CN107619129A - A kind of electroplating waste processing equipment - Google Patents
A kind of electroplating waste processing equipment Download PDFInfo
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- CN107619129A CN107619129A CN201711041043.4A CN201711041043A CN107619129A CN 107619129 A CN107619129 A CN 107619129A CN 201711041043 A CN201711041043 A CN 201711041043A CN 107619129 A CN107619129 A CN 107619129A
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Abstract
The present invention provides a kind of electroplating waste processing equipment, a kind of electroplating waste processing equipment can be by clarifier generating means and wastewater treatment equipment organic integration, so as to realize the whole-course automation of the preparation of cleanser and wastewater treatment, further, absorption also to suspended things is improved, by setting absorption stake to realize, the first time for waste water suspension filters, and by being gone out in waste water via adsorption tank bottom percolation during set porous layer and filter layer to realize second of filtering for waste water suspension, improve the adsorption effect of suspension.
Description
Technical field
The present invention relates to environmental protection machinery, more particularly to a kind of electroplating waste processing equipment.
Background technology
The processing method of heavy metal wastewater thereby has many kinds at present, for example, the alkali formula precipitation method, ion-exchange, electroosmose process,
Hyperfiltration, electric flocculation method etc..What application was most at present is the alkali formula precipitation method, is exactly only by adding alkali to adjust pH value, makes a huge sum of money
Belong to the method that ion forms hydroxide precipitation and removed.This method technique is simple, operation easily, build and operating cost compared with
It is low, but shortcoming be the optimal precipitation of various heavy metal ion pH value range it is different, it is necessary to stage agent addition precipitate, if waste water
In be mixed with complex ion, some ions are difficult to qualified discharge standard.Ion-exchange is to utilize the friendship in ion exchange resin
Change ion to swap and be removed with some ions in heavy metal wastewater thereby, the method for being purified waste water, this method
The shortcomings that be resin price costly, operating cost is high, and resin regeneration is more difficult, and concentrated water is difficult.In heavy metal wastewater thereby
Heavy metals removal method is although various, but is all difficult to full automatic purification of waste water, and reason is in waste water removal process and gives up
Water removal is to be divided to realize that therefore, it is difficult to realize whole-course automation in two steps with the preparation of cleanser.
Further, substantial amounts of suspension is there is likely to be in heavy metal wastewater thereby.Suspension refers to the solid being suspended in water
Material is the main reason for causing water muddiness.Suspended material in water is particulate of the particle diameter about between 10nm-0.1um.
It is visually visible.These particulates are mainly by silt, clay, protozoan, algae, bacterium, virus and macromolecule organic etc.
Composition, is usually suspended among current.Turbid phenomenon caused by water, also all it is as caused by this class material.
The processing of suspension is typically the first step or second step of water process, and effective processing for suspension is water process
One of committed step, it is therefore necessary to it is constantly optimized.
The content of the invention
In order to solve the above-mentioned technical problem, the present invention provides a kind of electroplating waste processing equipment.
The present invention is realized with following technical scheme：
A kind of electroplating waste processing equipment, including adsorption tank side described in adsorption tank and the clarifier-tank that is connected with the adsorption tank
Wall opens up a water inlet, and the water inlet connects with the first control valve, and the water inlet flows into for waste water, the adsorption tank bottom
Portion is connected with the entrance of a funnel type pipeline, and the outlet of the funnel type pipeline is with the entrance of the clarifier-tank by the second control
Valve connects, and the level height of the adsorption tank is higher than the clarifier-tank；The shape of the funnel type entrance and the absorption
The shape in bottom of pond portion is consistent, and waste water flows out the adsorption tank via the outlet of the funnel type pipeline；
The clarifier-tank is connected in order to caused by the cleanser by the 3rd control valve with a cleanser generating means
Cleanser instills clarifier-tank, and first control valve, the second control valve and the 3rd control valve are controlled by an intelligent controller；
The cleanser generating means includes the first reagent locker room, the second reagent locker room, the 3rd reagent locker room, the
Four reagent locker rooms, the 5th reagent locker room and mixing chamber；
The first reagent locker room is connected with mixing chamber by the first controlling valve, and the second reagent locker room is with mixing
Room is connected by the second controlling valve, and the 3rd reagent locker room is connected with mixing chamber by the 3rd controlling valve, the 4th examination
Agent locker room is connected with mixing chamber by the 4th controlling valve, and the 5th reagent locker room is connected with mixing chamber by the 5th control valve
It is logical.
Further, the purification agent generator also includes master controller, first controlling valve, the second controlling valve, the
Three controlling valves, the 4th controlling valve and the 5th controlling valve are controlled by the master controller.
Further, some absorption stakes are laid with the adsorption tank, the absorption stake is by stake bottom and is laid in the stake
Pile body on bottom is formed, and for the outer wall of the pile body by net high-polymer rings of material around generation, the pile body inside is hollow knot
Structure, its accommodated inside have granular adsorbent, and waste water contacts through the outer wall with the granular adsorbent；
The adsorption tank bottom is equipped with porous layer and filter layer successively according to order from top to bottom.
Further, the filter layer is equipped with resin coating core, and core aperture is 20-40um.
Further, the porous layer is formed by the laying of cellular high polymer material, between the cellular high polymer material
Gap is uniformly placed with one or more biological adsorption agent particles after modified processing.
The beneficial effects of the invention are as follows：
The present invention provides a kind of electroplating waste processing equipment, and a kind of electroplating waste processing equipment can send out clarifier
Generating apparatus and wastewater treatment equipment organic integration, so as to realize the whole-course automation of the preparation of cleanser and wastewater treatment, enter one
Step ground, the also absorption to suspended things are improved, and by setting absorption stake to realize, the first time for waste water suspension filters,
And by being gone out in waste water via adsorption tank bottom percolation during set porous layer and filter layer to realize to suspend for waste water
Second of filtering of thing, improve the adsorption effect of suspension.
Brief description of the drawings
Fig. 1 is a kind of front view for electroplating waste processing equipment that the present embodiment provides；
Wherein：1- adsorption tanks, 2- absorption stakes, 21- stakes bottom, 22- pile bodies, 3- porous layers, 4- filter layers, 10- water inlets,
The control valves of 100- first, 5- funnel type pipelines；01- clarifier-tanks, the control valves of 200- second, the control valves of 300- the 3rd, 04- cleansers
Generating means, 05- intelligent controllers, the first reagents of 041- locker room, the second reagents of 042- locker room, the storage of the reagents of 043- the 3rd
Room, the reagent locker rooms of 044- the 4th, the reagent locker rooms of 045- the 5th, 046- mixing chambers, 047- master controllers, 001- first regulate and control
Valve, the controlling valves of 002- second, the controlling valves of 003- the 3rd, the controlling valves of 004- the 4th, the controlling valves of 005- the 5th.
Embodiment
To make the object, technical solutions and advantages of the present invention clearer, the present invention is made into one below in conjunction with accompanying drawing
It is described in detail on step ground.
Embodiment 1：
A kind of electroplating waste processing equipment, as shown in figure 1, including：
The clarifier-tank 01 connected including adsorption tank 1 and with the adsorption tank, the side wall of adsorption tank 1 open up a water inlet
10, the water inlet 10 connects with the first control valve 100, and the water inlet 10 flows into for waste water；The bottom of adsorption tank 1 with
The entrance of one funnel type pipeline 5 connects, and the shape of the entrance of funnel type pipeline 5 is consistent with the shape of the bottom of adsorption tank 1, gives up
Water flows out the adsorption tank 1, outlet and the clarifier-tank of the funnel type pipeline 5 via the outlet of the funnel type pipeline 5
01 entrance connects by the second control valve 200, and the level height of the adsorption tank 1 is higher than the clarifier-tank 01；
The clarifier-tank 01 is connected in order to the cleanser by the 3rd control valve 300 with a cleanser generating means 04
Cleanser caused by generating means 04 instills clarifier-tank 01, first control valve 100, the second control valve 200 and the 3rd control
Valve 300 is controlled by an intelligent controller 05；
The cleanser generating means 04 includes the first reagent locker room 041, the second reagent locker room 042, the 3rd reagent
Locker room 043, the 4th reagent locker room 044, the 5th reagent locker room 045 and mixing chamber 046.
The first reagent locker room 041 is connected with mixing chamber 046 by the first controlling valve 001, and second reagent is deposited
Storage chamber 042 is connected with mixing chamber 046 by the second controlling valve 002, and the 3rd reagent locker room 043 and mixing chamber logical 046 are logical
Cross the 3rd controlling valve 003 to connect, the 4th reagent locker room 044 is connected with mixing chamber 046 by the 4th controlling valve 004, institute
The 5th reagent locker room 045 is stated to connect by the 5th controlling valve 005 with mixing chamber 046.
The purification agent generator 04 also includes master controller 047, first controlling valve 001, the second controlling valve 002,
3rd controlling valve 003, the 4th controlling valve 004 and the 5th controlling valve 005 are controlled by the master controller 047.Specifically, it is described
First reagent locker room 041 is stored with diatomite suspension, and the second reagent locker room 042 is stored with metal sulfide, the 3rd examination
Agent locker room 043 is stored with sulphite, and the 4th reagent locker room 044 is stored with carbonate, and the 5th reagent locker room 045 stores
There is aluminium salt.The speed that five kinds of reagents instill mixing chamber is controlled by master controller 047.
Further, some absorption stakes 2 are laid with the adsorption tank 1, the absorption stake 2 is by stake bottom 21 and is laid in institute
State the pile body 22 on a bottom to form, the outer wall of the pile body 22 is by net high-polymer rings of material in generation, the pile body 22
Portion is hollow structure, and its accommodated inside has granular adsorbent, and waste water contacts through the outer wall with the granular adsorbent；
The bottom of adsorption tank 1 is equipped with porous layer 3 and filter layer 4 successively according to order from top to bottom.
Specifically, the porous layer 3 is formed by the laying of cellular high polymer material, the cellular high polymer material gap
Uniformly it is placed with one or more biological adsorption agent particles after modified processing.The porous layer also includes curing agent, institute
Curing agent is stated to be used to connect the cellular high polymer material.
Specifically, the filter layer 4 is equipped with resin coating core, and core aperture is 20um.
Specifically, the adsorption tank 1 is square, triangle or circle.
Specifically, the quantity that stake 2 is adsorbed in the adsorption tank 1 is 10.
Specifically, a diameter of 20mm of the biological adsorption agent particle.
Embodiment 2：
A kind of electroplating waste processing equipment, as shown in figure 1, including：
The clarifier-tank 01 connected including adsorption tank 1 and with the adsorption tank, the side wall of adsorption tank 1 open up a water inlet
10, the water inlet 10 connects with the first control valve 100, and the water inlet 10 flows into for waste water；The bottom of adsorption tank 1 with
The entrance of one funnel type pipeline 5 connects, and the shape of the entrance of funnel type pipeline 5 is consistent with the shape of the bottom of adsorption tank 1, gives up
Water flows out the adsorption tank 1, outlet and the clarifier-tank of the funnel type pipeline 5 via the outlet of the funnel type pipeline 5
01 entrance connects by the second control valve 200, and the level height of the adsorption tank 1 is higher than the clarifier-tank 01；
The clarifier-tank 01 is connected in order to the cleanser by the 3rd control valve 300 with a cleanser generating means 04
Cleanser caused by generating means 04 instills clarifier-tank 01, first control valve 100, the second control valve 200 and the 3rd control
Valve 300 is controlled by an intelligent controller 05；The cleanser generating means 04 tries including the first reagent locker room 041, second
Agent locker room 042, the 3rd reagent locker room 043, the 4th reagent locker room 044, the 5th reagent locker room 045 and mixing chamber
046。
The first reagent locker room 041 is connected with mixing chamber 046 by the first controlling valve 001, and second reagent is deposited
Storage chamber 042 is connected with mixing chamber 046 by the second controlling valve 002, and the 3rd reagent locker room 043 leads to 046 mistake with mixing chamber
3rd controlling valve 003 is connected, and the 4th reagent locker room 044 is connected with mixing chamber 046 by the 4th controlling valve 004, described
5th reagent locker room 045 is connected with mixing chamber 046 by the 5th controlling valve 005.
The purification agent generator 04 also includes master controller 047, first controlling valve 001, the second controlling valve 002,
3rd controlling valve 003, the 4th controlling valve 004 and the 5th controlling valve 005 are controlled by the master controller 047.Specifically, it is described
First reagent locker room 041 is stored with diatomite suspension, and the second reagent locker room 042 is stored with metal sulfide, the 3rd examination
Agent locker room 043 is stored with sulphite, and the 4th reagent locker room 044 is stored with carbonate, and the 5th reagent locker room 045 stores
There is aluminium salt.The speed that five kinds of reagents instill mixing chamber is controlled by master controller 047.
Further, some absorption stakes 2 are laid with the adsorption tank 1, the absorption stake 2 is by stake bottom 21 and is laid in institute
State the pile body 22 on a bottom to form, the outer wall of the pile body 22 is by net high-polymer rings of material in generation, the pile body 22
Portion is hollow structure, and its accommodated inside has granular adsorbent, and waste water contacts through the outer wall with the granular adsorbent；
The bottom of adsorption tank 1 is equipped with porous layer 3 and filter layer 4 successively according to order from top to bottom.
Specifically, the porous layer 3 is formed by the laying of cellular high polymer material, the cellular high polymer material gap
Uniformly it is placed with one or more biological adsorption agent particles after modified processing.The porous layer also includes curing agent, institute
Curing agent is stated to be used to connect the cellular high polymer material.
Specifically, the filter layer 4 is equipped with resin coating core, and core aperture is 40um.
Specifically, the adsorption tank 1 is square, triangle or circle.
Specifically, the quantity that stake 2 is adsorbed in the adsorption tank 1 is 40.
Specifically, a diameter of 30mm of the biological adsorption agent particle.
Above disclosure is only preferred embodiment of present invention, can not limit the right model of the present invention with this certainly
Enclose, therefore the equivalent variations made according to the claims in the present invention, still belong to the scope that the present invention is covered.
Claims (4)
1. a kind of electroplating waste processing equipment, it is characterised in that the clarifier-tank connected including adsorption tank and with the adsorption tank, institute
State adsorption tank side wall and open up a water inlet, the water inlet connects with the first control valve, and the water inlet flows into for waste water, institute
The entrance that adsorption tank bottom is stated with a funnel type pipeline is connected, and the outlet of the funnel type pipeline passes through with the entrance of the clarifier-tank
The connection of the second control valve is crossed, the level height of the adsorption tank is higher than the clarifier-tank；The shape of the funnel type entrance
Consistent with the shape of the adsorption tank bottom, waste water flows out the adsorption tank via the outlet of the funnel type pipeline；
The clarifier-tank is connected by the 3rd control valve with a cleanser generating means in order to which the cleanser generating means produces
Raw cleanser instills clarifier-tank, and first control valve, the second control valve and the 3rd control valve are controlled by an intelligent control
Device；
The cleanser generating means includes the first reagent locker room, the second reagent locker room, the 3rd reagent locker room, the 4th examination
Agent locker room, the 5th reagent locker room and mixing chamber；
The first reagent locker room is connected with mixing chamber by the first controlling valve, and the second reagent locker room leads to mixing chamber
The connection of the second controlling valve is crossed, the 3rd reagent locker room is connected with mixing chamber by the 3rd controlling valve, and the 4th reagent is deposited
Storage chamber is connected with mixing chamber by the 4th controlling valve, and the 5th reagent locker room is connected with mixing chamber by the 5th controlling valve.
A kind of 2. electroplating waste processing equipment according to claim 1, it is characterised in that：
The purification agent generator also includes master controller, first controlling valve, the second controlling valve, the 3rd controlling valve, the 4th
Controlling valve and the 5th controlling valve are controlled by the master controller.
A kind of 3. electroplating waste processing equipment according to claim 1, it is characterised in that：
Some absorption stakes are laid with the adsorption tank, the absorption stake is by stake bottom and the pile body structure being laid on the stake bottom
Into the outer wall of the pile body is by net high-polymer rings of material around generation, and the pile body inside is hollow structure, and its accommodated inside has
Granular adsorbent, waste water contact through the outer wall with the granular adsorbent；
The adsorption tank bottom is equipped with porous layer and filter layer successively according to order from top to bottom.
A kind of 4. electroplating waste processing equipment according to claim 3, it is characterised in that：
The filter layer is equipped with resin coating core, and core aperture is 20-40um.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711041043.4A CN107619129A (en) | 2017-10-30 | 2017-10-30 | A kind of electroplating waste processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711041043.4A CN107619129A (en) | 2017-10-30 | 2017-10-30 | A kind of electroplating waste processing equipment |
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| Publication Number | Publication Date |
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| CN107619129A true CN107619129A (en) | 2018-01-23 |
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| CN201711041043.4A Pending CN107619129A (en) | 2017-10-30 | 2017-10-30 | A kind of electroplating waste processing equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114275946A (en) * | 2022-01-04 | 2022-04-05 | 上海晨鸾环保科技有限公司 | Waste water treatment system for electrolytic oxidation adsorption reduction |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101357798A (en) * | 2007-07-31 | 2009-02-04 | 深圳市邦友通科技有限公司 | Heavy metal wastewater purificant |
| CN103539266A (en) * | 2013-10-31 | 2014-01-29 | 湖南大学 | Structure capable of being used for treating heavy metals in bottom mud dredging tail water and construction method thereof |
| CN104355481A (en) * | 2014-10-20 | 2015-02-18 | 苏州富奇诺水治理设备有限公司 | Device for reclaimed water treatment |
-
2017
- 2017-10-30 CN CN201711041043.4A patent/CN107619129A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101357798A (en) * | 2007-07-31 | 2009-02-04 | 深圳市邦友通科技有限公司 | Heavy metal wastewater purificant |
| CN103539266A (en) * | 2013-10-31 | 2014-01-29 | 湖南大学 | Structure capable of being used for treating heavy metals in bottom mud dredging tail water and construction method thereof |
| CN104355481A (en) * | 2014-10-20 | 2015-02-18 | 苏州富奇诺水治理设备有限公司 | Device for reclaimed water treatment |
Non-Patent Citations (1)
| Title |
|---|
| 苏会东等: "《水污染控制工程》", 31 May 2017, 中国建材工业出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114275946A (en) * | 2022-01-04 | 2022-04-05 | 上海晨鸾环保科技有限公司 | Waste water treatment system for electrolytic oxidation adsorption reduction |
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Application publication date: 20180123 |
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