CN207243638U - Based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment - Google Patents
Based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment Download PDFInfo
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- CN207243638U CN207243638U CN201720962038.6U CN201720962038U CN207243638U CN 207243638 U CN207243638 U CN 207243638U CN 201720962038 U CN201720962038 U CN 201720962038U CN 207243638 U CN207243638 U CN 207243638U
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Abstract
One kind is complexed sewage treatment equipment based on fenton methods processing Treatment of Industrial Park of Plating, including：Medicament electric hybrid module, medicament electric hybrid module include regulating tank and dosing tank, and regulating tank is connected by force (forcing) pump with dosing tank；Main reaction component, main reaction component include main reactor, light supply apparatus and aerator are provided with main reactor, in also setting up persevering liquid level discharging device in main reactor.The utility model is provided with light supply apparatus and aerator in main reactor, introduces ultraviolet source, can accelerate Fe3+To Fe2+Conversion and OH（Hydroxyl radical free radical）Generation, so as to improve metal complex oxidation effectiveness, the ionic state for making heavy metal ion become to precipitate by the complex pattern that can not be precipitated originally.The beneficial effects of the utility model are as follows：Efficiently solve the problems such as bottom is not cut in unstable, the contact break that the contact break of complexing waste water is reacted.The utility model can also reduce the yield of sludge, effectively reduce secondary pollution.
Description
Technical field
Electroplating sewerage processing equipment technical field is the utility model is related to, more specifically, more particularly to one kind is based on
Fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment.
Background technology
Treatment of Industrial Park of Plating is different from Common platings factory, and often the plating of product producing line is single for Common platings factory, it is dirty to produce waste water
It is more single to contaminate thing, its processing method is simple, effect stability.And in Treatment of Industrial Park of Plating, it is related to, and plating is wide, product category is more,
The waste water of generation is also corresponding complicated, and heavy metal intractability up to standard is big.
Treatment of Industrial Park of Plating complexing waste water is mainly by chemical nickle-plating wastewater, leaching zinc waste water, admiro waste water, nickel sulfamic acid
Waste water etc. forms, and such heavy metals complex compound is complicated, and discharge is irregular, and intractability is big, belongs to difficult to deal with
Waste water.Commonsense method processing, complex compound are difficult to remove, and cause heavy metal to be difficult to the emission request for reaching national regulation.Existing
Waste water treatment process in, in order to crack the influence of waste water complexing agent, progressively in treatment process increase contact break technique, mainly
Based on fenton method contact break techniques, abolishing complexing of the complexing agent on heavy metal using fenton reactions oxidisability influences.
But the complexing agent wide variety in complexing waste water, complexing ratio is fluid, is done even with fenton methods
Contact break treatment process, also can not stably reaching standard discharge.And fenton methods reaction condition requires harsh, reaction raw materials utilization rate
Low, generation sludge is more, easily produces secondary pollution.
Utility model content
（One）Technical problem
In conclusion how to solve that wastewater treatment difficulty existing for Treatment of Industrial Park of Plating waste discharge in the prior art is big, holds
Secondary pollution problems are easily caused, become those skilled in the art's urgent problem to be solved.
（Two）Technical solution
The utility model provides a kind of based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment, the equipment
Including：
For the medicament electric hybrid module pre-processed to Treatment of Industrial Park of Plating complexing waste water, the medicament electric hybrid module includes
The regulating tank for loading Treatment of Industrial Park of Plating complexing waste water and the dosing tank for storing fenton pharmacy responses are useful for, in described
One is provided with regulating tank and is used for the feed water flow gauge and a dosing pump that are controlled to inflow, on the dosing pump
Inlet tube and outlet tube are provided with, the inlet tube is connected with the dosing tank, and the outlet tube is inserted into the regulating tank
In；
For carrying out the main reaction component of contact break degradation reaction operation, the main reaction group to Treatment of Industrial Park of Plating complexing waste water
Part includes main reactor, and the main reactor is connected with the regulating tank, be provided with the main reactor light supply apparatus with
And aerator, the light supply apparatus include UV lamp body and are connected to control the lamp of the UV lamp body with the UV lamp body
Body controller, the UV lamp body are inserted into the main reactor, and the lamp body controller is arranged at outside the main reactor, institute
State aerator and include aeration pump and aeration tube, the aeration tube is arranged in the main reactor and close to the master
The bottom wall of reactive tank is set, and the aeration tube is connected with the aeration pump, in offering multiple solarization air caps in the aeration tube, in
Persevering liquid level discharging device is set in the main reactor, and the perseverance liquid level discharging device includes horizontal water pipe, described horizontal
Water pipe is arranged on the side wall of the main reactor, and one end of the horizontal water pipe is inserted into the main reactor, its end
Be connected with and be vertically arranged water pipe, it is described be vertically arranged water pipe in be vertically arranged in the main reactor, the bottom of its low side and the main reactor
It is arranged at intervals between wall, the other end of the horizontal water pipe is arranged at the outside of the main reactor, is provided with outlet valve
Door.
Preferably, in being provided with blow-down pipe on the side wall of the main reactor and close to the position of its bottom wall, put in described
Blow valve is provided with blank pipe.
Preferably, on vertical direction, the regulating tank and the dosing tank enumerate setting, the regulating tank is arranged at
The upside of the dosing tank；In in horizontal direction, the main reaction component is set up in parallel with the medicament electric hybrid module.
Preferably, the tip edge of the dosing tank is provided with ramped shaped dosing mouth.
（Three）Beneficial effect
Based on said structure design, the utility model is provided with light supply apparatus and aerator in main reactor,
Ultraviolet source is introduced on the basis of traditional fenton reactions, conversions and OH of the Fe3+ to Fe2+ can be accelerated（Hydroxyl radical free radical）
Generation.In the case where reacting equal conditions with common fenton, the utility model improves metal network due to the increase of OH concentration
Compound oxidation effectiveness, the ionic state for making heavy metal ion become to precipitate by the complex pattern that can not be precipitated originally, improves
Treatment effeciency.In addition, Fe3+Can be to Fe2+Converted, saved ferrous sulfate usage amount, while reduce sludge generation, reduced
Due to secondary pollution caused by sludge.
It is as follows by said structure design, the beneficial effects of the utility model：Efficiently solve the contact break reaction of complexing waste water
Unstable, contact break the problems such as not cutting bottom, also, the utility model can also effectively reduce the yield of sludge, effectively reduce
Secondary pollution.
Brief description of the drawings
Fig. 1 is the knot for handling Treatment of Industrial Park of Plating complexing sewage treatment equipment in the utility model embodiment based on fenton methods
Structure schematic diagram；
In figure, the correspondence of component names and accompanying drawing number is：
Regulating tank 1, dosing tank 2, feed water flow gauge 3, dosing pump 4, main reactor 5,
UV lamp body 6, lamp body controller 7, aeration pump 8, aeration tube 9.
Embodiment
The embodiment of the utility model is described in further detail with reference to the accompanying drawings and examples.Following embodiments
For illustrating the utility model, but cannot be used for limiting the scope of the utility model.
In the description of the utility model, unless otherwise indicated, " multiple " are meant that two or more；Term
The orientation or position of the instruction such as " on ", " under ", "left", "right", " interior ", " outer ", " front end ", " rear end ", " head ", " afterbody " are closed
It is to be described based on orientation shown in the drawings or position relationship, to be for only for ease of description the utility model and simplifying, rather than
Indicate or imply that signified device or element there must be specific orientation, with specific azimuth configuration and operation, therefore cannot
It is interpreted as the limitation to the utility model.In addition, term " first ", " second ", " the 3rd " etc. are only used for description purpose, and cannot
It is interpreted as indicating or implying relative importance.
, it is necessary to illustrate in the description of the utility model, unless otherwise clearly defined and limited, term " phase
Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected；Can
To be mechanical connection or be electrically connected；It can be directly connected, can also be indirectly connected by intermediary.For this
For the those of ordinary skill in field, concrete meaning of the above-mentioned term in the utility model can be understood with concrete condition.
Please refer to Fig.1, Fig. 1 is to handle Treatment of Industrial Park of Plating based on fenton methods in the utility model embodiment to be complexed at waste water
Manage the structure diagram of equipment.
The utility model provides a kind of fenton methods processing Treatment of Industrial Park of Plating that is based on and is complexed sewage treatment equipment, for reality
Now to the processing of Treatment of Industrial Park of Plating complexing waste water.
In an embodiment in the utility model, which includes：
1st, the medicament electric hybrid module for being pre-processed to Treatment of Industrial Park of Plating complexing waste water
Medicament electric hybrid module includes is complexed the regulating tank 1 of waste water and for storing for loading Treatment of Industrial Park of Plating
The dosing tank 2 of fenton pharmacy responses.Regulating tank 1 and dosing tank 2 can be made of corrosion resistant metal plate, for example with
Aluminum design designs.After surface of aluminum plate generates aluminium oxide, its corrosion resistance, which accesses, largely to be improved.Certainly, adjust
Section groove 1 and dosing tank 2 can also be adopted made of plastic, it is with the advantages that light weight, corrosion resistance is superior.
It is used for the feed water flow gauge 3 and a dosing pump that are controlled to inflow in being provided with one on regulating tank 1
4, inlet tube and outlet tube are provided with dosing pump 4, and inlet tube is connected with dosing tank 2, and outlet tube is inserted into regulating tank 1.
The amount of water of groove 1 can be controlled to adjust by feed water flow gauge 3, the fenton in dosing tank 2 can be reacted by dosing pump 4
Medicament is pumped into regulating tank 1, so that waste water is pre-mixed with fenton pharmacy responses, reacts.
2nd, for the main reaction component to Treatment of Industrial Park of Plating complexing waste water progress contact break degradation reaction operation
Main reaction component includes main reactor 5, and main reactor 5 is preferentially high, corrosion resistance and good using structural strength
Plate is made, it sprays anti-corrosion layer as optimal structural design using aluminum alloy plate materials, naturally it is also possible to using the plastic plate system of thickening
Into.
Main reactor 5 is connected with regulating tank 1, and the solution in such regulating tank 1 can just be directly inputted to main reactor 5
It is interior.Be provided with light supply apparatus and aerator in main reactor 5, light supply apparatus include UV lamp body 6 and with UV lamp body 6
The lamp body controller 7 of control UV lamp body 6 is connected to, UV lamp body 6 is inserted into main reactor 5, and lamp body controller 7 is arranged at master
Outside reactive tank 5, aerator includes aeration pump 8 and aeration tube 9, and aeration tube 9 is arranged in main reactor 5 and close to main
The bottom wall of reactive tank 5 is set, and aeration tube 9 is connected with aeration pump 8, in offering multiple solarization air caps on aeration tube 9.
In setting persevering liquid level discharging device in main reactor 5, permanent liquid level discharging device includes horizontal water pipe, horizontal water
Pipe is arranged on the side wall of main reactor 5, and one end of horizontal water pipe is inserted into main reactor 5, its end is connected with and is vertically arranged water
Pipe, is vertically arranged water pipe in being vertically arranged, be arranged at intervals between the bottom wall of its low side and main reactor 5, horizontal water pipe in main reactor 5
The other end be arranged at the outside of main reactor 5, be provided with flowing water Valve.
Based on said structure design, the utility model is provided with light supply apparatus and aerator in main reactor 5,
Ultraviolet source is introduced on the basis of traditional fenton reactions, Fe can be accelerated3+To Fe2+Conversion and OH（Hydroxyl radical free radical）
Generation.In the case where reacting equal conditions with common fenton, the utility model improves metal network due to the increase of OH concentration
Compound oxidation effectiveness, the ionic state for making heavy metal ion become to precipitate by the complex pattern that can not be precipitated originally, improves
Treatment effeciency.In addition, Fe3+Can be to Fe2+Converted, saved ferrous sulfate usage amount, while reduce sludge generation, reduced
Due to secondary pollution caused by sludge.
It is as follows by said structure design, the beneficial effects of the utility model：Efficiently solve the contact break reaction of complexing waste water
Unstable, contact break the problems such as not cutting bottom, also, the utility model can also effectively reduce the yield of sludge, effectively reduce
Secondary pollution.
In said structure design, aerator can speed up hydroxyl radical free radical generation, while disturb current, can play
The effect of mixing.
Specifically, in being provided with blow-down pipe on the side wall of main reactor 5 and close to the position of its bottom wall, on blow-down pipe
It is provided with blow valve.Blow-down pipe is set, can be by the liquid fast evacuation in main reactor 5 after equipment use.
In an embodiment of the utility model, on vertical direction, regulating tank 1 and dosing tank 2 enumerate setting,
Regulating tank 1 is arranged at the upside of dosing tank 2；In in horizontal direction, main reaction component and medicament electric hybrid module be set up in parallel.
It is added to for the ease of medicament in dosing tank 2, the tip edge of dosing tank 2 is provided with ramped shaped dosing mouth.
In the utility model, a cover board can also be set on ramped shaped dosing mouth, improve the leakproofness of dosing tank 2, ensure medicament
Clean level.
The embodiment of the utility model in order to example and description for the sake of and provide, and be not exhaustively or will
The utility model is limited to disclosed form.Many modifications and variations are aobvious and easy for the ordinary skill in the art
See.Selection and description embodiment are to more preferably illustrate the principle and practical application of the utility model, and make this area
Those of ordinary skill it will be appreciated that the utility model so as to designing various embodiments with various modifications suitable for special-purpose.
Claims (4)
1. one kind is based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment, it is characterised in that including：
For the medicament electric hybrid module pre-processed to Treatment of Industrial Park of Plating complexing waste water, the medicament electric hybrid module includes use
In the regulating tank for loading Treatment of Industrial Park of Plating complexing waste water（1）And for storing the dosing tank of fenton pharmacy responses（2）, in institute
State and a feed water flow gauge for being used to be controlled inflow is provided with regulating tank（3）An and dosing pump（4）, it is described
Inlet tube and outlet tube are provided with dosing pump, the inlet tube is connected with the dosing tank, and the outlet tube is inserted into institute
State in regulating tank；
For carrying out the main reaction component of contact break degradation reaction operation, the main reaction component bag to Treatment of Industrial Park of Plating complexing waste water
Main reactor is included（5）, the main reactor is connected with the regulating tank, be provided with the main reactor light supply apparatus and
Aerator, the light supply apparatus include UV lamp body（6）And it is connected to control the UV lamp body with the UV lamp body
Lamp body controller（7）, the UV lamp body is inserted into the main reactor, and the lamp body controller is arranged at the main reactor
Outside, the aerator includes aeration pump（8）And aeration tube（9）, the aeration tube is arranged in the main reactor, simultaneously
Bottom wall close to the main reactor is set, and the aeration tube is connected with the aeration pump, more in being offered in the aeration tube
A solarization air cap, in setting persevering liquid level discharging device in the main reactor, the perseverance liquid level discharging device includes horizontal water
Pipe, the horizontal water pipe are arranged on the side wall of the main reactor, and one end of the horizontal water pipe is inserted into the main reaction
In groove, its end be connected with and be vertically arranged water pipe, it is described be vertically arranged water pipe in be vertically arranged in the main reactor, its low side and the master
It is arranged at intervals between the bottom wall of reactive tank, the other end of the horizontal water pipe is arranged at the outside of the main reactor, sets thereon
It is equipped with flowing water Valve.
2. according to claim 1 existed based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment, its feature
In,
In being provided with blow-down pipe on the side wall of the main reactor and close to the position of its bottom wall, set on the blow-down pipe
There is blow valve.
3. according to claim 1 existed based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment, its feature
In,
In on vertical direction, the regulating tank and the dosing tank enumerate setting, the regulating tank is arranged at the dosing tank
Upside；
In in horizontal direction, the main reaction component is set up in parallel with the medicament electric hybrid module.
4. according to claim 3 existed based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment, its feature
In,
The tip edge of the dosing tank is provided with ramped shaped dosing mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720962038.6U CN207243638U (en) | 2017-08-03 | 2017-08-03 | Based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720962038.6U CN207243638U (en) | 2017-08-03 | 2017-08-03 | Based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment |
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| CN207243638U true CN207243638U (en) | 2018-04-17 |
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| CN201720962038.6U Active CN207243638U (en) | 2017-08-03 | 2017-08-03 | Based on fenton methods processing Treatment of Industrial Park of Plating complexing sewage treatment equipment |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113087117A (en) * | 2021-04-29 | 2021-07-09 | 东莞理工学院 | MXene enhanced Fenton-like oxidative degradation heavy metal complex and method for recovering heavy metal |
| CN113735323A (en) * | 2021-09-16 | 2021-12-03 | 南京大学 | Method for strengthening treatment of heavy metal complex wastewater |
| CN114515566A (en) * | 2022-01-18 | 2022-05-20 | 燕山大学 | Application of functional protein ferric oxide composite material in oxidation complex-breaking complex-state heavy metal |
| CN114634266A (en) * | 2022-04-21 | 2022-06-17 | 湖北大学 | Method for reducing COD value of waste acid in industrial production and application |
-
2017
- 2017-08-03 CN CN201720962038.6U patent/CN207243638U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113087117A (en) * | 2021-04-29 | 2021-07-09 | 东莞理工学院 | MXene enhanced Fenton-like oxidative degradation heavy metal complex and method for recovering heavy metal |
| CN113735323A (en) * | 2021-09-16 | 2021-12-03 | 南京大学 | Method for strengthening treatment of heavy metal complex wastewater |
| CN114515566A (en) * | 2022-01-18 | 2022-05-20 | 燕山大学 | Application of functional protein ferric oxide composite material in oxidation complex-breaking complex-state heavy metal |
| CN114634266A (en) * | 2022-04-21 | 2022-06-17 | 湖北大学 | Method for reducing COD value of waste acid in industrial production and application |
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