribution ring or inclined tube, the first control valve is provided with described water inlet pipe,
Be provided with the second control valve on the inclined tube, first control valve be arranged at the junction of the inclined tube and the water inlet pipe with
Between the water distribution ring.
Further, the water inlet end of described water inlet pipe is connected with Venturi tube, and the negative port of the Venturi tube is made
For acid solution charge door, there is magnetic field at the trunnion of the Venturi tube.Intake using Venturi tube, form negative at negative port
Pressure, reaches the purpose of automatical dosing, while flow rate of liquid is higher at Venturi tube trunnion, liquid cutting magnetic induction line produce electric current compared with
Greatly, the effect of preliminary light electrolysis is reached, light electrolysis effect is improved, while having sterilization, the effect of broken wall.
Specifically, described charging mechanism includes casing drum, charging spout and screw meter, and described casing drum one end is stretched into
In the reactor body, the other end is connected by screw meter with the charging spout.Can first it be added by charging mechanism
Disposable carbon material, then be interrupted during the course of the reaction or continuous and quantitative addition iron material by screw meter so that iron material
Make full use of, it is to avoid iron material deposit clumps.
Further, for ease of the gas in reactor body is discharged, the three phase separation mechanism has emptying pipeline
It is in communication with the outside.
Preferably, described reactor body upper dimension is more than the size of its underpart, size is smaller larger to size
Section transitions part forms settling zone, and the settling zone top is provided with downflow weir；The settling zone is provided with towards described anti-
The precipitation plate for answering device body sidewall slope to set.Reactor upper dimension becomes big so that flow rate of liquid is slack-off, is conducive to not three
The particle of precipitation precipitates under transition region and precipitation plate effect in phase separation mechanism, prevents iron carbon material in reactor body
By the loss of downflow weir.
Further, described reactor body bottom and the air chamber bottom are provided with drain.Utilize drain
When can be lumpd in reactor body, in air chamber or block serious, emptying manipulation is carried out.
Beneficial effect：Double-stirring machine structure is set in the application between admission gear and water intake mechanism, in two agitating paddles
Bottoms material is stirred towards top stirring, top material towards bottom under effect, not only to stir, and can be by
The iron carbon and flocculate on orifice plate top are stirred upwards, it is to avoid the problem of aggregation results in blockage above orifice plate；Admission gear and enter
Water dispenser structure can also reach simultaneously has multiple stirring in stirring action, the application, can be prevented effectively from the caking of iron carbon, it is to avoid stifled
Plug.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
Fig. 1 is the utility model micro-electrolysis reactor structural representation；
Fig. 2 is schematic enlarged-scale view at A in Fig. 1；
Fig. 3 is schematic enlarged-scale view at B in Fig. 1；
Fig. 4 is rabbling mechanism structural representation；
Fig. 5 is charging mechanism structural representation.
Wherein:1. reactor body, 11. transition portions, 12. precipitation plates, 13. downflow weirs, 14. drains, 2. enter water dispenser
Structure, 21. water inlet pipes, 22. water distribution rings, 23. inclined tubes, 3. admission gears, 31. air chambers, 32. air inlet pipe, 33. orifice plates, 4. chargers
Structure, 41. casing drums, 42. charging spouts, 43. screw meters, 5. three phase separation mechanisms, 51. emptying pipelines, 6. agitating shafts, 7. the
One agitating paddle, 8. second agitating paddles, 9. Venturi tubes, 91. negative ports, 92. trunnions, 93. magnet coils.
Embodiment
Embodiment 1
As shown in figure 1, a kind of efficient micro-electrolysis reactor, including reactor body 1, water intake mechanism 2, admission gear 3, stir
Mix mechanism, charging mechanism 4 and three phase separation mechanism 5；
As illustrated in fig. 1 and 2, the admission gear 3 includes air chamber 31 and the institute for being arranged on the bottom of reactor body 1
The orifice plate 33 stated the air inlet pipe 32 of the connection of air chamber 31 and separate the air chamber 31 and the inner chamber body of reactor body 1, institute
The air inlet pipe 32 stated in a ring, its side be provided with the air inlet being connected with source of the gas, the air inlet pipe 32 be provided with opening to
Under venthole；
As illustrated in fig. 1 and 2, the water intake mechanism 2 is arranged on the top of the admission gear 3, including water inlet pipe 21, water distribution
Circle 22, the water distribution ring 22 is arranged in the reactor body 1, and the water inlet pipe 21 is used to connect the water distribution ring 22 and outer
Boundary water source, as shown in figure 3, the water inlet end of described water inlet pipe 21 is connected with Venturi tube 9, the negative pressure of the Venturi tube 9 connects
Mouthfuls 91 as acid solution charge door, has magnetic field (can be real by magnet coil 93 or strong magnet at the trunnion 92 of the Venturi tube 9
Now), the apopore that Open Side Down is provided with described water distribution ring 22, described water intake mechanism 2 also includes inclined tube 23, described oblique
The one end of pipe 23 is connected with the water inlet pipe 21, and the other end is stretched into the reactor body 1, and towards the bottom of water distribution ring 22
Set, be provided with described water inlet pipe 21 on the first control valve, the inclined tube 23 and be provided with the second control valve, first control
Valve processed is arranged between the inclined tube 23 and the junction of the water inlet pipe 21 and the water distribution ring 22.
As shown in figure 4, the rabbling mechanism include agitating shaft 6 and the first agitating paddle 7 for being arranged on the agitating shaft 6 with
Second agitating paddle 8, first agitating paddle 7 is located at the top of the water intake mechanism 2, and second agitating paddle 8 enters described in
Between water dispenser structure 2 and the admission gear 3, first agitating paddle 7 is by material in the reactor body 1 towards described second
Agitating paddle 8 is stirred, and second agitating paddle 8 stirs material in the reactor body 1 towards first agitating paddle 7.
As shown in figure 5, described charging mechanism 4 includes casing drum 41, charging spout 42 and screw meter 43, the charging
41 one end of cylinder are stretched into the reactor body 1, and the other end is connected by screw meter 43 with the charging spout 42.
As shown in figure 1, the three phase separation mechanism 5 is located at the middle part of reactor body 1, it has emptying pipeline 51,
And be in communication with the outside by emptying pipeline 51；The described upper dimension of reactor body 1 is more than the size of its underpart, and size is smaller
To the formation of size major part transition portion 11 settling zone, the settling zone top is provided with downflow weir 13；The settling zone is set
It is equipped with the precipitation plate 12 set towards the sidewall slope of reactor body 1.The described bottom of reactor body 1 and the air chamber
31 bottoms are provided with drain 14.
Operation principle is as follows：Carried by casing drum 41 to reaction and carbon material is added in main body, and from water inlet pipe 21 to reaction
Be passed through waste water in device main body, at the same by charging spout 42 and screw meter 43 and casing drum 41 into reactor body it is continuous
It is quantitatively adding iron material；When waste water passes through Venturi tube 9, the cutting magnetic induction line at trunnion 92 so that waste water is powered, and occur electricity
Solution is reacted and reaches sterilization effect, while adding acid at the negative port 91 of Venturi tube 9 according to wastewater property.Waste water is by cloth
The apopore of hydrosphere 22 enters reactor body, while gas enters air inlet chamber 31 by the venthole of air inlet pipe 32, and passes through orifice plate
33 are uniformly passed through in reactor body.Material further produces micro-electrolysis reaction under the effect of iron carbon material in reactor body,
Agitating device is stirred simultaneously, and the second agitating paddle 8 stirs the material on the top of orifice plate 33 towards top in the process, and first
Agitating paddle 7 stirs the material on reactor body top towards bottom, forms circulation so that waste water and iron carbon in reactor body
Material is well mixed so that the waste water that the waste water in reactor body enters with water inlet pipe 21 is sufficiently mixed, and reaction is abundant, without dead
Angle, while avoiding solid accumulation at orifice plate 33 and water inlet pipe 21 from blocking.When the accumulation of the bottoms material of water distribution ring 22 is more, open oblique
Pipe 23 is intake, and effectively can be broken up the material of accumulation using inclined tube 23, it is to avoid the blocking of water intake mechanism 2.
Waste water carries out solid-liquid-gas three phase separation after micro-electrolysis reaction through three phase separation mechanism 5, and gas is by emptying pipeline 51
Empty, the particle such as iron carbon is precipitated to the bottom of three phase separation mechanism 5, and reacted liquid reaches the top of reactor body, passes through
Changeover portion flow velocity is reduced suddenly, is conducive to further precipitating the particulate matters such as wherein subsidiary iron carbon, it is to avoid its with liquid by
The overflow of downflow weir 13 is discharged.
It should be appreciated that specific embodiment described above is only used for explaining the utility model, it is not used to limit this reality
With new.The obvious changes or variations extended out by spirit of the present utility model is still in protection of the present utility model
Among scope.
Claims (10)
1. a kind of efficient micro-electrolysis reactor, it is characterised in that：Including reactor body (1), water intake mechanism (2), admission gear
(3), rabbling mechanism, charging mechanism (4) and three phase separation mechanism (5)；
The admission gear (3) includes being arranged on the air chamber (31) of the reactor body (1) bottom, connected with the air chamber (31)
Logical air inlet pipe (32) and the orifice plate (33) for separating the air chamber (31) and the reactor body (1) inner chamber body；
The water intake mechanism (2) is arranged on the top of the admission gear (3), and the three phase separation mechanism (5) is located at described anti-
Answer in the middle part of device main body (1)；The rabbling mechanism includes agitating shaft (6) and the first agitating paddle being arranged on the agitating shaft (6)
(7) with the second agitating paddle (8), first agitating paddle (7) is located at the top of the water intake mechanism (2), second agitating paddle
(8) it is located between the water intake mechanism (2) and the admission gear (3), first agitating paddle (7) is by the reactor body
(1) interior material is stirred towards second agitating paddle (8), and second agitating paddle (8) is by the reactor body (1) interior material
Towards first agitating paddle (7) stirring.
2. efficient micro-electrolysis reactor according to claim 1, it is characterised in that：Described air inlet pipe (32) in a ring,
Its side is provided with the air inlet being connected with source of the gas, the air inlet pipe (32) and is provided with the venthole that Open Side Down.
3. efficient micro-electrolysis reactor according to claim 1, it is characterised in that：Described water intake mechanism (2) include into
Water pipe (21), water distribution ring (22), the water distribution ring (22) are arranged in the reactor body (1), and the water inlet pipe (21) is used
In connecting the apopore that Open Side Down is provided with the water distribution ring (22) and external source, described water distribution ring (22).
4. efficient micro-electrolysis reactor according to claim 3, it is characterised in that：Described water intake mechanism (2) also includes
Inclined tube (23), described inclined tube (23) one end is connected with the water inlet pipe (21), and the other end is stretched into the reactor body (1),
And set towards the water distribution ring (22) bottom.
5. efficient micro-electrolysis reactor according to claim 4, it is characterised in that：It is provided with described water inlet pipe (21)
Be provided with the second control valve on first control valve, the inclined tube (23), first control valve be arranged at the inclined tube (23) and
Between the junction of the water inlet pipe (21) and the water distribution ring (22).
6. the efficient micro-electrolysis reactor according to claim 3 or 4, it is characterised in that：Described water inlet pipe (21) are entered
Water end (W.E.) is connected with Venturi tube (9), and the negative port (91) of the Venturi tube (9) is used as acid solution charge door, the venturi
Trunnion (92) place of pipe (9) has magnetic field.
7. efficient micro-electrolysis reactor according to claim 1, it is characterised in that：Described charging mechanism (4) includes adding
The reactor body (1) is stretched into barrel (41), charging spout (42) and screw meter (43), described casing drum (41) one end
Interior, the other end is connected by screw meter (43) with the charging spout (42).
8. efficient micro-electrolysis reactor according to claim 1, it is characterised in that：The three phase separation mechanism (5) has
Emptying pipeline (51) is in communication with the outside.
9. efficient micro-electrolysis reactor according to claim 1, it is characterised in that：Described reactor body (1) top
Size is more than the size of its underpart, and size is smaller to size major part transition portion (11) formation settling zone, the settling zone
Top is provided with downflow weir (13)；The settling zone is provided with the precipitation set towards the reactor body (1) sidewall slope
Plate (12).
10. efficient micro-electrolysis reactor according to claim 1, it is characterised in that：Described reactor body (1) bottom
Drain (14) is provided with the air chamber (31) bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621254210.4U CN206502646U (en) | 2016-11-22 | 2016-11-22 | Efficient micro-electrolysis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621254210.4U CN206502646U (en) | 2016-11-22 | 2016-11-22 | Efficient micro-electrolysis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206502646U true CN206502646U (en) | 2017-09-19 |
Family
ID=59842638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621254210.4U Active CN206502646U (en) | 2016-11-22 | 2016-11-22 | Efficient micro-electrolysis reactor |
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| Country | Link |
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| CN (1) | CN206502646U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107619099A (en) * | 2017-10-17 | 2018-01-23 | 中冶赛迪技术研究中心有限公司 | Internal-circulation type Fenton reactor |
| CN108083390A (en) * | 2016-11-22 | 2018-05-29 | 山西宝晟源机电设备有限公司 | Efficient micro-electrolysis reactor |
-
2016
- 2016-11-22 CN CN201621254210.4U patent/CN206502646U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108083390A (en) * | 2016-11-22 | 2018-05-29 | 山西宝晟源机电设备有限公司 | Efficient micro-electrolysis reactor |
| CN107619099A (en) * | 2017-10-17 | 2018-01-23 | 中冶赛迪技术研究中心有限公司 | Internal-circulation type Fenton reactor |
| CN107619099B (en) * | 2017-10-17 | 2024-02-23 | 中冶赛迪技术研究中心有限公司 | Internal circulation Fenton reactor |
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