CN206352100U - A kind of degradation treatment device of coal chemical industrial waste water - Google Patents
A kind of degradation treatment device of coal chemical industrial waste water Download PDFInfo
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- CN206352100U CN206352100U CN201621360399.5U CN201621360399U CN206352100U CN 206352100 U CN206352100 U CN 206352100U CN 201621360399 U CN201621360399 U CN 201621360399U CN 206352100 U CN206352100 U CN 206352100U
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- waste water
- ozone
- coal chemical
- chemical industrial
- industrial waste
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Abstract
A kind of degradation treatment device for coal chemical industrial waste water that the utility model is provided, is first fallen the solid particulate filters in waste water by sedimentation basin, then can be adsorbed the suspension in waste water by the adsorption plate set in sedimentation basin, the peculiar smell gone in water removal；Effectively remove by ozone Oxidation Treatment room the organic matter and hard-degraded substance in waste water again afterwards, carrying out filtering again by biological oxidation room makes water cleaner, the apparatus structure is simple, practical, easy to operate, can make the cleaner of coal chemical industrial waste water processing.
Description
Technical field
The utility model belongs to technical field of waste water processing, and the degradation treatment more particularly, to a kind of coal chemical industrial waste water is filled
Put.
Background technology
Coal chemical industry enterprises waste discharge has based on high concentration gas washing wastewater containing a large amount of phenol, cyanogen, oil, ammonia nitrogen etc.
Poison, harmful substance.In comprehensive wastewater CODcr it is general in 5000mg/l or so, ammonia nitrogen in 200~500mg/l, it is organic contained by waste water
Pollutant includes phenols, polycyclc aromatic compound and nitrogenous, oxygen, heterocyclic compound of sulphur etc., is a kind of typically containing in distress
The industrial wastewater of the organic compound of degraded.Easily biodegradable organicses in waste water are mainly phenolic compound and benzene-like compounds；
Arsenic is coughed up, naphthalene, furans, is narrowed azole and is belonged to degradable type organic；The organic matter of difficult degradation mainly has arsenic pyridine, carbazole, biphenyl, three
Benzene etc..Processing of the existing facility to waste water be not comprehensive, handles not in place, in addition, needing substantial amounts of related facility during processing, ties
Structure is complicated, and cost is higher, cumbersome.
The content of the invention
Problem to be solved in the utility model is to provide a kind of degradation treatment device of coal chemical industrial waste water, apparatus structure letter
It is single, practical, it is easy to operate, the cleaner of coal chemical industrial waste water processing can be made.
The purpose of this utility model is the degradation treatment device for providing a kind of coal chemical industrial waste water, solves existing facility
Processing to waste water is not comprehensive, handles the defect such as not in place.
In order to solve the above technical problems, the technical solution adopted in the utility model is：
A kind of degradation treatment device for coal chemical industrial waste water that the utility model is provided, including water inlet, sedimentation basin, ozone oxygen
Change process chamber, biological oxidation room and delivery port, the water inlet is arranged on the lower end of sedimentation basin, the sedimentation basin and ozone oxidation
Process chamber is connected, and the ozone Oxidation Treatment room is connected with biological oxidation room, and the delivery port is arranged on biological oxidation room
Lower end.
Preferably, the sedimentation basin is to be provided with screen pack above hollow structure, the hollow structure, hollow structure
Lower section is set to sludge-tank, and the water inlet is arranged between screen pack and sludge-tank.
Preferably, adsorption plate is additionally provided with above the screen pack, the adsorption plate includes active charcoal material.
Preferably, the ozone Oxidation Treatment room includes ozone distributor, ozone appendix, supersonic generator and filler
Unit, wherein, the ozone distributor is arranged at the bottom of ozone Oxidation Treatment room, and one end of the ozone air inlet pipe extends smelly
The outside of oxygen oxidation processes room, the other end is connected with ozone distributor, and the supersonic generator is provided with ozone Oxidation Treatment
Indoor top, the filler unit is arranged on the middle part of ozone Oxidation Treatment room.
Preferably, the filler unit include the first filler unit and the second filler unit, first filler unit and
The structure of second filler unit is identical, and is symmetrical arranged between the two in center line.
Preferably, first filler unit and the second filler unit include several dividing plates, and the dividing plate is in vertical
Set, intake tunnel, the two ends alternating of described two adjacent intake tunnels are constituted between described two dividing plates being disposed adjacent
It is provided with plug at end part part.
Preferably, the dividing plate is made up of multiple baton rounds, and is connected between the adj acent plastic ball by connecting rod.
Preferably, catalyst is filled with the baton round, and its outer surface is evenly equipped with several circular holes.
Preferably, the specific surface area of the baton round is 1500-1600m2/g。。
Preferably, the bottom level of the biological oxidation room is provided with multiple biological oxidation rods, the biological oxidation rod
Lower horizontal is provided with carrier flow bed biomembrane.
Compared with prior art, the beneficial effects of the utility model are：
The degradation treatment device for a kind of coal chemical industrial waste water that the utility model is provided, first by sedimentation basin by waste water
Solid particulate filters fall, and effectively remove by ozone Oxidation Treatment room organic matter and hard-degraded substance in waste water again afterwards,
Carrying out filtering again by biological oxidation room makes water cleaner, and the apparatus structure is simple, practical, easy to operate, can make coal
Chemical wastewater treatment it is cleaner.
Further, the suspension in waste water can be adsorbed by the adsorption plate set in sedimentation basin, goes water removal
In peculiar smell.
Brief description of the drawings
Fig. 1 is the structural representation of processing unit；
Fig. 2 is the structural representation of filler unit；
Fig. 3 is the side structure schematic view of filler unit；
Wherein：1st, water inlet 2, sedimentation basin 21, adsorption plate 22, screen pack 3, the first pipeline 4, ozone Oxidation Treatment
Room 41, ozone distributor 42, ozone appendix 43, supersonic generator 44, the first filler unit 441, dividing plate 4411,
Baton round 4412, connecting rod 442, plug at end part part 443, intake tunnel 45, the second filler unit 5, the second pipeline
6th, biological oxidation room 61, biological oxidation rod 62, carrier flow bed biomembrane 7, delivery port.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
As shown in figure 1, at a kind of degradation treatment device of coal chemical industrial waste water, including water inlet 1, sedimentation basin 2, ozone oxidation
Room 4, biological oxidation room 6 and delivery port 7 are managed, water inlet 1 is connected with sedimentation basin 2, sedimentation basin 2 passes through the first pipeline 3 and ozone oxygen
Change process chamber 4 to be connected, ozone Oxidation Treatment room 4 is connected by the second pipeline 5 with biological oxidation room 6, biological oxidation room 6 and water outlet
Mouth 7 is connected.
The sedimentation basin 2 is to be provided with screen pack 22, the lower section of hollow structure above hollow structure, the hollow structure
Sludge-tank 23 is set to, the water inlet is arranged between screen pack 22 and sludge-tank 23.Waste water is carried out by screen pack 22
Primary filter, the solid particle that the screen pack 22 is used in filtered wastewater, solid particle is discharged into sludge-tank 23.Meanwhile, institute
The top for stating screen pack 22 is additionally provided with adsorption plate 21, and the adsorption plate 21 includes active charcoal material, can effectively remove color
Degree, stink simultaneously, also can remove most organic pollutants and some inorganic matters in secondary effluent, include some poisonous huge sum of moneys
Category.
The ozone Oxidation Treatment room 4 includes ozone distributor 41, ozone appendix 42, supersonic generator 43, first
The filler unit 44 of filler unit 44 and second, wherein, the ozone distributor 41 is arranged at the bottom of ozone Oxidation Treatment room 4,
The upper end of ozone distributor 41 is evenly arranged with miniature steam vent.One end of the ozone air inlet pipe 42 extends ozone Oxidation Treatment room
4 outside, the other end is connected with ozone distributor 41.
The supersonic generator 43 is provided with the top in ozone Oxidation Treatment room 4, the energy of supersonic generator 43
Enough play a part of vibrating waste water fluid stream, be conducive to the further contact of ozone and waste water.
The filler unit 45 of first filler unit 44 and second is arranged at the middle part of ozone Oxidation Treatment room 4.Such as Fig. 2 institutes
Show, first filler unit 44 includes several dividing plates 441, plug at end part part 442 and intake tunnel 443, multiple dividing plates
441 in being vertically arranged, and intake tunnel 443 is arranged between dividing plate 441, and plug at end part part 442 is distributed in logical into water respectively
Plug at end part part 442 in upper end or bottom in road 443, adjacent intake tunnel 443 is handed in upper end, bottom
For setting.
As shown in figure 3, each dividing plate 441 is constituted by multiple baton rounds 4411, by connecting rod 4412 by baton round 4411
It is attached, catalyst is filled with baton round 4411, baton round 4411 is made up of PVC materials, uniformly set on baton round 4411
It is equipped with several circular holes.
Second filler unit 45 is identical with the structure of the first filler unit 44, still, the second filler unit 45 and the first filler
It is symmetrical arranged between unit 44 in center line.Catalysis oxidation twice can be carried out, waste water is led to by the water inlet of the second filler unit 45
Baton round 4411 in the dividing plate 441 of the both sides of road 443 flows out, and the organic substance of difficult degradation enters in the presence of ozone and catalyst
Row degraded, then waste water is further degraded into the first filler unit 44, the effective organic matter and difficulty removed in waste water
Degradation material.
Further, the specific surface area of baton round 4411 is 1500-1600m2/ g, preferably most preferably 1556m2/g.Increase
The contact area of waste water and filler.
The bottom level of biological oxidation room 6 is provided with multiple biological oxidation rods 61, the lower horizontal of biological oxidation rod 61
It is provided with carrier flow bed biomembrane 62.Four mistakes are carried out to waste water by biological oxidation rod 61 and carrier flow bed biomembrane 62
Filter, obtains cleaner water.
The course of work of the present embodiment：Waste water is delivered in sedimentation basin 2, primary filter is carried out by screen pack 22, so
Further the suspension in waste water is adsorbed by adsorption plate 21 afterwards, the peculiar smell gone in water removal, then waste water enters ozone
Oxidation processes room 4, waste water enters the second filler unit 45, is flowed from baton round 4411 in the dividing plate 441 of the both sides of intake tunnel 443
Go out, the organic substance of difficult degradation is degraded in the presence of ozone and catalyst, waste water is carried out into the first filler unit 44
Further degraded, effectively removes the organic matter and hard-degraded substance in waste water, and then waste water enters biological oxidation room 6, passes through
Biological oxidation rod 61 and carrier flow bed biomembrane 62 are handled waste water, and clear water after treatment is discharged from delivery port 7.
The utility model carries out primary filter by screen pack, can be absorbed the suspension in waste water by adsorption plate
Come, the peculiar smell gone in water removal, reacted using ozone is produced by ozone Oxidation Treatment room with waste water, effectively remove waste water
In organic matter and hard-degraded substance；Carrying out filtering again by biological oxidation room makes water cleaner, the apparatus structure is simple,
Practicality, it is easy to operate, the cleaner of coal chemical industrial waste water processing can be made.
One embodiment of the present utility model is described in detail above, but content is only of the present utility model preferable
Embodiment, it is impossible to be considered as being used to limit practical range of the present utility model.It is all according to present utility model application scope made it is equal
Deng change and improvement etc., all should still it belong within patent covering scope of the present utility model.
Claims (10)
1. a kind of degradation treatment device of coal chemical industrial waste water, it is characterised in that：Including water inlet (1), sedimentation basin (2), ozone oxygen
Change process chamber (4), biological oxidation room (6) and delivery port (7), the water inlet (1) is arranged on the lower end of sedimentation basin (2), described
Sedimentation basin (2) is connected with ozone Oxidation Treatment room (4), and the ozone Oxidation Treatment room (4) is connected with biological oxidation room (6)
Logical, the delivery port (7) is arranged on the lower end of biological oxidation room (6).
2. a kind of degradation treatment device of coal chemical industrial waste water according to claim 1, it is characterised in that：The sedimentation basin
(2) it is hollow structure, is provided with above the hollow structure below screen pack (22), hollow structure and is set to sludge-tank
(23), the water inlet is arranged between screen pack (22) and sludge-tank (23).
3. a kind of degradation treatment device of coal chemical industrial waste water according to claim 2, it is characterised in that：The screen pack
(22) adsorption plate (21) is additionally provided with above, the adsorption plate (21) includes active charcoal material.
4. a kind of degradation treatment device of coal chemical industrial waste water according to claim 1, it is characterised in that：The ozone oxidation
Process chamber (4) includes ozone distributor (41), ozone appendix (42), supersonic generator (43) and filler unit, wherein, institute
State the bottom that ozone distributor (41) is arranged at ozone Oxidation Treatment room (4), one end of the ozone air inlet pipe (42) extends smelly
The outside of oxygen oxidation processes room (4), the other end is connected with ozone distributor (41), and the supersonic generator (43) is provided with smelly
Top in oxygen oxidation processes room (4), the filler unit is arranged on the middle part of ozone Oxidation Treatment room (4).
5. a kind of degradation treatment device of coal chemical industrial waste water according to claim 4, it is characterised in that：The filler unit
Including the first filler unit (44) and the second filler unit (45), first filler unit (44) and the second filler unit (45)
Structure it is identical, and be symmetrical arranged between the two in center line.
6. a kind of degradation treatment device of coal chemical industrial waste water according to claim 5, it is characterised in that：First filler
Unit (44) and the second filler unit (45) include several dividing plates (441), and the dividing plate (441) is described in being vertically arranged
Intake tunnel (443), the two of described two adjacent intake tunnels (443) are constituted between the dividing plate (441) that two are disposed adjacent
End has been arranged alternately plug at end part part (442).
7. a kind of degradation treatment device of coal chemical industrial waste water according to claim 6, it is characterised in that：The dividing plate
(441) it is made up of, and is connected between the adj acent plastic ball (4411) by connecting rod (4412) multiple baton rounds (4411).
8. a kind of degradation treatment device of coal chemical industrial waste water according to claim 7, it is characterised in that：The baton round
(4411) catalyst is filled with, and its outer surface is evenly equipped with several circular holes.
9. a kind of degradation treatment device of coal chemical industrial waste water according to claim 7 or 8, it is characterised in that：The plastics
The specific surface area of ball (4411) is 1500-1600m2/g。
10. a kind of degradation treatment device of coal chemical industrial waste water according to claim 1, it is characterised in that：The biological oxygen
The bottom level for changing room (6) is provided with multiple biological oxidation rods (61), and the lower horizontal of the biological oxidation rod (61) is provided with
Carrier flow bed biomembrane (62).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621360399.5U CN206352100U (en) | 2016-12-12 | 2016-12-12 | A kind of degradation treatment device of coal chemical industrial waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621360399.5U CN206352100U (en) | 2016-12-12 | 2016-12-12 | A kind of degradation treatment device of coal chemical industrial waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206352100U true CN206352100U (en) | 2017-07-25 |
Family
ID=59347305
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621360399.5U Expired - Fee Related CN206352100U (en) | 2016-12-12 | 2016-12-12 | A kind of degradation treatment device of coal chemical industrial waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206352100U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107879554A (en) * | 2017-11-20 | 2018-04-06 | 叶子毓 | A kind of waste water circulation utilized device and application method |
-
2016
- 2016-12-12 CN CN201621360399.5U patent/CN206352100U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107879554A (en) * | 2017-11-20 | 2018-04-06 | 叶子毓 | A kind of waste water circulation utilized device and application method |
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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: 20170725 Termination date: 20171212 |
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| CF01 | Termination of patent right due to non-payment of annual fee |