CN205442858U - Ozone air floating recycling treatment device - Google Patents
Ozone air floating recycling treatment device Download PDFInfo
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- CN205442858U CN205442858U CN201521083334.6U CN201521083334U CN205442858U CN 205442858 U CN205442858 U CN 205442858U CN 201521083334 U CN201521083334 U CN 201521083334U CN 205442858 U CN205442858 U CN 205442858U
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Abstract
The utility model discloses an ozone air floating recycling treatment device mainly solves the waste that the current ozone air floating device that exists can cause ozone pollution or ozone resource among the prior art, the lower problem of ozone utilization ratio. This ozone air floating recycling treatment device include flocculation reaction tank, in proper order with air supporting pond, the clean water basin of flocculation reaction tank intercommunication, the top in air supporting pond has connected gradually the sediment machine of scraping, exhaust gas collection cover, the exhaust gas collection cover communicates through the pipeline in proper order has ozone generator, gas - liquid mixing pump, gas - liquid mixing pump has liquid inlet and gas -liquid export, liquid inlet and clean water basin intercommunication, gas -liquid export and air supporting pond intercommunication. By the proposal, the utility model discloses reached and not caused the waste of ozone pollution or ozone resource and the purpose of ozone high -usage, had very high practical value and spreading value.
Description
Technical field
This utility model relates to a kind of equipment utilizing ozone air-float to process sewage, specifically, relates to a kind of ozone air-float cyclic processing device.
Background technology
In the waste water that Coal Chemical Industry produces, organic compound is extremely complex, in comprehensive wastewater COD typically at about 5000mg/l, ammonia nitrogen 200～500mg/l, organic pollutants contained by waste water includes phenols, polycyclc aromatic compound and nitrogenous, the heterocyclic compound etc. of oxygen, sulfur, is the industrial wastewater of a kind of typical organic compound containing difficult degradation；Hospital sewage contains a large amount of sex pheromone, and outside parasitic ovum such as roundworm egg and various virus such as hepatitis virus, pulmonary tuberculosis bacterium and dysentery bacillus etc., possibly together with a large amount of pollutant, wherein Organic substance accounts for about the 60% of total amount of pollutants discharge, and indissoluble solution material accounts for the 40% of total amount.
Above-mentioned rock gas, Coal Chemical Industry, medical and chemical industry and the process of municipal sewage, if carrying out disinfection decontamination with chloroform, carbon tetrachloride, vinyl chloride, trichloro ethylene, chlorophenols, will produce carcinogen after a procedure, i.e. can produce secondary pollution；And ozone is strong oxidizer, hazardous compound can be carried out natural decomposition after a procedure, not there is carcinogenecity and other harm, the strand of harmful poisonous compound be had the efficient oxidation decomposition function, and virus and antibacterial are had fabulous killing effect；Trade effluent, medical sewage, municipal sewage, mud and clean water can be carried out non-harmful environmental protection treatment.
The defect that existing ozone air-float device exists has: first, its ozone tail gas produced directly discharges or discharges after vent ozone destructor destroys, directly discharge existence causes ozone pollution, and after vent ozone destructor destroys, discharge causes the waste of ozone resource and wastes the energy；Second, now directly multiple ozone release head is being set at the bottom of cesspool, ozone bubble rises too fast, and ramps, and makes ozone utilization rate relatively low.
Utility model content
Problem to be solved in the utility model is that existing ozone air-float device can cause ozone pollution or the waste of ozone resource；Ozone utilization rate is relatively low.
In order to solve the problems referred to above, this utility model following technical scheme of offer:
Ozone air-float cyclic processing device includes flocculation tank, the flotation tank connected successively, clear water reserviors with flocculation tank；The top of flotation tank is connected with Slag Scraping Device, exhaust collection cover in turn；Exhaust collection cover has been sequentially communicated ozonator, gas-liquid mixing pump by pipeline；Gas-liquid mixing pump has liquid inlet and gas liquid outlet, and liquid inlet connects with clear water reserviors, and gas liquid outlet connects with flotation tank.
Further, the bottom of flotation tank is provided with multiple transverse tube, multiple vertical tube；Multiple transverse tubes are arranged in order, and are connected by least one vertical tube between adjacent transverse tube；Arbitrary transverse tube or arbitrary vertical tube connect with gas liquid outlet；The most uniformly it is communicated with on transverse tube and vertical tube between multiple release head, release head and transverse tube or vertical tube to be communicated with and controls the rotator that release head rotates；Rotator can replace with other equipment with spinfunction.
Further, flocculation tank is provided with agitator；Agitator includes puddler, and one end of puddler connects has motor, motor to be positioned at outside flocculation tank；Multiple stirring paddle it is uniformly provided with on puddler.
Further, adsorption tank it is communicated with between flocculation tank and flotation tank.
Specifically, any one or more it is provided with in activated carbon, montmorillonite, Maifanitum in adsorption tank；Also other equipment with adsorption function can be provided with in adsorption tank.
Specifically, flocculation tank is communicated with grid pond, and grid pond connects with treatment sewage pond.
Compared with prior art, this utility model has the advantages that ozone continues to rise through exhaust collection cover from flotation tank and enters ozonator and enter back into gas-liquid mixing pump and reuse, form the recycling of ozone tail gas, sewage disposal enters clear water reserviors for gas-liquid mixing pump after completing, form the recycling after sewage disposal, this utility model can carry out the recycling after the recycling of ozone tail gas and sewage disposal, it is to avoid ozone pollution that direct discharge brings and the ozone resource brought after destroying and the waste of the energy.
Accompanying drawing explanation
Fig. 1 is the structural representation of embodiment 1.
Fig. 2 is the structural representation of embodiment 2.
Fig. 3 is the structure for amplifying schematic diagram of part A in Fig. 2.
Fig. 4 is the connection diagram of transverse tube and vertical tube.
In above-mentioned accompanying drawing, component names corresponding to reference is as follows:
1-flocculation tank, 2-flotation tank, 3-clear water reserviors, 4-Slag Scraping Device, 5-exhaust collection cover, 6-gas-liquid mixing pump, 7-transverse tube, 8-vertical tube, 9-release head, 10-rotator, 11-puddler, 12-motor, 13-stirring paddle, 14-adsorption tank, 15-grid pond, 16-ozonator.
Detailed description of the invention
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings, and embodiment of the present utility model includes but not limited to the following example.
Embodiment 1
As shown in Fig. 1, Fig. 3, Fig. 4, ozone air-float cyclic processing device includes flocculation tank 1, the flotation tank 2 connected successively, clear water reserviors 3 with flocculation tank 1；The top of flotation tank 2 is connected with Slag Scraping Device 4, exhaust collection cover 5 in turn；Exhaust collection cover 5 has been sequentially communicated ozonator, gas-liquid mixing pump 6 by pipeline；Gas-liquid mixing pump 6 has liquid inlet and gas liquid outlet, and liquid inlet connects with clear water reserviors 3, and gas liquid outlet connects with flotation tank 2；The bottom of flotation tank 2 is provided with multiple transverse tube 7, multiple vertical tube 8；Multiple transverse tubes 7 are arranged in order, and are connected by least one vertical tube 8 between adjacent transverse tube 7；Arbitrary transverse tube 7 or arbitrary vertical tube 8 connect with gas liquid outlet；The most uniformly it is communicated with on transverse tube 7 and vertical tube 8 between multiple release head 9, release head 9 and transverse tube 7 or vertical tube 8 to be communicated with and controls the rotator 10 that release head 9 rotates；Flocculation tank 1 is provided with agitator；Flocculation tank connects 1 and is connected to flocculant chemicals feeder and coagulant chemicals feeder；Agitator includes puddler 11, and one end of puddler 11 connects has motor 12, motor 12 to be positioned at outside flocculation tank 1；Multiple stirring paddle 13 it is uniformly provided with on puddler 11.
Wherein, rotator 10 can replace with other equipment with spinfunction；Agitator makes sewage be sufficiently mixed with the flocculant in flocculation tank 1 and coagulant, rapid subsidence；Rotator 10 is low speed rotation device 10.
Embodiment 2
Shown in Fig. 2-4, the present embodiment difference from embodiment 1 is, flocculation tank 1 is communicated with grid pond 15, and grid pond 15 connects with treatment sewage pond；Adsorption tank 14 it is communicated with between flocculation tank 1 and flotation tank 2；Any one or more it is provided with in activated carbon, montmorillonite, Maifanitum in adsorption tank 14；Also other equipment with adsorption function can be provided with in adsorption tank 14.
nullShown in Fig. 2-4，Embodiment 1 and embodiment 2 are in use，Sewage enters after grid pond 15 is tentatively filtered from treatment sewage pond and enters flocculation tank 1，After by flocculant chemicals feeder and coagulant chemicals feeder, dosing in flocculation tank 1 makes the float in sewage and finely ground particle substance rapid precipitation，Enter after adsorption tank 14 filters out precipitate and finely ground particle substance and enter flotation tank 2，Ozonator 16 produce ozone by gas-liquid mixing pump 6 mix by release head 9 discharge into wastewater disinfection sterilize，Ozone bubbles drives float to rise，Scraped by Slag Scraping Device 4，Ozone bubbles ruptures，Ozone continues to rise through exhaust collection cover 5 and enters ozonator 16 and enter back into gas-liquid mixing pump 6 and reuse，Form the recycling of ozone tail gas，Sewage disposal enters clear water reserviors 3 for gas-liquid mixing pump 6 after completing，Form the recycling after sewage disposal，This utility model can carry out the recycling after the recycling of ozone tail gas and sewage disposal，Avoid and directly discharge the ozone pollution brought and the ozone resource brought after destroying and the waste of the energy；This utility model make release head 9 to rotate by rotator 10, release head 9 discharges ozone bubbles in rotary course, ozone bubbles is made to make its curve increase with certain rotary speed, rise time longer more with the time of contact of sewage, therefore the Disinfection Effect reached is more preferably, the utilization rate of ozone is higher.
According to above-described embodiment, this utility model just can be realized well.What deserves to be explained is; on the premise of designing based on said structure; for solving same technical problem; even if some made on this utility model are without substantial change or polishing; the essence of the technical scheme used is still as this utility model, therefore it should also be as in protection domain of the present utility model.
Claims (6)
1. an ozone air-float cyclic processing device, including flocculation tank (1), it is characterised in that: also include flotation tank (2), the clear water reserviors (3) connected successively with flocculation tank (1)；The top of flotation tank (2) is connected with Slag Scraping Device (4), exhaust collection cover (5) in turn；Exhaust collection cover (5) has been sequentially communicated ozonator (16), gas-liquid mixing pump (6) by pipeline；Gas-liquid mixing pump (6) has liquid inlet and gas liquid outlet, and liquid inlet connects with clear water reserviors (3), and gas liquid outlet connects with flotation tank (2).
Ozone air-float cyclic processing device the most according to claim 1, it is characterised in that: the bottom of flotation tank (2) is provided with multiple transverse tube (7), multiple vertical tube (8)；Multiple transverse tubes (7) are arranged in order, and are connected by least one vertical tube (8) between adjacent transverse tube (7)；Arbitrary transverse tube (7) or arbitrary vertical tube (8) connect with gas liquid outlet；The most uniformly it is communicated with on transverse tube (7) and vertical tube (8) between multiple release head (9), release head (9) and transverse tube (7) or vertical tube (8) to be communicated with and controls the rotator (10) that release head (9) rotates.
Ozone air-float cyclic processing device the most according to claim 2, it is characterised in that: flocculation tank is provided with agitator in (1)；Agitator includes puddler (11), and one end of puddler (11) connects has motor (12), motor (12) to be positioned at flocculation tank (1) outward；Multiple stirring paddle (13) it is uniformly provided with on puddler (11).
Ozone air-float cyclic processing device the most according to claim 3, it is characterised in that: it is communicated with adsorption tank (14) between flocculation tank (1) and flotation tank (2).
Ozone air-float cyclic processing device the most according to claim 4, it is characterised in that: it is provided with in activated carbon, montmorillonite, Maifanitum any one or more in adsorption tank (14).
6. according to the ozone air-float cyclic processing device described in any one of claim 1-5, it is characterised in that: flocculation tank (1) is communicated with grid pond (15), and grid pond (15) connect with treatment sewage pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521083334.6U CN205442858U (en) | 2015-12-23 | 2015-12-23 | Ozone air floating recycling treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521083334.6U CN205442858U (en) | 2015-12-23 | 2015-12-23 | Ozone air floating recycling treatment device |
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| Publication Number | Publication Date |
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| CN205442858U true CN205442858U (en) | 2016-08-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201521083334.6U Active CN205442858U (en) | 2015-12-23 | 2015-12-23 | Ozone air floating recycling treatment device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439323A (en) * | 2015-12-23 | 2016-03-30 | 云南润玖环境工程有限公司 | Ozone gas floatation circular processing apparatus |
| CN108503095A (en) * | 2018-06-23 | 2018-09-07 | 安徽拓谷物联科技有限公司 | Domestic sewage in rural areas integrated equipment for wastewater treatment |
-
2015
- 2015-12-23 CN CN201521083334.6U patent/CN205442858U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439323A (en) * | 2015-12-23 | 2016-03-30 | 云南润玖环境工程有限公司 | Ozone gas floatation circular processing apparatus |
| CN108503095A (en) * | 2018-06-23 | 2018-09-07 | 安徽拓谷物联科技有限公司 | Domestic sewage in rural areas integrated equipment for wastewater treatment |
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