CN209652050U - A kind of COD absorption resin desorption wastewater treatment and reuse system - Google Patents
A kind of COD absorption resin desorption wastewater treatment and reuse system Download PDFInfo
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- CN209652050U CN209652050U CN201920103954.3U CN201920103954U CN209652050U CN 209652050 U CN209652050 U CN 209652050U CN 201920103954 U CN201920103954 U CN 201920103954U CN 209652050 U CN209652050 U CN 209652050U
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- iron
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- flocculation sedimentation
- carbon micro
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Abstract
The utility model discloses a kind of COD to adsorb resin desorption wastewater treatment and reuse system, including flocculation sedimentation processing module, iron-carbon micro-electrolysis processing module, Fenton processing module and nanofiltration processing module, by including that flocculation sedimentation tank, water pump and associated pipe are constituted, the iron-carbon micro-electrolysis processing module is made of the flocculation sedimentation processing module iron-carbon micro-electrolysis oxidator.The utility model has the advantages that when being run by processing system, coking wastewater resin desorption waste water enters the flocculation sedimentation tank in flocculation sedimentation processing module after pre-treatment, then enter iron-carbon micro-electrolysis processing module by water pump lifting, Fenton oxidation reactor after being handled by iron-carbon micro-electrolysis oxidator through water pump lifting into Fenton processing module, pass through oxidation processes, Fenton produces water and enters flocculation sedimentation tank, water, which is produced, by nanofiltration processing module nanofiltration membrane is back to resin backwash process, the rate of recovery of this nanofiltration membrane can achieve 85% -95%, 90% or more organic matter removal efficiency.
Description
Technical field
The utility model relates to resin desorption field of waste water treatment, it particularly relates to which a kind of COD absorption resin desorption is useless
Water process and reclaiming system.
Background technique
Coking wastewater resin desorption waste water salt content is high, and organic pollutant content is high, type is complicated and difficult to degrade, at waste water
It is high to manage difficulty.Currently it is mainly used for standby coal.Since water yield is larger, standby coal can not be completely used for；Salt content is high, and standby coal is for solid
Useless generation greatly increases.This had not only caused the waste of water resource, but also increased the cost of wastewater treatment and fixed-end forces, therefore just
A kind of COD is needed to adsorb resin desorption wastewater treatment and reuse system to solve the problems, such as this.
For the problems in the relevant technologies, currently no effective solution has been proposed.
Utility model content
The purpose of this utility model is to provide a kind of COD to adsorb resin desorption wastewater treatment and reuse system, to solve
The problems mentioned above in the background art.
The technical solution of the utility model is achieved in that
A kind of COD absorption resin desorption wastewater treatment and reuse system, including flocculation sedimentation processing module, iron-carbon micro-electrolysis
Processing module, Fenton processing module and nanofiltration processing module, the flocculation sedimentation processing module is by including flocculation sedimentation tank, water pump
It is constituted with associated pipe, the iron-carbon micro-electrolysis processing module is made of iron-carbon micro-electrolysis oxidator, the iron-carbon micro-electrolysis oxygen
Change and be connected with air blower on device, the Fenton processing module is made of Fenton oxidation reactor, and the nanofiltration processing module includes
Nano filter membrance device, the first chemicals dosing plant and chemically-cleaning device.
Further, equipped with chemicals dosing plant and agitating device in the flocculation sedimentation tank.
Further, it is filled with filler inside the iron-carbon micro-electrolysis oxidator, iron carbon mass ratio is 1 in the filler:
1-1:5。
Further, the Fenton oxidation reactor includes the second chemicals dosing plant, agitating device and mating pump tube.
Further, the nano filter membrance device includes cartridge filter, low-lift pump, membrane module and auxiliary device, the film
Component is antipollution nanofiltration membrane.
Further, first chemicals dosing plant includes the first liquor box, the first blender, first liquid level gauge, metering pump
With the first attachment.
Further, the chemically-cleaning device include the second liquor box, the second blender, second liquid level gauge, heater,
Circulating pump and the second attachment.
The utility model provides a kind of COD absorption resin desorption wastewater treatment and reuse system, has the beneficial effect that:
(1), when the utility model is run by processing system, coking wastewater resin desorption waste water enters after pre-treatment
Then flocculation sedimentation tank in flocculation sedimentation processing module enters iron-carbon micro-electrolysis processing module by water pump lifting, passes through iron
Fenton oxidation reactor through water pump lifting into Fenton processing module after the processing of carbon micro-electrolysis oxidator, by oxidation processes,
Fenton produces water and enters flocculation sedimentation tank, produces water by nanofiltration processing module nanofiltration membrane and is back to resin backwash process, this nanofiltration membrane
The rate of recovery can achieve 85% -95%, 90% or more organic matter removal efficiency.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only the utility model
Some embodiments for those of ordinary skill in the art without creative efforts, can also be according to this
A little attached drawings obtain other attached drawings.
Fig. 1 is to be according to what a kind of COD of the utility model embodiment adsorbed resin desorption wastewater treatment and reuse system
System figure；
Fig. 2 is to be adsorbed in resin desorption wastewater treatment and reuse system to wad a quilt with cotton according to a kind of COD of the utility model embodiment
The system diagram of retrogradation shallow lake processing module；
Fig. 3 is to adsorb iron in resin desorption wastewater treatment and reuse system according to a kind of COD of the utility model embodiment
The system diagram of carbon micro-electrolysis processing module；
Fig. 4 is that sweet smell in resin desorption wastewater treatment and reuse system is adsorbed according to a kind of COD of the utility model embodiment
The system diagram for processing module of pausing；
Fig. 5 is to be adsorbed in resin desorption wastewater treatment and reuse system to receive according to a kind of COD of the utility model embodiment
Filter the system diagram of processing module.
In figure:
1, flocculation sedimentation processing module；2, iron-carbon micro-electrolysis processing module；3, Fenton processing module；4, nanofiltration handles mould
Block；5, flocculation sedimentation tank；6, water pump；7, pipeline；8, iron-carbon micro-electrolysis oxidator；9, air blower；10, Fenton oxidation reactor；
11, nano filter membrance device；12, the first chemicals dosing plant；13, chemically-cleaning device；14, chemicals dosing plant；15, agitating device；16, it fills out
Material；17, the second chemicals dosing plant；18, agitating device；19, mating pump tube；20, cartridge filter；21, low-lift pump；22, film
Component；23, auxiliary device；24, the first liquor box；25, the first blender；26, first liquid level gauge；27, metering pump；28, first
Attachment；29, the second liquor box；30, the second blender；31, second liquid level gauge；32, heater；33, circulating pump；34, second is attached
Part.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art's every other embodiment obtained, all belongs to
In the range of the utility model protection.
In the following, making further description to the utility model in conjunction with attached drawing and specific embodiment:
Fig. 1-5 is please referred to, resin desorption wastewater treatment and reuse system is adsorbed according to a kind of COD of the utility model embodiment
System, including flocculation sedimentation processing module 1, iron-carbon micro-electrolysis processing module 2, Fenton processing module 3 and nanofiltration processing module 4, institute
It states flocculation sedimentation processing module 1 to be constituted by including flocculation sedimentation tank 5, water pump 6 with associated pipe 7, the iron-carbon micro-electrolysis processing
Module 2 is made of iron-carbon micro-electrolysis oxidator 8, is connected with air blower 9 on the iron-carbon micro-electrolysis oxidator 8, at the Fenton
Reason module 3 is made of Fenton oxidation reactor 10, and the nanofiltration processing module 4 includes nano filter membrance device 11, the first chemicals dosing plant
12 with chemically-cleaning device 13.
By the above scheme of the utility model, when being run by processing system, coking wastewater resin desorption waste water passes through
Enter the flocculation sedimentation tank 5 in flocculation sedimentation processing module 1 after pre-treatment, is then lifted into iron-carbon micro-electrolysis by water pump 6
Processing module 2, the Fenton oxidation being promoted in Fenton processing module 3 after being handled by iron-carbon micro-electrolysis oxidator 8 through water pump 6 are anti-
Device 10 is answered, by oxidation processes, Fenton produces water and enters flocculation sedimentation tank 5, produces water by 4 nanofiltration membrane of nanofiltration processing module and is back to
Resin backwash process, the rate of recovery of this nanofiltration membrane can achieve 85% -95%, 90% or more organic matter removal efficiency.
In a particular application, for flocculation sedimentation tank 5, in the flocculation sedimentation tank 5 equipped with chemicals dosing plant 14 with
Agitating device 15.
In a particular application, it for iron-carbon micro-electrolysis oxidator 8, is loaded inside the iron-carbon micro-electrolysis oxidator 8
There is filler 16, iron carbon mass ratio is 1:1-1:5 in the filler 16.
In a particular application, for Fenton oxidation reactor 10, the Fenton oxidation reactor 10 adds including second
Medicine device 17, agitating device 18 and mating pump tube 19.
In a particular application, for nano filter membrance device 11, the nano filter membrance device 11 includes cartridge filter 20, low
Press pump 21, membrane module 22 and auxiliary device 23, the membrane module 22 are antipollution nanofiltration membrane.
In a particular application, for the first chemicals dosing plant 12, first chemicals dosing plant 12 includes the first liquor box
24, the first blender 25, first liquid level gauge 26, metering pump 27 and the first attachment 28.
In a particular application, for chemically-cleaning device 13, the chemically-cleaning device 13 includes the second liquor box
29, the second blender 30, second liquid level gauge 31, heater 32, circulating pump 33 and the second attachment 34.
In conclusion by means of the above-mentioned technical proposal of the utility model, when being run by processing system, coking wastewater tree
The flocculation sedimentation tank 5 that waste water enters after pre-treatment in flocculation sedimentation processing module 1 is desorbed in rouge, is then promoted by water pump 6
Into iron-carbon micro-electrolysis processing module 2, Fenton processing module 3 is promoted to through water pump 6 after handling by iron-carbon micro-electrolysis oxidator 8
In Fenton oxidation reactor 10, by oxidation processes, Fenton produce water enter flocculation sedimentation tank 5, received by nanofiltration processing module 4
Filter membrane produces water and is back to resin backwash process, and the rate of recovery of this nanofiltration membrane can achieve 85% -95%, organic matter removal efficiency
90% or more；Tthe utility model system is not only reasonable in design, easy to operate, and monitors comprehensively, collects convenient for information, can
Popularity uses.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection scope within.
Claims (7)
1. a kind of COD adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that including flocculation sedimentation processing module
(1), iron-carbon micro-electrolysis processing module (2), Fenton processing module (3) and nanofiltration processing module (4), the flocculation sedimentation handle mould
Block (1) by including that flocculation sedimentation tank (5), water pump (6) are constituted with associated pipe (7), the iron-carbon micro-electrolysis processing module (2) by
Iron-carbon micro-electrolysis oxidator (8) is constituted, and is connected with air blower (9) on the iron-carbon micro-electrolysis oxidator (8), the Fenton processing
Module (3) is made of Fenton oxidation reactor (10), the nanofiltration processing module (4) include nano filter membrance device (11), first plus
Medicine device (12) and chemically-cleaning device (13).
2. a kind of COD according to claim 1 adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that institute
It states in flocculation sedimentation tank (5) equipped with chemicals dosing plant (14) and agitating device (15).
3. a kind of COD according to claim 2 adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that institute
It states and is filled with filler (16) inside iron-carbon micro-electrolysis oxidator (8), iron carbon mass ratio is 1:1-1:5 in the filler (16).
4. a kind of COD according to claim 3 adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that institute
Stating Fenton oxidation reactor (10) includes the second chemicals dosing plant (17), agitating device (18) and mating pump tube (19).
5. a kind of COD according to claim 4 adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that institute
Stating nano filter membrance device (11) includes cartridge filter (20), low-lift pump (21), membrane module (22) and auxiliary device (23), the film
Component (22) is antipollution nanofiltration membrane.
6. a kind of COD according to claim 5 adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that institute
Stating the first chemicals dosing plant (12) includes the first liquor box (24), the first blender (25), first liquid level gauge (26), metering pump (27)
With the first attachment (28).
7. a kind of COD according to claim 6 adsorbs resin desorption wastewater treatment and reuse system, which is characterized in that institute
Stating chemically-cleaning device (13) includes the second liquor box (29), the second blender (30), second liquid level gauge (31), heater
(32), circulating pump (33) and the second attachment (34).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920103954.3U CN209652050U (en) | 2019-01-22 | 2019-01-22 | A kind of COD absorption resin desorption wastewater treatment and reuse system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920103954.3U CN209652050U (en) | 2019-01-22 | 2019-01-22 | A kind of COD absorption resin desorption wastewater treatment and reuse system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209652050U true CN209652050U (en) | 2019-11-19 |
Family
ID=68522038
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920103954.3U Active CN209652050U (en) | 2019-01-22 | 2019-01-22 | A kind of COD absorption resin desorption wastewater treatment and reuse system |
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| CN (1) | CN209652050U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110862179A (en) * | 2019-12-19 | 2020-03-06 | 锦科绿色科技(苏州)有限公司 | Water treatment system and control workstation |
| CN110921954A (en) * | 2019-12-10 | 2020-03-27 | 西安华盛坤泰能源环保科技有限公司 | Method and system for treating oilfield wastewater by combining iron-carbon micro-electrolysis and Fenton oxidation |
-
2019
- 2019-01-22 CN CN201920103954.3U patent/CN209652050U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110921954A (en) * | 2019-12-10 | 2020-03-27 | 西安华盛坤泰能源环保科技有限公司 | Method and system for treating oilfield wastewater by combining iron-carbon micro-electrolysis and Fenton oxidation |
| CN110862179A (en) * | 2019-12-19 | 2020-03-06 | 锦科绿色科技(苏州)有限公司 | Water treatment system and control workstation |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 251604 Liyuan street, economic development zone, Shanghe County, Jinan City, Shandong Province Patentee after: Shandong shuifayou Membrane Technology Co.,Ltd. Address before: 251604 Liyuan street, economic development zone, Shanghe County, Jinan City, Shandong Province Patentee before: Shandong you Film Technology Co.,Ltd. |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A COD adsorption resin desorption wastewater treatment and reuse system Effective date of registration: 20221018 Granted publication date: 20191119 Pledgee: Shandong Shanghe Rural Commercial Bank Co.,Ltd. Yuhuangmiao Sub branch Pledgor: Shandong shuifayou Membrane Technology Co.,Ltd. Registration number: Y2022980018831 |