CN106630302A - Emulsion treatment equipment - Google Patents

Emulsion treatment equipment Download PDF

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Publication number
CN106630302A
CN106630302A CN201710070825.4A CN201710070825A CN106630302A CN 106630302 A CN106630302 A CN 106630302A CN 201710070825 A CN201710070825 A CN 201710070825A CN 106630302 A CN106630302 A CN 106630302A
Authority
CN
China
Prior art keywords
tank
water inlet
reaction tank
delivery port
processing equipment
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201710070825.4A
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Chinese (zh)
Inventor
蒋伟
刁永辉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Yongyi Environmental Protection Technology Co Ltd
Original Assignee
Jiangsu Yongyi Environmental Protection Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiangsu Yongyi Environmental Protection Technology Co Ltd filed Critical Jiangsu Yongyi Environmental Protection Technology Co Ltd
Priority to CN201710070825.4A priority Critical patent/CN106630302A/en
Publication of CN106630302A publication Critical patent/CN106630302A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/005Processes using a programmable logic controller [PLC]

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention discloses emulsion treatment equipment. The equipment comprises a tank body, a chemical reagent adding tank, a reaction tank and a clean water tank, wherein a waste water inlet and a chemical reagent adding opening are formed in the upper part of the chemical reagent adding tank; the chemical reagent adding opening is externally connected with a flocculating agent box; a residue separating basket is arranged at the upper part of the chemical reagent adding tank and positioned below the waste water inlet; a mixing tank and a residue scraper are arranged in the reaction tank; the mixing tank is provided with a water inlet, a dissolved air water inlet and a water outlet; the dissolved air water inlet of the mixing tank is externally connected with a dissolved air tank through a dissolved air water release pipe; a residue collecting tank is arranged below one end of the residue scraper; an oil baffle plate is arranged at the bottom of the reaction tank; a water outlet is formed in the lower part of the clean water tank. The equipment is skillful in design and simple in structure, has the waste water treatment efficiency higher than that in the national regulated discharge standard, and is low in manufacture cost, reduces the operation cost of enterprises, and is applicable to large and small enterprises.

Description

A kind of emulsion processing equipment
Technical field
The invention belongs to technical field of waste water processing, more particularly to a kind of emulsion processing equipment.
Background technology
Emulsion is a kind of high performance semi-synthetic metal working fluid, in machine-building and processing industry, the cutting of metal With grinding a large amount of emulsions need to be used to be used as lubrication, machine oil and surfactant are mainly contained in emulsion, be to use As needed dilute with water adds what emulsifying agent was formulated to oil emulsion.
Emulsion through multiple Reusability and with air contact after, it may occur that it is different degrees of become sour, rot etc. become Matter phenomenon, performance is reduced, and to regularly replace new emulsion, causes to generate substantial amounts of waste emulsified mixture.Contain in waste emulsified mixture High concentration oil, high-enriched organics, and a large amount of metallic particles are incorporated in metal cutting process, containing metallic particles pollution Thing, arbitrarily discharge can cause serious environmental pollution, it is therefore necessary to carry out effectively processing the discharge restriction for reaching public sewage Require.
At present, for the processing method of waste emulsified mixture mainly has Physical and microbial method.Physical common are ultrafiltration Method, is a kind of membrane separation technique, and it is much like with counter-infiltration, also with UF membrane of the pellicle using pressure differential as motive force Process, by selective film, the particulate of the different molecular weight in solution is separated, under pressure medium, less than hole The particulate in footpath, through the micropore on film, is trapped with solvent more than the particulate in aperture.The size and shape of micropore is determined on film The separating property of film is determined.The particulate being trapped can not form filter cake, be still retained in filtrate with cytosolic form.But useless breast Change the high concentration oil that contains in liquid and easily cause film blocking, reduce the service life of film, and it is higher to change the cost of membrane module, The operation cost of enterprise can be increased;Microbial method is, by the suitable bacteria culture of culture, to realize the degraded and decomposition of emulsion, But do not allow easily biological-degradable, therefore the process of waste emulsified mixture to be difficult to reach discharge mark containing high-enriched organics in emulsion It is accurate.
The content of the invention
The invention mainly solves the technical problem of a kind of emulsion processing equipment is provided, equipment deft design, the structure Simplify, waste water treatment efficiency is higher than state emission standard, device fabrication low cost reduces the operation cost of enterprise, is suitable for Use in large and small type enterprise.
To solve above-mentioned technical problem, one aspect of the present invention is:A kind of emulsion processing equipment is provided, Including the second partition of first dividing plate and longitudinal direction in cell body, the cell body with longitudinal direction, first dividing plate and described second The cell body is isolated into dividing plate dosing pond, reaction tank and the clear water reserviors arranged successively along flow direction;
The top in the dosing pond has waste water inlet and a dosing mouth, the external flocculant medicine-chest of the dosing mouth, it is described plus The top in medicine pond and have every slag basket positioned at the lower section of waste water inlet, the delivery port in the dosing pond is located at bottom;
There is mixing pit and Slag Scraping Device, the mixing pit is located at the bottom of the reaction tank, described to scrape in the reaction tank Slag machine is located at the top of the reaction tank;The mixing pit has water inlet, dissolved air water import and delivery port, the mixing pit Water inlet is connected with the delivery port in the dosing pond, and the dissolved air water import of the mixing pit is by the external molten gas of dissolved air water release pipe Tank, the delivery port of the mixing pit is communicated with the reaction tank;Dreg collecting slot is provided with below one end of the Slag Scraping Device, it is described to scrape Slag machine scrapes slag by the reaction tank towards the dreg collecting slot;The delivery port of the reaction tank be located at the second partition bottom and Connect with the clear water reserviors;The bottom of the reaction tank is provided with oil baffle, and the oil baffle is located at the second partition and described Between mixing pit;
The bottom of the clear water reserviors has delivery port.
Further say, the bottom of the clear water reserviors has circulation port, and the dissolving has water inlet and air inlet, institute The water inlet for stating dissolving is connected by circulation pipe with the circulation port of the clear water reserviors, and the circulation pipe is provided with reflux pump, institute State the external high-pressure air source of air inlet of dissolving.
Further say, be additionally provided with sandfiltration pot and carbon filtration tank, the delivery port of the clear water reserviors connects the sand by pipeline The water inlet of filter tank, the delivery port of the sandfiltration pot connects the water inlet of the carbon filtration tank by pipeline, and connects the clear water On the pipeline of pond and the sandfiltration pot or connect the pipeline of the sandfiltration pot and the carbon filtration tank and be provided with suction pump.
Further say, be provided with PLC, the Slag Scraping Device, the magnetic valve of the flocculant medicine-chest, the dissolving Magnetic valve, the reflux pump and the suction pump all electrically connect with PLC respectively.
Further say, the height of the oil baffle is 55-65cm.
Further say that there is interval, the interval structure between the bottom surface of the lower end of the second partition and the cell body Into the delivery port of the reaction tank, the height at the interval is 10-15cm.
Further say, floating ball lever meter, the floating ball lever meter and PLC electricity are provided with the clear water reserviors Connection.
Further say, the dreg collecting slot is located at the top of the clear water reserviors.
Further say, the Slag Scraping Device is chain type Slag Scraping Device, the chain type Slag Scraping Device includes motor, linked transmission Mechanism and scum board, the chain type transmission mechanism is connected with the motor, and the scum board is fixed on the linked transmission Mechanism, the scum board is moved under chain type transmission mechanism drive, and the motor is electrically connected with the PLC Connect.
Further say, the medicament added in the flocculant medicine-chest is PAM (polyacrylamide), and the flocculant medicine Case is provided with rabbling mechanism.
Beneficial effects of the present invention at least have it is following some:
First, the flocculant that the present invention is added can form larger with the macromolecular particle in waste emulsified mixture or small molecule particle Flocculate, while in dissolving dissolved air water decompression release after micro-bubble is formed in water body, due to the density of flocculate It is less than hydrone, so can float to form scum layer after micro-bubble adhesion flocculate, and scraped to dreg collecting slot by Slag Scraping Device, so as to The polluter in water is rapidly removed, the purpose of water purification is reached;In addition the oil baffle that the present invention is provided with can stop with water (flow) direction The part grease of flowing so as to float up to the top in central reaction pond, and scraped by Slag Scraping Device, it is to avoid part not with flocculant The grease for forming flocculate enters clear water reserviors;
2nd, the present invention is additionally provided with sandfiltration pot and carbon filtration tank, and the water body in clear water reserviors can further remove water through sandfiltration pot Silt and metal ion in body etc., the activated carbon filled in carbon filtration tank can other impurities and ozone in adsorbed water body, it is and right Pigment in water body is adsorbed, it is ensured that to the treatment effect of waste emulsified mixture be higher than state emission standard;
3rd, the water part in clear water reserviors is introduced into pressure air-dissolving in dissolving by the reflux pump that the present invention is provided with, after decompression Mixing pit is directly entered, using partial reflux method of pressed dissolved-air release, the water yield of pressurization is few, can save the power consumption of equipment, And do not promote emulsification, treatment effect to be better than full method of pressed dissolved-air release during air supporting;
4th, the interval with 10-15cm between second partition of the present invention and the bottom surface of cell body, and the height being spaced is less than clear The minimum liquid level face in pond, the purpose of the design is, due to the density of the density ratio water of grease it is big, therefore ought not by gear oil When the grease that plate stops flows through second partition, macromolecular grease can be accumulated in the lower end of second partition, so as to float simultaneously Scraped by Slag Scraping Device, the water body that inflow clear water reserviors are effectively ensured does not contain grease;
5th, using PLC to whole equipment whole-process control and monitoring, automation intensity is high, reduces artificial for the present invention Workload, can effectively improve the purified treatment efficiency of equipment;And PLC carries hardware fault self-monitoring function, breaks down When can send a warning in time, it is ensured that the equipment reliability of operation.
Description of the drawings
Fig. 1 is the structural representation of the present invention;
The mark of each part is as follows in accompanying drawing:
Cell body 1, the first dividing plate 2, second partition 3, dosing pond 4, reaction tank 5, clear water reserviors 6, flocculant medicine-chest 7, every slag basket 8th, mixing pit 9, Slag Scraping Device 10, dissolving 11, dreg collecting slot 12, oil baffle 13, reflux pump 14, sandfiltration pot 15, carbon filtration tank 16, draw water Pump 17, floating ball lever meter 18, waste water inlet 41, dosing mouth 42, delivery port 61, circulation port 62 and scum board 101.
Specific embodiment
Presently preferred embodiments of the present invention is described in detail below in conjunction with the accompanying drawings, so that advantages and features of the invention energy It is easier to be readily appreciated by one skilled in the art, apparent clearly defines so as to make to protection scope of the present invention.
Embodiment:A kind of emulsion processing equipment, as shown in figure 1, the present invention includes having in cell body 1, the cell body 1 indulging To the first dividing plate 2 and longitudinal direction second partition 3, first dividing plate 2 and the second partition 3 are isolated into the cell body 1 Dosing pond 4, reaction tank 5 and the clear water reserviors 6 arranged successively along flow direction;
The top in the dosing pond 4 has waste water inlet 41 and dosing mouth 42, the external flocculant medicine-chest of the dosing mouth 42 7, the top in the dosing pond 4 and positioned at the lower section of waste water inlet 41 have every slag basket 8, the delivery port in the dosing pond 4 is located at Bottom;
There is mixing pit 9 and Slag Scraping Device 10, the mixing pit 9 is located at the bottom of the reaction tank 5 in the reaction tank 5, The Slag Scraping Device 10 is located at the top of the reaction tank 5;The mixing pit 9 has water inlet, dissolved air water import and delivery port, institute The water inlet for stating mixing pit 9 is connected with the delivery port in the dosing pond 4, and the dissolved air water import of the mixing pit 9 passes through dissolved air water The external dissolving 11 of release pipe, the delivery port of the mixing pit 9 is communicated with the reaction tank 5;One end of the Slag Scraping Device 10 Lower section is provided with dreg collecting slot 12, and the Slag Scraping Device 10 scrapes slag by the reaction tank 5 towards the dreg collecting slot 12;The reaction tank 5 Delivery port is located at the bottom of the second partition 3 and connects with the clear water reserviors 6;The bottom of the reaction tank 5 is provided with oil baffle 13, the oil baffle 13 is located between the second partition 3 and the mixing pit 9;
The bottom of the clear water reserviors 6 has delivery port 61.
The bottom of the clear water reserviors 6 has circulation port 62, and the dissolving 11 has water inlet and air inlet, the molten gas The water inlet of tank 11 is connected by circulation pipe with the circulation port 62 of the clear water reserviors, and the circulation pipe is provided with reflux pump 14, institute State the external high-pressure air source of air inlet of dissolving 11.
Sandfiltration pot 15 and carbon filtration tank 16 are additionally provided with, the delivery port of the clear water reserviors 6 connects the sandfiltration pot 15 by pipeline Water inlet, the delivery port of the sandfiltration pot 15 connects the water inlet of the carbon filtration tank 16 by pipeline, and connects the clear water The pipeline of pond 6 and the sandfiltration pot 15 is provided with suction pump 17.
It is provided with PLC, the Slag Scraping Device 10, the magnetic valve of the flocculant medicine-chest 7, the electromagnetism of the dissolving 11 Valve, the reflux pump 14 and the suction pump 17 are all electrically connected with PLC respectively.
The height of the oil baffle 13 is 55-65cm.
There is interval, the interval constitutes the reaction between the bottom surface of the lower end of the second partition 3 and the cell body 1 The delivery port in pond 5, the height at the interval is 10-15cm.
Floating ball lever meter 18 is provided with the clear water reserviors 6, the floating ball lever meter 18 is electrically connected with the PLC. The minimum liquid level of the floating ball lever meter is 25-35cm.
The dreg collecting slot 12 is located at the top of the clear water reserviors 6.
The Slag Scraping Device 10 is chain type Slag Scraping Device, and the chain type Slag Scraping Device includes motor, chain type transmission mechanism and scrapes Slag plate 101, the chain type transmission mechanism is connected with the motor, and the scum board 101 is fixed on the linked transmission machine Structure, the scum board 101 is moved under chain type transmission mechanism drive, and the motor is electrically connected with the PLC Connect.
The medicament added in the flocculant medicine-chest 7 is PAM, and the flocculant medicine-chest 7 is provided with rabbling mechanism.
The operation principle of the present invention is as follows:When waste emulsified mixture is from waste water inlet into cell body, first passes through and blocked automatically every slag basket Debris and bulky grain waste residue variously-shaped in emulsifying liquid waste water are cut and removed, and is entered in reaction tank by pipeline, enter anti- The waste emulsified mixture of Ying Chizhong contains PAM flocculants, and PAM flocculants form larger flocculate with the particulate matter in water body, while The dissolved air water that discharges in dissolving forms micro-bubble, floats after micro-bubble adhesion flocculate and forms scum layer and by scraping slag Machine is scraped, in addition, the grease in waste emulsified mixture is stopped by oil baffle, floated, is equally scraped by Slag Scraping Device;After purifying again Water body enters clear water reserviors by the bottom of second partition, because the minimum liquid level face in clear water reserviors is higher than second partition and cell body bottom Distance between the two, therefore the small molecule grease in water body can be suspended in the lower end of second partition, be accumulated into macromolecular oil Float after shape thing, scraped by Slag Scraping Device;When the liquid level in clear water reserviors is higher than 25-30cm, the suction pump in clear water reserviors exit is opened It is dynamic, pull water out and respectively enter and discharge after sandfiltration pot and the purification of carbon filtration tank;In addition, the water in clear water reserviors some pass through back Stream pump enters dissolving, and forms dissolved air water with into the compressed air in dissolving, can be recycled.
Embodiments of the invention are the foregoing is only, the scope of the claims of the present invention is not thereby limited, it is every using this The equivalent structure transformation that bright specification and accompanying drawing content are made, or other related technical fields are directly or indirectly used in, It is included within the scope of the present invention in the same manner.

Claims (10)

1. a kind of emulsion processing equipment, it is characterised in that:Including cell body, the cell body is interior to be had the first dividing plate of longitudinal direction and indulges To second partition, first dividing plate and the second partition by the cell body be isolated into it is arranging successively along flow direction plus Medicine pond, reaction tank and clear water reserviors;
The top in the dosing pond has waste water inlet and a dosing mouth, the external flocculant medicine-chest of the dosing mouth, the dosing pond Top and have every slag basket positioned at the lower section of waste water inlet, the delivery port in the dosing pond is located at bottom;
There is mixing pit and Slag Scraping Device, the mixing pit is located at the bottom of the reaction tank, the Slag Scraping Device in the reaction tank Positioned at the top of the reaction tank;The mixing pit has water inlet, dissolved air water import and delivery port, the water inlet of the mixing pit Mouth is connected with the delivery port in the dosing pond, and the dissolved air water import of the mixing pit manages external dissolving by dissolved air water release, The delivery port of the mixing pit is communicated with the reaction tank;Dreg collecting slot is provided with below one end of the Slag Scraping Device, it is described to scrape slag Machine scrapes slag by the reaction tank towards the dreg collecting slot;The delivery port of the reaction tank be located at the second partition bottom and with The clear water reserviors connection;The bottom of the reaction tank is provided with oil baffle, and the oil baffle is located at the second partition and described mixed Close between pond;
The bottom of the clear water reserviors has delivery port.
2. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The bottom of the clear water reserviors has to be followed Collar extension, the dissolving has water inlet and air inlet, and the water inlet of the dissolving is by circulation pipe and the clear water reserviors Circulation port connects, and the circulation pipe is provided with reflux pump, the external high-pressure air source of air inlet of the dissolving.
3. a kind of emulsion processing equipment according to claim 1, it is characterised in that:Sandfiltration pot and carbon filtration tank are additionally provided with, The delivery port of the clear water reserviors connects the water inlet of the sandfiltration pot by pipeline, and the delivery port of the sandfiltration pot is connected by pipeline Meet on the water inlet of the carbon filtration tank, and the pipeline of the connection clear water reserviors and the sandfiltration pot or connect the sandfiltration pot and institute The pipeline for stating carbon filtration tank is provided with suction pump.
4. a kind of emulsion processing equipment according to claim 1, it is characterised in that:PLC is provided with, it is described to scrape slag Machine, the magnetic valve of the flocculant medicine-chest, the magnetic valve of the dissolving, the reflux pump and the suction pump all respectively with PLC is electrically connected.
5. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The height of the oil baffle is 55- 65cm。
6. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The lower end of the second partition and institute State and have between the bottom surface of cell body interval, the interval constitutes the delivery port of the reaction tank, and the height at the interval is 10- 15cm。
7. a kind of emulsion processing equipment according to claim 4, it is characterised in that:Ball float liquid is provided with the clear water reserviors Position meter, the floating ball lever meter is electrically connected with the PLC.
8. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The dreg collecting slot is located at the clear water The top in pond.
9. a kind of emulsion processing equipment according to claim 4, it is characterised in that:The Slag Scraping Device scrapes slag for chain type Machine, the chain type Slag Scraping Device includes motor, chain type transmission mechanism and scum board, the chain type transmission mechanism and the driving Motor connection, the scum board is fixed on the chain type transmission mechanism, and the scum board is under chain type transmission mechanism drive Mobile, the motor is electrically connected with the PLC.
10. a kind of emulsion processing equipment according to claim 1, it is characterised in that:Add in the flocculant medicine-chest Medicament be PAM, and the flocculant medicine-chest is provided with rabbling mechanism.
CN201710070825.4A 2017-02-09 2017-02-09 Emulsion treatment equipment Pending CN106630302A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710070825.4A CN106630302A (en) 2017-02-09 2017-02-09 Emulsion treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710070825.4A CN106630302A (en) 2017-02-09 2017-02-09 Emulsion treatment equipment

Publications (1)

Publication Number Publication Date
CN106630302A true CN106630302A (en) 2017-05-10

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ID=58844623

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CN201710070825.4A Pending CN106630302A (en) 2017-02-09 2017-02-09 Emulsion treatment equipment

Country Status (1)

Country Link
CN (1) CN106630302A (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101182053A (en) * 2007-11-12 2008-05-21 中国海洋石油总公司 Backflow air-floating device for water-arrangement optimization multi-phase flow pump
CN102249370A (en) * 2011-05-16 2011-11-23 云南今业生态建设集团有限公司 High efficiency integrated processor for oily water
CN103030229A (en) * 2011-09-30 2013-04-10 宝山钢铁股份有限公司 Oily wastewater treatment device and treatment method in steel industry
CN203461894U (en) * 2013-08-07 2014-03-05 陈凤珠 Restaurant waste water purification device
CN103626325A (en) * 2012-08-22 2014-03-12 杨志江 Advanced treatment device for oil-containing waste water
CN203890166U (en) * 2014-06-05 2014-10-22 诸城市格林诺斯环保科技有限公司 Dissolved air flotation machine
CN204848347U (en) * 2015-05-31 2015-12-09 德清县同福楼食品有限公司 Take oil water separator of air supporting machine
CN106186140A (en) * 2016-08-01 2016-12-07 桐乡市致远环保科技有限公司 High-efficient vertical streaming air-flotation system and operation method thereof
CN206544953U (en) * 2017-02-09 2017-10-10 江苏永益环保科技有限公司 A kind of emulsion processing equipment

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101182053A (en) * 2007-11-12 2008-05-21 中国海洋石油总公司 Backflow air-floating device for water-arrangement optimization multi-phase flow pump
CN102249370A (en) * 2011-05-16 2011-11-23 云南今业生态建设集团有限公司 High efficiency integrated processor for oily water
CN103030229A (en) * 2011-09-30 2013-04-10 宝山钢铁股份有限公司 Oily wastewater treatment device and treatment method in steel industry
CN103626325A (en) * 2012-08-22 2014-03-12 杨志江 Advanced treatment device for oil-containing waste water
CN203461894U (en) * 2013-08-07 2014-03-05 陈凤珠 Restaurant waste water purification device
CN203890166U (en) * 2014-06-05 2014-10-22 诸城市格林诺斯环保科技有限公司 Dissolved air flotation machine
CN204848347U (en) * 2015-05-31 2015-12-09 德清县同福楼食品有限公司 Take oil water separator of air supporting machine
CN106186140A (en) * 2016-08-01 2016-12-07 桐乡市致远环保科技有限公司 High-efficient vertical streaming air-flotation system and operation method thereof
CN206544953U (en) * 2017-02-09 2017-10-10 江苏永益环保科技有限公司 A kind of emulsion processing equipment

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Application publication date: 20170510

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