CN209493451U - A kind of spraying Wastewater zero-discharge treatment system - Google Patents
A kind of spraying Wastewater zero-discharge treatment system Download PDFInfo
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- CN209493451U CN209493451U CN201920132807.9U CN201920132807U CN209493451U CN 209493451 U CN209493451 U CN 209493451U CN 201920132807 U CN201920132807 U CN 201920132807U CN 209493451 U CN209493451 U CN 209493451U
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Abstract
The utility model relates to sewage treatment fields, a kind of spraying Wastewater zero-discharge treatment system is disclosed, including industrial wastewater conditioning tank, the precipitating component being connected on the industrial wastewater conditioning tank, the biochemical reaction component connecting with the precipitating component, the end processing component connecting with the biochemical reaction component and the clear water reserviors being connected on the end processing component;The precipitating component includes the air-float integral equipment connecting with industrial wastewater conditioning tank, the fenton reaction system connecting with the air-float integral equipment, the coagulation-flocculation pond connecting with the fenton reaction system, the efficient sedimentation tank connecting with the coagulation-flocculation pond, the intermediate pool connecting with the efficient sedimentation tank, and the intermediate pool is connect with the biochemical reaction component.The utility model has the effect of being not easy to influence subsequent biochemical reaction.
Description
Technical field
The utility model relates to the technical fields of sewage treatment, more particularly, to a kind of spraying wastewater zero discharge processing system
System.
Background technique
Spraying waste water is mainly derived from water paint at present, and water paint emulsifies lotion after being be the paint that film forming matter is prepared, this
Kind paint can be diluted in construction with water.
The existing processing to aqueous paint waste water mostly use the mode of biochemical reaction to the pollutant in water paint at
Reason.
Prior art among the above has the following deficiencies: since water paint has the property dispersed in water, is locating
During managing aqueous paint waste water, frequently encounter foam is big, demulsification not exclusively, haze reduction it is difficult, influence subsequent biochemical reaction.
Utility model content
In view of the deficienciess of the prior art, the utility model lies in that provide a kind of spraying Wastewater zero-discharge treatment system,
Have the effect of being not easy to influence subsequent biochemical reaction.
To achieve the above object, the utility model provides following technical solution: a kind of spraying wastewater zero discharge processing system
System, connect including industrial wastewater conditioning tank, the precipitating component being connected on the industrial wastewater conditioning tank, with the precipitating component
Biochemical reaction component, the end processing component that is connect with the biochemical reaction component and be connected on the end processing component
Clear water reserviors;The precipitating component includes the air-float integral equipment connecting with industrial wastewater conditioning tank and air bearing one
The fenton reaction system for changing equipment connection, the coagulation-flocculation pond connecting with the fenton reaction system are wadded a quilt with cotton with the coagulation
The efficient sedimentation tank of solidifying pond connection, the intermediate pool connecting with the efficient sedimentation tank, the intermediate pool and the biochemistry are anti-
Component is answered to connect.
By using above-mentioned technical proposal, waste water is injected into industrial wastewater conditioning tank by worker, and then waste water is conveyed
It is precipitated to precipitating component, the pollutant of fraction floats is removed at the present air-float integral equipment of waste water, is then existed
The precipitating of pollutant is carried out at fenton reaction system, coagulation-flocculation pond and efficient sedimentation tank, finally more limpid waste water stream
Enter to intermediate pool, then the waste water in intermediate pool carries out biochemical reaction through biochemical reaction component again, after biochemical reaction
Waste water be drained into clear water reserviors after the processing by end processing component, waste water carry out biochemical reaction be that turbidity is lower,
It is not easy to influence biochemical reaction, so that the efficiency of biochemical reaction is higher.
The utility model is further arranged to: the biochemical reaction component includes reacting with the UASB of intermediate pool connection
Pond, the aerobic tank being connected to the anoxic pond, is connected to the aerobic tank anoxic pond being connected to the UASB reaction tank
MBR reaction tank, the MBR reaction tank are connect with the end processing component, and the MBR reaction tank is connect with the clear water reserviors.
By using above-mentioned technical proposal, UASB reaction tank generates biogas and precipitates suspended matter, to reduce waste water
Turbidity, the biogas of generation can recycle, and the bacterium in anoxic pond and aerobic tank handles pollutant, MBR reaction
Pond substantially reduces ammonia nitrogen and suspended matter in waste water by membrane bioreactor.
The utility model is further arranged to: cleaning water tank is connected in the intermediate pool, the cleaning water tank is separate
One end of intermediate pool is connect with clear water reserviors.
By using above-mentioned technical proposal, the waste water in intermediate pool enters clear water reserviors by the cleaning of cleaning water tank
It is interior, the cleaning of water tank is cleaned so that waste water is more clean.
The utility model is further arranged to: the intermediate pool is connect by connecting tube with the cleaning water tank, described
Connecting tube is located in the intermediate pool and the bottom far from the intermediate pool.
By using above-mentioned technical proposal, bottom of the connecting tube far from intermediate pool, since intermediate pool bottom has one
Fixed sediment, connecting tube present position can the water to intermediate pool top preferably absorbed, so that connecting tube be made to inhale
The water of receipts is more clean.
The utility model is further arranged to: the end processing component includes in being connected on the MBR reaction tank
Between water tank, the cartridge filter being connected on the intermediate water tank, the RO system that is connected on the cartridge filter, the RO
System is connect with the clear water reserviors.
By using above-mentioned technical proposal, cartridge filter further filters waste water, and RO system passes through reverse osmosis
Saturating mode in water bacterium, virus, colloid, organic matter and 98% or more dissolubility salt remove so that useless
Water is more clean.
The utility model is further arranged to: the RO system include the first RO film, the 2nd RO film, RO concentrated water case and efficiently
Steam generator, the first RO film and the connection of the 2nd RO film, the 2nd RO film are connected to RO concentrated water case, and RO concentrated water case and high-efficiency steam are sent out
Raw device connection, one end of the first RO film are connected to cartridge filter, and the other end is connected to high-efficient steam generator and clear water reserviors, the
Two RO films are also connected to high-efficient steam generator and clear water reserviors.
By using above-mentioned technical proposal, the first RO film and the 2nd RO film are filtered water, and RO concentrated water case recycles concentrated water,
High-efficient steam generator is evaporated water, and water after cooling is delivered at clear water reserviors, to carry out recycling benefit to part concentrated water
With.
The utility model is further arranged to: ultraviolet sterilizer, the ultraviolet sterilization are equipped on the clear water reserviors
Device is in communication with the outside.
By using above-mentioned technical proposal, the water in clear water reserviors passes through ultraviolet sterilizer, ultraviolet sterilization in outflow
Device kills the bacterium in water, so that the water of output is more clean.
The utility model is further arranged to: gas transmission component, the gas transmission group are equipped in the industrial wastewater conditioning tank
Part include the appendix being fixedly connected in the industrial wastewater conditioning tank, several be mounted on gas transmissions on the appendix point
Pipe.
By using above-mentioned technical proposal, for appendix by air input value industrial wastewater conditioning tank, gas transmission is in charge of will be empty
Gas discharge, so that pollutant is distributed more uniformly in waste water, facilitates the processing in later period to stir to waste water.
In conclusion the utility model has the following beneficial effects:
By setting precipitating component, biochemical reaction component and end processing component, precipitating component first precipitates waste water
Operation, biochemical reaction component and end processing component handle the waste water after precipitating, so that biochemical reaction and end
Processing is not easily susceptible to influence, treatment effeciency with higher.
Detailed description of the invention
Fig. 1 is the external structure schematic diagram of the utility model;
Fig. 2 is enlarged drawing at the A of Fig. 1, the connection structure that embodiment appendix and gas transmission are in charge of;
Fig. 3 is the inner connecting structure schematic diagram for embodying precipitating component.
Appended drawing reference: 1, industrial wastewater conditioning tank;11, gas transmission component;111, appendix;112, gas transmission is in charge of;2, it precipitates
Component;21, air-float integral equipment;22, fenton reaction system;23, coagulation-flocculation pond;24, efficient sedimentation tank;25, intermediate
Pond;3, biochemical reaction component;31, UASB reaction tank;32, anoxic pond;33, aerobic tank;34, MBR reaction tank;4, end-o f-pipe -control
Component;41, intermediate water tank;42, cartridge filter;43, RO system;431, the first RO film;432, the 2nd RO film;433, RO concentrated water
Case;434, high-efficient steam generator;5, clear water reserviors;51, ultraviolet sterilizer;6, water tank is cleaned;61, connecting tube.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
It referring to Figures 1 and 2, is a kind of spraying Wastewater zero-discharge treatment system disclosed by the utility model, including Industry Waste
Water conditioning tank 1, gas transmission component 11 is equipped in industrial wastewater conditioning tank 1, and gas transmission component 11 includes that appendix 111 and gas transmission are in charge of
112, appendix 111 is fixedly connected in industrial wastewater conditioning tank 1, several gas transmissions are in charge of 112 and are fixedly connected on appendix 111
It above and along the length direction of appendix 111 is uniformly distributed, gas transmission is in charge of 112 and is connected to appendix 111.
Referring to Figure 1 and Figure 3, precipitating component 2 is connected on industrial wastewater conditioning tank 1, precipitating component 2 includes air-float integral
Equipment 21, fenton reaction system 22, coagulation-flocculation pond 23, efficient sedimentation tank 24 and intermediate pool 25, air-float integral equipment
21 are connected to industrial wastewater conditioning tank 1, and fenton reaction system 22 is connected to air-float integral equipment 21, coagulation-flocculation pond 23 with
Fenton reaction system 22 is connected to, and efficient sedimentation tank 24 is connected to coagulation-flocculation pond 23, intermediate pool 25 and efficient sedimentation tank 24
Connection.
Intermediate pool 25 is connect with biochemical reaction component 3, biochemical reaction component 3 include UASB reaction tank 31, anoxic pond 32,
Aerobic tank 33 and MBR reaction tank 34, UASB reaction tank 31 are connected to intermediate pool 25, and anoxic pond 32 and UASB reaction tank 31 connect
Logical, aerobic tank 33 is connected to anoxic pond 32, and MBR reaction tank 34 is connected to aerobic tank 33.
End processing component 4 is connected on MBR reaction tank 34.End processing component 4 includes intermediate water tank 41, security personnel's filtering
Device 42 and RO system 43, intermediate water tank 41 are connected to cartridge filter 42, the one end of intermediate water tank 41 far from cartridge filter 42
It is connected to MBR reaction tank 34.RO system 43 includes the first RO film 431, the 2nd RO film 432, RO concentrated water case 433 and high-efficiency steam hair
Raw device 434, the first RO film 431 are connected to the 2nd RO film 432, and the 2nd RO film 432 is connected to RO concentrated water case 433, RO concentrated water case 433
It is connected to high-efficient steam generator 434.
Clear water reserviors 5 are connected on high-efficient steam generator 434, high-efficient steam generator 434 is connected to clear water reserviors 5, and MBR is anti-
Pond 34 is answered to be connected to clear water reserviors 5.It is connected to by connecting tube 61 with cleaning water tank 6 in intermediate pool 25, one end position of connecting tube 61
In in the intermediate pool 25 and bottom far from intermediate pool 25, the other end is connected to cleaning water tank 6, and cleaning water tank 6 is far from intermediate
The one end in pond 25 is connected to clear water reserviors 5, and ultraviolet sterilizer 51 is equipped on clear water reserviors 5.
The implementation principle of the present embodiment are as follows: waste water is injected into industrial wastewater conditioning tank 1 by worker, and then waste water is conveyed
It is precipitated to precipitating component 2, the pollutant of fraction floats is removed at present 21 equipment of air-float integral equipment of waste water, then
The precipitating of pollutant is carried out at fenton reaction system 22, coagulation-flocculation pond 23 and efficient sedimentation tank 24, it is finally more limpid
Waste water be flowed into intermediate pool 25, then the waste water in intermediate pool 25 again through biochemical reaction component 3 carry out biochemical reaction, give up
Water successively passes through UASB reaction tank 31, anoxic pond 32, aerobic tank 33 and MBR reaction tank 34, leave the waste water of MBR reaction tank 34 according to
It is secondary to be finally drained into clear water reserviors 5 by intermediate water tank 41, cartridge filter 42 and RO system 43, the waste water for leaving RO system 43
In.When water is discharged from clear water reserviors 5, by ultraviolet sterilizer 51, so that the bacterium to water is killed.First RO film
431 and the 2nd RO film 432 water is filtered, RO concentrated water case 433 recycles concentrated water, and high-efficient steam generator 434 steams water
Hair, water after cooling is delivered at clear water reserviors 5, to be recycled to part concentrated water.
The embodiment of present embodiment is the preferred embodiment of the utility model, and not limitation is originally practical new according to this
The protection scope of type, therefore: the equivalence changes that all structures, shape, principle according to the utility model are done should all be covered by practical
Within novel protection scope.
Claims (8)
1. a kind of spraying Wastewater zero-discharge treatment system, it is characterized in that: including industrial wastewater conditioning tank (1), being connected to the work
Precipitating component (2) on industry wastewater equalization pond (1), the biochemical reaction component (3) being connect with precipitating component (2), with it is described
The end processing component (4) of biochemical reaction component (3) connection and the clear water reserviors (5) being connected on the end processing component (4);
Precipitating component (2) includes the air-float integral equipment (21) connecting with industrial wastewater conditioning tank (1) and air bearing one
The fenton reaction system (22) for changing equipment (21) connection, the coagulation-flocculation pond being connect with the fenton reaction system (22)
(23), the efficient sedimentation tank (24) being connect with the coagulation-flocculation pond (23), the centre being connect with the efficient sedimentation tank (24)
Pond (25), the intermediate pool (25) connect with the biochemical reaction component (3).
2. a kind of spraying Wastewater zero-discharge treatment system according to claim 1, it is characterized in that: the biochemical reaction component
It (3) include the UASB reaction tank (31) being connected to intermediate pool (25), the anoxic pond that is connected to the UASB reaction tank (31)
(32), the aerobic tank (33) being connected to the anoxic pond (32), the MBR reaction tank (34) being connected to the aerobic tank (33), institute
It states MBR reaction tank (34) to connect with the end processing component (4), the MBR reaction tank (34) and the clear water reserviors (5) are even
It connects.
3. a kind of spraying Wastewater zero-discharge treatment system according to claim 2, it is characterized in that: the intermediate pool (25)
On be connected with cleaning water tank (6), cleaning water tank (6) connect far from the one end of intermediate pool (25) with clear water reserviors (5).
4. a kind of spraying Wastewater zero-discharge treatment system according to claim 3, it is characterized in that: the intermediate pool (25)
It is connect by connecting tube (61) with the cleaning water tank (6), the connecting tube (61) is located in the intermediate pool (25) and remote
Bottom from the intermediate pool (25).
5. a kind of spraying Wastewater zero-discharge treatment system according to claim 2, it is characterized in that: the end processing component
It (4) include the intermediate water tank (41) being connected on the MBR reaction tank (34), the security personnel being connected on the intermediate water tank (41)
Filter (42), the RO system (43) being connected on the cartridge filter (42), the RO system (43) and the clear water reserviors
(5) it connects.
6. a kind of spraying Wastewater zero-discharge treatment system according to claim 5, it is characterized in that: the RO system (43) is wrapped
Include the first RO film (431), the 2nd RO film (432), RO concentrated water case (433) and high-efficient steam generator (434), the first RO film
(431) be connected to the 2nd RO film (432), the 2nd RO film (432) is connected to RO concentrated water case (433), RO concentrated water case (433) and efficiently
Steam generator (434) connection, one end of the first RO film (431) are connected to cartridge filter (42), the other end and high-efficiency steam
Generator (434) is connected to clear water reserviors (5), and the 2nd RO film (432) also connects with high-efficient steam generator (434) and clear water reserviors (5)
It is logical.
7. a kind of spraying Wastewater zero-discharge treatment system according to claim 1, it is characterized in that: on the clear water reserviors (5)
It is equipped with ultraviolet sterilizer (51), the ultraviolet sterilizer (51) is in communication with the outside.
8. a kind of spraying Wastewater zero-discharge treatment system according to claim 1, it is characterized in that: the industrial wastewater is adjusted
It is equipped with gas transmission component (11) in pond (1), the gas transmission component (11) includes being fixedly connected on the industrial wastewater conditioning tank (1)
(112) are in charge of in interior appendix (111), several gas transmissions being mounted on the appendix (111).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201920132807.9U CN209493451U (en) | 2019-01-25 | 2019-01-25 | A kind of spraying Wastewater zero-discharge treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201920132807.9U CN209493451U (en) | 2019-01-25 | 2019-01-25 | A kind of spraying Wastewater zero-discharge treatment system |
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Publication Number | Publication Date |
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CN209493451U true CN209493451U (en) | 2019-10-15 |
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ID=68156002
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CN201920132807.9U Active CN209493451U (en) | 2019-01-25 | 2019-01-25 | A kind of spraying Wastewater zero-discharge treatment system |
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CN (1) | CN209493451U (en) |
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2019
- 2019-01-25 CN CN201920132807.9U patent/CN209493451U/en active Active
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