CN207632644U - A kind of processing system of oily waste water - Google Patents

A kind of processing system of oily waste water Download PDF

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Publication number
CN207632644U
CN207632644U CN201721502762.7U CN201721502762U CN207632644U CN 207632644 U CN207632644 U CN 207632644U CN 201721502762 U CN201721502762 U CN 201721502762U CN 207632644 U CN207632644 U CN 207632644U
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China
Prior art keywords
charging tank
retort
pipeline
pond
processing
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CN201721502762.7U
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Chinese (zh)
Inventor
陈明翠
谢应权
汪君晖
陈志军
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Chongqing Neide Environmental Technology Co., Ltd.
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Chongqing Snyder Water Treatment Technology Co Ltd
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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The utility model belongs to technical field of waste water processing, more particularly to a kind of processing system of oily waste water, including grille well, oil separator, electric air floating device, ozone pond, the first processing pond, second processing pond, third processing pond, the first charging tank, the second charging tank, the first retort, third charging tank, the 4th charging tank, the 5th charging tank, the second retort, the 6th charging tank, the 7th charging tank, third retort, micro-filtrate membrane filtration device and collecting pit;The processing system of the utility model offer oily waste water can effectively reduce the processing cost of oily sludge, and oiliness sewage treatment significant effect realizes the separation of oil and water, meets national standard of drainage.

Description

A kind of processing system of oily waste water
Technical field
The utility model belongs to technical field of waste water processing more particularly to a kind of processing system of oily waste water.
Background technology
Oily waste water main source is oil-containing rainwater and cleans the oily wastewater of the generations such as oil depot, fuel charger, place, is existed Water have the characteristics that water variation greatly, discharge it is discontinuous.Biodegradability is poor, and traditional treatment process has:As Physical is (heavy Drop, machinery, centrifugation, coarse, filtering, UF membrane etc.);Physical-chemical process (flotation, absorption, ion exchange etc.);Chemical method is (solidifying Gather, be acidified, saltout, be electrolysed);Biochemical process (activated sludge, biofilter, oxidation pond etc.), traditional flocculation sediment, Not only the big operating cost of dosage is high for air supporting partition method, but also causes secondary pollution, generates a large amount of oily sludges, belongs to dangerous Waste, processing cost are expensive;The methods of absorption, filtering are also required to artificial frequently cleaning, and management is inconvenient, similarly have processing dirty The problem of mud, it is difficult to reach discharging standards.
Utility model content
In order to solve the above-mentioned technical problem the utility model provides a kind of processing system of oily waste water, can effectively handle Oily waste water, it is at low cost, treatment effeciency is high, meet discharging standards.
The technical solution that the utility model solves above-mentioned technical problem is as follows:
The utility model provides a kind of processing system of oily waste water, including grille well, oil separator, electric air floating device, smelly Oxygen pond, the first processing pond, second processing pond, third processing pond, the first charging tank, the second charging tank, the first retort, third are thrown Batch can, the 4th charging tank, the 5th charging tank, the second retort, the 6th charging tank, the 7th charging tank, third retort, microfiltration membranes Filter device and collecting pit;
The water outlet of the grille well is connected with the water inlet of the oil separator by pipeline, the water outlet of the oil separator Mouth is connected with the water inlet of the electric air floating device by pipeline, the water outlet of the electric air floating device and the ozone pond Water inlet is connected by pipeline, and the water outlet in the ozone pond is connected with the water inlet of first processing pond by pipeline Logical, the water outlet of first processing pond is connected with the water inlet in the second processing pond by pipeline, the second processing The water outlet in pond is connected to the water inlet of the third processing pond by pipeline, the water outlet of the third processing pond with it is described micro- The water inlet of membrane filtration device is connected by pipeline, the water outlet of the micro-filtrate membrane filtration device and the collecting pit into The mouth of a river is connected by pipeline;
The discharge port of first charging tank and the discharge port of second charging tank pass through pipeline and described first respectively The feed inlet of retort is connected, and first processing pond is equipped with the first dosing mouth, the discharge port of first retort and institute The first dosing mouth is stated to be connected to by pipeline;
The discharge port of the third charging tank, the discharge port and the 5th charging tank of the 4th charging tank discharge port pass through respectively Pipeline is connected with the feed inlet of second retort, and the second processing pond is equipped with the second dosing mouth, second reaction The discharge port of tank is connected to second dosing mouth by pipeline;
The discharge port of 6th charging tank passes through pipeline and the third respectively with the discharge port of the 7th charging tank The feed inlet of retort is connected, and the third processing pond is equipped with third dosing mouth, the discharge port of the third retort and institute Third dosing mouth is stated to be connected to by pipeline.
It is further preferred as the utility model, it is all provided in first retort, the second retort and third retort There is agitating device.
It is further preferred as the utility model, all control valve is equipped on the pipeline.
The utility model has the beneficial effects that:The processing system of oily waste water provided by the utility model, which can be reduced effectively, to be contained The processing cost of greasy dirt, oiliness sewage treatment significant effect realize the separation of oil and water, meet national standard of drainage.
Description of the drawings
Fig. 1 is the utility model processing system structural schematic diagram.
In attached drawing, parts list represented by the reference numerals are as follows:
1, grille well, 2, oil separator, 3, electric air floating device, 4, ozone pond, the 5, first processing pond, 6, second processing pond, 7, Third processing pond, 8, micro-filtrate membrane filtration device, 9, collecting pit, the 10, first charging tank, the 11, second charging tank, the 12, first reaction Tank, the 13, second retort, 14, third charging tank, the 15, the 4th charging tank, the 16, the 5th charging tank, the 17, the 6th charging tank, 18, 7th charging tank, 19, third retort.
Specific implementation mode
The principles of the present invention and feature are described below, example is served only for explaining the utility model, and It is non-to be used to limit the scope of the utility model.
Embodiment
A kind of processing system of oily waste water as shown in Figure 1, including grille well 1, oil separator 2, electric air floating device 3, ozone Pond 4, the first processing pond 5, second processing pond 6, third processing pond 7, the first charging tank 10, the second charging tank 11, the first retort 12, third charging tank 14, the 4th charging tank 15, the 5th charging tank 16, the second retort 13, the 6th charging tank the 17, the 7th feed intake Tank 18, third retort 19, micro-filtrate membrane filtration device 8 and collecting pit 9;
The water outlet of the grille well 1 is connected with the water inlet of the oil separator 2 by pipeline, the oil separator 2 Water outlet is connected with the water inlet of the electric air floating device 3 by pipeline, the water outlet of the electric air floating device 3 with it is described smelly The water inlet in oxygen pond 4 is connected by pipeline, and the water outlet in the ozone pond 4 and the water inlet of first processing pond 5 pass through Pipeline is connected, and the water outlet of first processing pond 5 is connected with the water inlet in the second processing pond 6 by pipeline, institute The water outlet for stating second processing pond 6 is connected to the water inlet of the third processing pond 7 by pipeline, the third processing pond 7 Water outlet is connected with the water inlet of the micro-filtrate membrane filtration device 8 by pipeline, the water outlet of the micro-filtrate membrane filtration device 8 It is connected by pipeline with the water inlet of the collecting pit 9;
The discharge port of the discharge port of first charging tank 10 and second charging tank 11 respectively by pipeline with it is described The feed inlet of first retort 12 is connected, and first processing pond 5 is equipped with the first dosing mouth, and first retort 12 goes out Material mouth is connected to first dosing mouth by pipeline, the iron in sodium peroxydisulfate and the second charging tank 11 in the first charging tank 10 Powder is mixed in the first retort 12, and the mixture obtained after mixing is added in the first processing pond 5 and is carried out to containing waste water Processing;
The discharge port of the discharge port of the third charging tank 14, the discharge port and the 5th charging tank 16 of the 4th charging tank 15 It is connected respectively with the feed inlet of second retort 13 by pipeline, the second processing pond 6 is equipped with the second dosing mouth, institute The discharge port for stating the second retort 13 is connected to second dosing mouth by pipeline, siloxanes in third charging tank 14, The chain extender in polyglycol ether and the 5th charging tank 16 in four charging tanks 15, addition, which has in the second retort 13, is reacted Mixing, wherein storage has propylene glycol in advance in the second retort 13, the product direct emission that the second retort 13 obtains is in second In processing pond 6;
The discharge port of 6th charging tank 17 and the discharge port of the 7th charging tank 18 respectively by pipeline with it is described The feed inlet of third retort 19 is connected, and the third processing pond 7 is equipped with third dosing mouth, and the third retort 19 goes out Material mouth is connected to the third dosing mouth by pipeline, the poly- second in chitosan and the 7th charging tank 18 in the 6th charging tank 17 Glycol is added in third retort 19, and product obtained by the reaction is added in third processing pond 7;First retort 12, second It is equipped with agitating device in retort 13 and third retort 19;All control valve is equipped on the pipeline.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all in this practicality Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model Within the scope of shield.

Claims (3)

1. a kind of processing system of oily waste water, which is characterized in that including grille well (1), oil separator (2), electric air floating device (3), ozone pond (4), the first processing pond (5), second processing pond (6), third processing pond (7), the first charging tank (10), second are thrown Batch can (11), the first retort (12), third charging tank (14), the 4th charging tank (15), the 5th charging tank (16), the second reaction Tank (13), the 6th charging tank (17), the 7th charging tank (18), third retort (19), micro-filtrate membrane filtration device (8) and collecting pit (9);
The water outlet of the grille well (1) is connected with the water inlet of the oil separator (2) by pipeline, the oil separator (2) Water outlet be connected by pipeline with the water inlet of the electric air floating device (3), the water outlet of the electric air floating device (3) with The water inlet of the ozone pond (4) is connected by pipeline, the water outlet of the ozone pond (4) and first processing pond (5) Water inlet be connected by pipeline, the water inlet of the water outlet of first processing pond (5) and the second processing pond (6) is logical Piping is connected, and the water outlet of the second processing pond (6) and the water inlet of the third processing pond (7) are connected by pipeline Logical, the water outlet of the third processing pond (7) is connected with the water inlet of the micro-filtrate membrane filtration device (8) by pipeline, institute The water outlet for stating micro-filtrate membrane filtration device (8) is connected with the water inlet of the collecting pit (9) by pipeline;
The discharge port of the discharge port of first charging tank (10) and second charging tank (11) respectively by pipeline with it is described The feed inlet of first retort (12) is connected, and first processing pond (5) is equipped with the first dosing mouth, first retort (12) discharge port is connected to first dosing mouth by pipeline;
The discharge port of the discharge port of the third charging tank (14), the discharge port and the 5th charging tank (16) of the 4th charging tank (15) It is connected respectively with the feed inlet of second retort (13) by pipeline, the second processing pond (6) is equipped with the second dosing Mouthful, the discharge port of second retort (13) is connected to second dosing mouth by pipeline;
The discharge port of 6th charging tank (17) and the discharge port of the 7th charging tank (18) respectively by pipeline with it is described The feed inlet of third retort (19) is connected, and the third processing pond (7) is equipped with third dosing mouth, the third retort (19) discharge port is connected to the third dosing mouth by pipeline.
2. the processing system of oily waste water according to claim 1, which is characterized in that first retort (12), second It is equipped with agitating device in retort (13) and third retort (19).
3. the processing system of oily waste water according to claim 1, which is characterized in that be all equipped with adjusting on the pipeline Valve.
CN201721502762.7U 2017-11-08 2017-11-08 A kind of processing system of oily waste water Active CN207632644U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721502762.7U CN207632644U (en) 2017-11-08 2017-11-08 A kind of processing system of oily waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721502762.7U CN207632644U (en) 2017-11-08 2017-11-08 A kind of processing system of oily waste water

Publications (1)

Publication Number Publication Date
CN207632644U true CN207632644U (en) 2018-07-20

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107792972A (en) * 2017-11-08 2018-03-13 重庆耐德水处理科技有限公司 The handling process and processing system of a kind of oily waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107792972A (en) * 2017-11-08 2018-03-13 重庆耐德水处理科技有限公司 The handling process and processing system of a kind of oily waste water
CN107792972B (en) * 2017-11-08 2023-05-26 重庆耐德水处理科技有限公司 Treatment process and treatment system for oily wastewater

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CP01 Change in the name or title of a patent holder

Address after: 401121 No. 6 Yangliu Road, North Yubei District, Chongqing

Patentee after: Chongqing Neide Environmental Technology Co., Ltd.

Address before: 401121 No. 6 Yangliu Road, North Yubei District, Chongqing

Patentee before: Chongqing Snyder Water Treatment Technology Co. Ltd.

CP01 Change in the name or title of a patent holder