CN208038189U - Electroplating wastewater integrative automated processing system - Google Patents
Electroplating wastewater integrative automated processing system Download PDFInfo
- Publication number
- CN208038189U CN208038189U CN201820115581.7U CN201820115581U CN208038189U CN 208038189 U CN208038189 U CN 208038189U CN 201820115581 U CN201820115581 U CN 201820115581U CN 208038189 U CN208038189 U CN 208038189U
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- electroplating wastewater
- chamber
- processing system
- automated processing
- adsorption chamber
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- Water Treatment By Sorption (AREA)
Abstract
The utility model provides a kind of electroplating wastewater integrative automated processing system, including controller and the separation chamber, coagulating room, mud chamber, adsorption chamber and the reverse osmosis cell that pass sequentially through pipeline and be connected to, for being pre-processed to electroplating wastewater, coagulating room includes the pH value regulating device for adjusting electroplating wastewater pH value and the chemicals dosing plant for coagulant to be added for separation chamber；Mud chamber bottom is provided with towards external sludge pipe；Adsorption chamber bottom is provided with the filler for physical absorption and ion exchange；It is sequentially communicated on the pipeline of separation chamber, coagulating room, mud chamber and adsorption chamber and is both provided with valve；Controller is electrically connected with pH value regulating device, chemicals dosing plant and valve.By treated electroplating wastewater, it can not only reach domestic water and use standard, be used for resident, can also be re-introduced into plating cutting line, realize the recycling of electroplating wastewater, reduce environmental pollution.
Description
Technical field
The utility model is related to technical field of sewage more particularly to a kind of electroplating wastewater integrative to automatically process and be
System.
Background technology
For meet the requirement of environmental protection, electroplating wastewater is handled.Electroplating wastewater mainly have water, suspended particulate substance, can
Particulate matter, heavy metal ion, ammonia nitrogen (NH3-N) and organic matter (COD) of precipitation etc..
The processing method of existing electroplating wastewater is：Removal of heavy metal ions directly is passed through to the electroplating wastewater of factory's discharge
Then device heavy-metal ion removal is discharged to the place that sewage treatment plant carries out ammonia nitrogen (NH3-N) and organic matter by sewage network
Reason.
Existing electroplating effluent treatment method has the following disadvantages：Equipment is easy tod produce when removal of heavy metal ions blocks damage
Bad phenomenon (when carrying out heavy metal processing especially by filter membrane), spoil disposal are difficult, processing is not thorough, no to organic matter
To fully and rationally using；It is required that the conditions such as the designed capacity of sewage treatment plant, operating mode meet the standard of receiving sewage, and it is electroplated dirty
Water is that randomness is discharged into sewage network, and very big inconvenience is brought to the construction plan of sewage treatment plant；Heavy-metal ion removal
Electroplating sewerage, which is transported in the way of sewage treatment plant, can give out dense stink, grow mosquitos and flies, be difficult to handle stink,
It is unfavorable for environmental sanitation.
Utility model content
The utility model provides a kind of electroplating wastewater integrative automated processing system, to solve electroplating wastewater direct emission
The technical issues of causing environmental pollution, being unfavorable for environmental sanitation.
The utility model provides a kind of electroplating wastewater integrative automated processing system, including：Controller and pass sequentially through pipe
Separation chamber, coagulating room, mud chamber, adsorption chamber and the reverse osmosis cell of road connection, wherein the separation chamber is used for useless to being electroplated
Water is pre-processed, and the coagulating room includes pH value regulating device for adjusting electroplating wastewater pH value and mixed for being added
The chemicals dosing plant of solidifying agent；The mud chamber bottom is provided with towards external sludge pipe；The adsorption chamber bottom, which is provided with, to be used for
The filler of physical absorption and ion exchange；The reverse osmosis cell includes polylith partition board, and the partition board separates the reverse osmosis cell
At multiple compartments, the liquid flowed out from the adsorption chamber is filtered by multiple partition boards successively, and the partition board includes reverse osmosis
Film；
It is sequentially communicated on the pipeline of the separation chamber, the coagulating room, the mud chamber and the adsorption chamber and is all provided with
It is equipped with valve；
The controller is electrically connected with the pH value regulating device, the chemicals dosing plant and the valve.
Further, the separation chamber includes solid-liquid separating machine.
Further, the adsorption chamber further includes the water quality detecting device for being detected to water body, the water quality inspection
It includes water quality collector, processor and display screen to survey device, and the water quality collector is used for the liquid in the adsorption chamber
The ingredient and content of body are acquired, and the collection result of acquisition is sent to the processor, and the processor is adopted to described
After collection result is calculated and judged, the testing result of acquisition is sent to the display screen and is shown.
Further, above-mentioned apparatus further includes storage basin, and the mud chamber is connected by the sludge pipe with the storage basin
It is logical.
Further, it is provided with valve on the sludge pipe.
Further, the filler includes activated carbon, hydroxyapatite and tired two or three dragged in stone.
Electroplating wastewater integrative automated processing system provided by the invention passes sequentially through separation chamber, coagulating room, precipitation
Room, adsorption chamber and reverse osmosis cell processing, to be separated by solid-liquid separation respectively to electroplating wastewater, flocculation treatment, physical absorption and purification
Processing can not only reach domestic water and use standard, be used for resident by treated electroplating wastewater, can also be again
It is secondary to enter in plating cutting line, it realizes the recycling of electroplating wastewater, reduces environmental pollution.
Description of the drawings
Hereinafter the utility model will be described in more detail based on the embodiments and with reference to the accompanying drawings.Wherein：
Fig. 1 is the structural schematic diagram for the electroplating wastewater integrative automated processing system that the utility model embodiment provides.
In the accompanying drawings, identical component uses identical reference numeral.Attached drawing is not drawn according to actual ratio.
Specific implementation mode
Below in conjunction with attached drawing, the utility model is described in further detail.
Fig. 1 is the structural schematic diagram for the electroplating wastewater integrative automated processing system that the utility model embodiment provides.Such as
Shown in Fig. 1, the present embodiment provides a kind of electroplating wastewater integrative automated processing systems, including：Controller (not shown) and
Pass sequentially through separation chamber 1, coagulating room 2, mud chamber 3, adsorption chamber 4 and the reverse osmosis cell 5 of the connection of pipeline 6, wherein described point
From room 1 for being pre-processed to electroplating wastewater, the coagulating room 2 includes the pH value for adjusting electroplating wastewater pH values
Regulating device (not shown) and chemicals dosing plant for coagulant to be added；3 bottom of the mud chamber is provided with towards outside
Sludge pipe (not shown)；4 bottom of the adsorption chamber is provided with the filler for physical absorption and ion exchange；It is described anti-
It includes polylith partition board (not shown) to permeate room 5, and the reverse osmosis cell 5 is separated into multiple compartments by the partition board, from described
The liquid that adsorption chamber 4 flows out is filtered by multiple partition boards successively, and the partition board includes reverse osmosis membrane；
It is sequentially communicated the pipeline 6 of the separation chamber 1, the coagulating room 2, the mud chamber 3 and the adsorption chamber 4
On be both provided with valve；The controller is electrically connected with the pH value regulating device, the chemicals dosing plant and the valve.
Specifically, separation chamber 1 for carrying out preliminary separation of solid and liquid to electroplating wastewater, such as utilizes solid-liquid separating machine to plating
Waste water is separated by solid-liquid separation, and the liquid after separation enters in coagulating room 2.Coagulating room 2 includes coagulating room 2
Chemicals dosing plant including blender and for coagulant to be added adds coagulant into coagulating room 2 from chemicals dosing plant, can make
Dirt in pending electroplating wastewater in coagulating room 2 be rapidly condensed into it is cotton-shaped, convenient for further separation, meanwhile,
Coagulating room 2 further includes blender, under the stirring action of blender so that and coagulant is quickly mixed with electroplating wastewater, and
And can realize the stirring of more times of cycling rates, suspended solid in water is sheared, the big floccule body for being easy to sedimentation is re-formed.
Electroplating wastewater after flocculation treatment enters mud chamber 3 and is precipitated, for example, time of repose is 1h~2h, this
Sample can be such that the heavy metal after flocculation treatment deposits completely, reach solid-liquid and be kept completely separate, then by the electroplating wastewater after precipitation
Supernatant liquor is input in adsorption chamber 4 and is handled, and lower layer's solid impurity in mud chamber 3 is discharged by sludge pipe.
4 bottom of adsorption chamber is provided with the filler for physical absorption and ion exchange, and the filler includes activated carbon, hydroxyl phosphorus
Lime stone and tired two or three dragged in stone.Further, filler surface culture has microorganism, organic matter in supernatant liquor and
Heavy metal ion by after filling adsorption, organic matter by the microbial degradation on filler surface to destroy adsorption equilibrium make absorption after
Continuous to carry out, heavy metal enters the inside of filler in a manner of diffusion after being adsorbed, and carries out ion exchange with filler, to destroy
Adsorption equilibrium makes physical absorption continue.
Further, enter in reverse osmosis cell Room 5 from the electroplating wastewater exported in adsorption chamber 4, reverse osmosis cell 5 includes polylith
The reverse osmosis cell 5 is separated into multiple compartments by partition board, the partition board, and the liquid flowed out from the adsorption chamber 4 passes through excessive successively
A partition board is filtered, and partition board includes reverse osmosis membrane, and the electroplating wastewater after multilayer reverse osmosis membrane processing, can reach life makes
Use water supply standard.
Electroplating wastewater integrative automated processing system provided in this embodiment, pass sequentially through separation chamber 1, coagulating room 2,
Mud chamber 3, adsorption chamber 4 and reverse osmosis cell 5 are handled, to be separated by solid-liquid separation respectively to electroplating wastewater, flocculation treatment, physical absorption
And purified treatment can not only reach domestic water and use standard, be used for resident by treated electroplating wastewater,
It can also be re-introduced into plating cutting line, realize the recycling of electroplating wastewater, reduce environmental pollution.
Further, chemicals dosing plant includes Scatula 21 and pipeline 23, the first end of the pipeline 23 and the Scatula
21 are connected, and the second end of the pipeline 23 stretches in the coagulating room 2, is additionally provided with and is used on the pipeline 23
Control the valve 22 of 23 break-make of the pipeline.
Further, the adsorption chamber 4 further includes the water quality detecting device for being detected to water body, the water quality inspection
It includes water quality collector, processor and display screen to survey device, and the water quality collector is used for the liquid in the adsorption chamber 4
The ingredient and content of body are acquired, and the collection result of acquisition is sent to the processor, and the processor is adopted to described
After collection result is calculated and judged, the testing result of acquisition is sent to the display screen and is shown.
Further, above system further includes storage basin, and the mud chamber 3 is connected by the sludge pipe with the storage basin
It is logical, it is provided with valve on the sludge pipe.
Further, the filler includes activated carbon, hydroxyapatite and tired two or three dragged in stone.
Although the present utility model has been described by reference to the preferred embodiments, but in the model for not departing from the utility model
In the case of enclosing, various improvement can be carried out to it and can replace component therein with equivalent.Especially, as long as not depositing
In structural conflict, items technical characteristic mentioned in the various embodiments can be combined in any way.The utility model
It is not limited to specific embodiment disclosed herein, but includes all technical solutions fallen within the scope of the appended claims.
Claims (5)
1. a kind of electroplating wastewater integrative automated processing system, which is characterized in that including：Controller is connected to pipeline is passed sequentially through
Separation chamber, coagulating room, mud chamber, adsorption chamber and reverse osmosis cell, wherein the separation chamber be used for electroplating wastewater carry out
Pretreatment, the coagulating room include pH value regulating device for adjusting electroplating wastewater pH value and for coagulant to be added
Chemicals dosing plant；The mud chamber bottom is provided with towards external sludge pipe；The adsorption chamber bottom is provided with inhales for physics
Attached and ion exchange filler；The reverse osmosis cell includes polylith partition board, and the reverse osmosis cell is separated into multiple by the partition board
Compartment, the liquid flowed out from the adsorption chamber are filtered by multiple partition boards successively, and the partition board includes reverse osmosis membrane；
It is sequentially communicated on the pipeline of the separation chamber, the coagulating room, the mud chamber and the adsorption chamber and is both provided with
Valve；
The controller is electrically connected with the pH value regulating device, the chemicals dosing plant and the valve.
2. electroplating wastewater integrative automated processing system according to claim 1, which is characterized in that the separation chamber includes
Solid-liquid separating machine.
3. electroplating wastewater integrative automated processing system according to claim 1, which is characterized in that the adsorption chamber also wraps
The water quality detecting device for being detected to water body is included, the water quality detecting device includes water quality collector, processor and shows
Display screen, the water quality collector is for being acquired the ingredient and content of the liquid in the adsorption chamber, and adopting acquisition
Collection result is sent to the processor, after the processor is calculated and judged to the collection result, by the detection of acquisition
As a result the display screen is sent to be shown.
4. electroplating wastewater integrative automated processing system according to claim 1, which is characterized in that further include storage basin,
The mud chamber is connected by the sludge pipe with the storage basin.
5. electroplating wastewater integrative automated processing system according to claim 4, which is characterized in that set on the sludge pipe
It is equipped with valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820115581.7U CN208038189U (en) | 2018-01-24 | 2018-01-24 | Electroplating wastewater integrative automated processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820115581.7U CN208038189U (en) | 2018-01-24 | 2018-01-24 | Electroplating wastewater integrative automated processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208038189U true CN208038189U (en) | 2018-11-02 |
Family
ID=63953972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820115581.7U Expired - Fee Related CN208038189U (en) | 2018-01-24 | 2018-01-24 | Electroplating wastewater integrative automated processing system |
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| Country | Link |
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| CN (1) | CN208038189U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110540334A (en) * | 2019-10-08 | 2019-12-06 | 常德威尔博金属表面处理有限责任公司 | Electroplating sewage treatment equipment and process thereof |
-
2018
- 2018-01-24 CN CN201820115581.7U patent/CN208038189U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110540334A (en) * | 2019-10-08 | 2019-12-06 | 常德威尔博金属表面处理有限责任公司 | Electroplating sewage treatment equipment and process thereof |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181102 Termination date: 20220124 |
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| CF01 | Termination of patent right due to non-payment of annual fee |