CN206538318U - A kind of device for handling the high organic wastewater of industrial high salt - Google Patents
A kind of device for handling the high organic wastewater of industrial high salt Download PDFInfo
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- CN206538318U CN206538318U CN201720262773.6U CN201720262773U CN206538318U CN 206538318 U CN206538318 U CN 206538318U CN 201720262773 U CN201720262773 U CN 201720262773U CN 206538318 U CN206538318 U CN 206538318U
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Abstract
The utility model provides a kind of device for handling the high organic wastewater of industrial high salt, including piece-rate system and biochemical system；Piece-rate system includes regulating reservoir, quartz filter, adsorptive reactor, intermediate pool, micro-electrolysis reactor and pH regulating reservoirs, is sequentially connected, realizes the separation of salt and organic matter in the high organic wastewater of high salt；Biochemical system includes desorbed solution reserve pool, anaerobism VTBR reactors, the first sedimentation basin, aerobic VTBR reactors, the second sedimentation basin, catalytic ozonation reactor and parsing regenerated liquid collecting pit, realizes the biochemical treatment of organic matter；Device of the present utility model, to NaCl, NH4The content of the chlorates such as Cl, KCl is at least 3.5% and the waste water of high organic matter is handled, and production and environmental requirement is met, with easy to operate, with low cost advantage.
Description
Technical field
The utility model belongs to a kind of wastewater treatment equipment, and in particular to a kind of device of the industrial high-salt wastewater of processing.
Background technology
With deepening continuously for process of industrialization, the seriously polluted normal life that have impact on the people that industrial wastewater is caused with
And the sustainable development of environment.The freshwater resources of particularly China are relatively deficient, how high-salt wastewater handled, realize water
Recycling for resource, is a urgent problem to be solved.High-salt wastewater refers mainly to total dissolved solidss TDS (Total
Dissolved Solid) content be at least 3.5%, its be mainly derived from directly using seawater industrial production, print and dye, make
The industries such as paper, chemical industry and agricultural chemicals.The waste water of these high salts, high organic matter, will certainly be to water body if unprocessed directly discharge
Biological, Drinking Water and industrial and agricultural production produce great harm with water.Conventional bioanalysis is handled, the salt of high concentration
With the organic matter of degradation resistant can all inhibitory action be produced to microorganism.
The processing of the high organic wastewater of high salt can also be handled using distillation, such as mechanical steam recompression technology,
Multiple-effect evaporation, membrane distillation etc., but this method investment and operating cost are higher, there is certain difficulty in popularization.
Consider investment and operating cost, the combination of the processing use resource reclaim preferably of the high organic wastewater of high salt
Technique, using the separation of salt and organic matter as pretreatment, with reference to biochemical, light electrolysis and the group technology of catalytic ozonation, profit
With combined treatment process, organic wastewater high to high salt carries out effective processing, is finally reached《Integrated wastewater discharge standard》
(GB8978-1996) first discharge standard.
Utility model content
In order to solve above-mentioned technical problem, the utility model, which provides one kind, to be entered to high salt, high organic wastewater
The device that row is effectively handled, to reach that the waste water after processing reaches《Integrated wastewater discharge standard》(GB8978-1996) one-level
Discharge standard.
The high organic wastewater of high salt refers to NaCl, NH in the utility model4The content of the chlorates such as Cl, KCl is at least
3.5% and content of organics (COD) >=10000mg/L pollutant effluents.
The technical solution of the utility model：
A kind of device for handling the high organic wastewater of industrial high salt, described device includes piece-rate system and biochemical system；
Described piece-rate system includes regulating reservoir 1, quartz filter 2, adsorptive reactor 3, intermediate pool 4, light electrolysis
Reactor 5 and pH regulating reservoirs 6；Regulating reservoir 1 is connected by the first elevator pump A1 with the water inlet of the upper end of quartz filter 2, stone
The delivery port of the lower end of sand filter 2 is connected by the second elevator pump A2 with the water inlet of the upper end of adsorptive reactor 3, adsorption reaction
The delivery port of the lower end of device 3 is passed through intermediate pool 4, and desorbed solution entrance and organic outlet are arranged at the bottom of adsorptive reactor 3；Intermediate pool
4 delivery port is connected by the 3rd elevator pump A3 with the water inlet of micro-electrolysis reactor 5, and the delivery port of micro-electrolysis reactor 5 leads to
Enter pH regulating reservoirs 6；The industrial high organic wastewater of high salt enters the filtering of quartz filter 2 after the regulation of regulating reservoir 1 and removed greatly
Particulate matter, water outlet is adsorbed on the sorbent by adsorptive reactor 3, organic matter, realizes that salt is separated with the one-level of organic matter；One
Water outlet after level separation enters in micro-electrolysis reactor 5, and wherein organic matter is further degraded, and realizes two stage treatment；High salt is given up
Water is discharged into aftertreatment systems after being adjusted in pH regulating reservoirs 6；
Described biochemical system includes desorbed solution reserve pool 2-0, anaerobism VTBR reactors 2-1, the first sedimentation basin 2-2, good
Oxygen VTBR reactors 2-3, the second sedimentation basin 2-4, catalytic ozonation reactor 2-5 and parsing regenerated liquid collecting pit 2-6；Parsing
Liquid reserve pool 2-0 entrances are connected with the organic outlet of the bottom of adsorptive reactor 3, and desorbed solution reserve pool 2-0 outlets are carried through the 4th
The entrance that pump A4 is connected to anaerobism VTBR reactor 2-1 lower ends is risen, the outlet connection first of anaerobism VTBR reactor 2-1 upper ends is sunk
The entrance of shallow lake pond 2-2, sedimentation basin 2-2 through the 5th aerobic VTBR reactors 2-3 lower ends of elevator pump A5 connections, aerobic VTBR reactors
It is anti-through the 5th elevator pump A5 connection catalytic ozonations that the outlet of 2-3 upper ends connects the second sedimentation basin 2-4, the second sedimentation basin 2-4
The entrance of device 2-5 lower ends is answered, the outlet connection parsing regenerated liquid collecting pit 2-6's of catalytic ozonation reactor 2-5 upper ends enters
Mouthful, parsing regenerated liquid collecting pit 2-6 outlet is connected with the desorbed solution entrance of the bottom of adsorptive reactor 3, is solved in adsorptive reactor 3
The waste water containing organic matter after analysis sequentially passes through anaerobism VTBR reactors 2-1 by the organic outlet of the bottom of adsorptive reactor 3, good
Oxygen VTBR reactors 2-3 and catalytic ozonation reactor 2-5, carries out tertiary treatment.
The beneficial effects of the utility model：A kind of device for handling the high organic wastewater of industrial high salt of the present utility model,
Can be to NaCl, NH4The content of the chlorates such as Cl, KCl is at least 3.5% and the waste water of high organic matter is handled, and meets life
Each device employed in production and environmental requirement, the utility model is ripe reaction unit, can not be expired when being used alone
The processing requirement of sufficient waste water, only can be only achieved processing standard, with operation side after combination and according to particular order practicality
Just, advantage with low cost.
Brief description of the drawings
Fig. 1 is the structural representation of the high organic waste-water treating apparatus of the utility model high salt.
In figure：1 regulating reservoir；2 quartz filters；3 adsorptive reactors；4 intermediate pools；
5 micro-electrolysis reactors；6pH regulating reservoirs；2-0 desorbed solution reserve pools；2-1 anaerobism VTBR reactors；
The sedimentation basins of 2-2 first；The aerobic VTBR reactors of 2-3；The sedimentation basins of 2-4 second；
2-5 catalytic ozonation reactors；2-6 parses regenerated liquid collecting pit；A elevator pumps.
Embodiment
Below in conjunction with accompanying drawing and technical scheme, embodiment of the present utility model is further illustrated.
Embodiment
A kind of device for handling the high organic wastewater of industrial high salt, described device includes piece-rate system and biochemical system；
Described piece-rate system includes regulating reservoir 1, quartz filter 2, adsorptive reactor 3, intermediate pool 4, light electrolysis
Reactor 5 and pH regulating reservoirs 6；Regulating reservoir 1 is connected by the first elevator pump A1 with the water inlet of the upper end of quartz filter 2, stone
The delivery port of the lower end of sand filter 2 is connected by the second elevator pump A2 with the water inlet of the upper end of adsorptive reactor 3, adsorption reaction
The delivery port of the lower end of device 3 is passed through intermediate pool 4, and desorbed solution entrance and organic outlet are arranged at the bottom of adsorptive reactor 3；Intermediate pool
4 delivery port is connected by the 3rd elevator pump A3 with the water inlet of micro-electrolysis reactor 5, and the delivery port of micro-electrolysis reactor 5 leads to
Enter pH regulating reservoirs 6；The industrial high organic wastewater of high salt enters the filtering of quartz filter 2 after the regulation of regulating reservoir 1 and removed greatly
Particulate matter, water outlet is adsorbed on the sorbent by adsorptive reactor 3, organic matter, realizes that salt is separated with the one-level of organic matter；One
Water outlet after level separation enters in micro-electrolysis reactor 5, and wherein organic matter is further degraded, and realizes two stage treatment；High salt is given up
Water is discharged into aftertreatment systems after being adjusted in pH regulating reservoirs 6；
Described biochemical system includes desorbed solution reserve pool 2-0, anaerobism VTBR reactors 2-1, the first sedimentation basin 2-2, good
Oxygen VTBR reactors 2-3, the second sedimentation basin 2-4, catalytic ozonation reactor 2-5 and parsing regenerated liquid collecting pit 2-6；Parsing
Liquid reserve pool 2-0 entrances are connected with the organic outlet of the bottom of adsorptive reactor 3, and desorbed solution reserve pool 2-0 outlets are carried through the 4th
The entrance that pump A4 is connected to anaerobism VTBR reactor 2-1 lower ends is risen, the outlet connection first of anaerobism VTBR reactor 2-1 upper ends is sunk
The entrance of shallow lake pond 2-2, sedimentation basin 2-2 through the 5th aerobic VTBR reactors 2-3 lower ends of elevator pump A5 connections, aerobic VTBR reactors
It is anti-through the 5th elevator pump A5 connection catalytic ozonations that the outlet of 2-3 upper ends connects the second sedimentation basin 2-4, the second sedimentation basin 2-4
The entrance of device 2-5 lower ends is answered, the outlet connection parsing regenerated liquid collecting pit 2-6's of catalytic ozonation reactor 2-5 upper ends enters
Mouthful, parsing regenerated liquid collecting pit 2-6 outlet is connected with the desorbed solution entrance of the bottom of adsorptive reactor 3, is solved in adsorptive reactor 3
The waste water containing organic matter after analysis sequentially passes through anaerobism VTBR reactors 2-1 by the organic outlet of the bottom of adsorptive reactor 3, good
Oxygen VTBR reactors 2-3 and catalytic ozonation reactor 2-5, carries out tertiary treatment.
Claims (1)
1. a kind of device for handling the industrial high organic wastewater of high salt, it is characterised in that described device include piece-rate system and
Biochemical system；
Described piece-rate system includes regulating reservoir (1), quartz filter (2), adsorptive reactor (3), intermediate pool (4), micro-
Electrolysis reactor (5) and pH regulating reservoirs (6)；Regulating reservoir (1) passes through the first elevator pump (A1) and quartz filter (2) upper end
Water inlet is connected, and the delivery port of quartz filter (2) lower end is by the second elevator pump (A2) and adsorptive reactor (3) upper end
Water inlet is connected, and the delivery port of adsorptive reactor (3) lower end is passed through intermediate pool (4), and desorbed solution is arranged at adsorptive reactor (3) bottom
Entrance and organic outlet；The delivery port of intermediate pool (4) enters water by the 3rd elevator pump (A3) and micro-electrolysis reactor (5)
Mouth is connected, and the delivery port of micro-electrolysis reactor (5) is passed through pH regulating reservoirs (6)；The industrial high organic wastewater of high salt passes through regulating reservoir
(1) enter quartz filter (2) filtering after adjusting and remove large particulate matter, water outlet is inhaled by adsorptive reactor (3), organic matter
It is attached on the sorbent, realize that salt is separated with the one-level of organic matter；Water outlet after one-level separation enters in micro-electrolysis reactor (5),
Wherein organic matter is further degraded, and realizes two stage treatment；High-salt wastewater is discharged into subsequent treatment after being adjusted in pH regulating reservoirs (6)
System；
Described biochemical system include desorbed solution reserve pool (2-0), anaerobism VTBR reactors (2-1), the first sedimentation basin (2-2),
Aerobic VTBR reactors (2-3), the second sedimentation basin (2-4), catalytic ozonation reactor (2-5) and parsing regenerated liquid collecting pit
(2-6)；Desorbed solution reserve pool (2-0) entrance is connected with the organic outlet of adsorptive reactor (3) bottom, desorbed solution reserve pool
(2-0) exports the entrance that anaerobism VTBR reactors (2-1) lower end is connected to through the 4th elevator pump (A4), anaerobism VTBR reactors
The outlet of (2-1) upper end connects the first sedimentation basin (2-2), and it is anti-that sedimentation basin (2-2) connects aerobic VTBR through the 5th elevator pump (A5)
The entrance of device (2-3) lower end is answered, the outlet of aerobic VTBR reactors (2-3) upper end connects the second sedimentation basin (2-4), the second precipitation
Pond (2-4) connects the entrance of catalytic ozonation reactor (2-5) lower end, catalytic ozonation reaction through the 5th elevator pump (A5)
The entrance of the outlet connection parsing regenerated liquid collecting pit (2-6) of device (2-5) upper end, the outlet of parsing regenerated liquid collecting pit (2-6)
It is connected with the desorbed solution entrance of adsorptive reactor (3) bottom, the waste water containing organic matter after being parsed in adsorptive reactor (3) is by inhaling
The organic outlet of reaction enclosure device (3) bottom sequentially pass through anaerobism VTBR reactors (2-1), aerobic VTBR reactors (2-3) and
Catalytic ozonation reactor (2-5), carries out tertiary treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720262773.6U CN206538318U (en) | 2017-03-17 | 2017-03-17 | A kind of device for handling the high organic wastewater of industrial high salt |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720262773.6U CN206538318U (en) | 2017-03-17 | 2017-03-17 | A kind of device for handling the high organic wastewater of industrial high salt |
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| CN201720262773.6U Expired - Fee Related CN206538318U (en) | 2017-03-17 | 2017-03-17 | A kind of device for handling the high organic wastewater of industrial high salt |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108147628A (en) * | 2018-02-28 | 2018-06-12 | 大连理工大学环境工程设计研究院有限公司 | The device that a kind of ethylene waste soda residue recycles |
| CN108341551A (en) * | 2018-02-28 | 2018-07-31 | 大连理工大学环境工程设计研究院有限公司 | A kind of processing method of liquefied gas alkaline mud waste liquid |
| CN108773944A (en) * | 2018-06-01 | 2018-11-09 | 山东深信节能环保科技有限公司 | Adsorb the method that electro-catalysis combination handles low dense organic wastewater with difficult degradation thereby |
-
2017
- 2017-03-17 CN CN201720262773.6U patent/CN206538318U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108147628A (en) * | 2018-02-28 | 2018-06-12 | 大连理工大学环境工程设计研究院有限公司 | The device that a kind of ethylene waste soda residue recycles |
| CN108341551A (en) * | 2018-02-28 | 2018-07-31 | 大连理工大学环境工程设计研究院有限公司 | A kind of processing method of liquefied gas alkaline mud waste liquid |
| CN108341551B (en) * | 2018-02-28 | 2021-01-05 | 大连理工大学环境工程设计研究院有限公司 | Treatment method of liquefied gas alkali residue waste liquid |
| CN108773944A (en) * | 2018-06-01 | 2018-11-09 | 山东深信节能环保科技有限公司 | Adsorb the method that electro-catalysis combination handles low dense organic wastewater with difficult degradation thereby |
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Granted publication date: 20171003 Termination date: 20200317 |