CN203095754U - Emulsion treatment device - Google Patents

Emulsion treatment device Download PDF

Info

Publication number
CN203095754U
CN203095754U CN 201320045521 CN201320045521U CN203095754U CN 203095754 U CN203095754 U CN 203095754U CN 201320045521 CN201320045521 CN 201320045521 CN 201320045521 U CN201320045521 U CN 201320045521U CN 203095754 U CN203095754 U CN 203095754U
Authority
CN
China
Prior art keywords
emulsion
air flotation
tank
outlet
flotation slot
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.)
Expired - Fee Related
Application number
CN 201320045521
Other languages
Chinese (zh)
Inventor
李根芹
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.)
Henan Tianchen Environ Metal Protection Science & Technology Co Ltd
Original Assignee
Henan Tianchen Environ Metal Protection Science & 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 Henan Tianchen Environ Metal Protection Science & Technology Co Ltd filed Critical Henan Tianchen Environ Metal Protection Science & Technology Co Ltd
Priority to CN 201320045521 priority Critical patent/CN203095754U/en
Application granted granted Critical
Publication of CN203095754U publication Critical patent/CN203095754U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Water Treatment By Sorption (AREA)

Abstract

The utility model discloses an emulsion treatment device which comprises a reaction tank, wherein a waste liquid inlet of the reaction tank is connected with a waste liquid storage tank; a demulsifier storage tank and a coagulant storage tank are connected to a reagent inlet of the reaction tank; a first air floatation tank is connected to the outlet of the reaction tank; a solid outlet of the first air floatation tank is connected with a pressure filter; a liquid outlet of the first air floatation tank is connected with a second air floatation tank; a solid outlet of the second air floatation tank is connected with the pressure filter; and an air outlet of the second air flotation tank is connected with an activated carbon canister structure. According to the emulsion treatment device, an emulsion is pretreated by using a demulsifier and a coagulant, so that oil molecules in the emulsifier are uniformly distributed in the emulsifier; the emulsion is then treated by using an air floatation method, so that the emulsion is subjected to solid-liquid separation; and finally, the emulsion is subjected to adsorption treatment by using activated carbon, and therefore the treated product accords with the emission requirement. The whole emulsion treatment device is relatively simple in structure and very convenient to operate.

Description

A kind of emulsion treatment unit
Technical field
The utility model relates to a kind of emulsion treatment unit that is used to handle emulsion.
Background technology
Emulsion is generally all to be oily(waste)water, and a lot of manufacturing enterprises all can produce emulsifying liquid waste water, and these emulsions have very big influence to environment, so need deal carefully with.The character of emulsion is generally all very stable, is difficult to obtain the ideal treatment effect with general physics and biochemical method, and the water outlet oleaginousness is 800~1000mg/L usually, does not reach the requirement of environment protection emission.
Existing emulsion treatment process has gravitational separation process, granulating method, Depth Filtration method and ultra-filtration membrane partition method.The clearance of gravitational separation process, granulating method is lower, and water outlet oleaginousness height can only be as the pre-treatment of oily(waste)water; The ultra-filtration membrane partition method has the efficient of removal height, the advantage that water outlet is effective, but structure more complicated, and operating procedure is loaded down with trivial details.
The utility model content
The purpose of this utility model provides a kind of simple in structure, easy to operate emulsion treatment unit.
In order to realize above purpose, the utility model adopts following technical scheme: a kind of emulsion treatment unit, comprise retort, the waste liquid import of retort links to each other with the waste liquid storage tank, be connected with emulsion splitter storage tank and coagulating agent storage tank in the reagent import of retort, be connected with first air flotation slot in the outlet of retort, the solid outlet of first air flotation slot links to each other with pressure filter, the liquid exit of first air flotation slot links to each other with second air flotation slot, the solid outlet of second air flotation slot links to each other with described pressure filter, and the air outlet of second air flotation slot links to each other with the charcoal canister structure.
Described activated carbon canister structure is made up of placed in-line first charcoal canister and second charcoal canister, and the import of first charcoal canister links to each other with the air outlet of second air flotation slot.
All be disposed with switch-valve and force (forcing) pump between described retort and waste liquid storage tank, emulsion splitter storage tank and the coagulating agent storage tank.
Be disposed with switch-valve and force (forcing) pump between the described retort and first air flotation slot.
Be disposed with switch-valve and force (forcing) pump between described first air flotation slot and second air flotation slot.
Be disposed with switch-valve and force (forcing) pump between described second air flotation slot and the charcoal canister structure.
Of the present utility modelly want emulsion to be carried out pre-treatment by emulsion splitter and coagulating agent, make the oil molecule in the emulsifying agent in emulsifying agent, be evenly distributed, by the air supporting method emulsifying agent is handled then, make the solid-liquid separation of emulsifying agent, handle by charcoal absorption at last, make the product after handling meet emission request, whole apparatus structure is simple relatively, operates also very convenient.
Description of drawings
Fig. 1 is the one-piece construction synoptic diagram of the utility model embodiment.
Embodiment
A kind of embodiment of emulsion treatment unit, in Fig. 1, the waste liquid import of its retort 1 links to each other with waste liquid storage tank 2, be connected with emulsion splitter storage tank 3 and coagulating agent storage tank 4 in the reagent import of retort 1, the outlet of emulsion splitter storage tank 3 links to each other with the reagent import of retort 1 by behind switch-valve and the force (forcing) pump.The outlet of coagulating agent storage tank 4 also links to each other with the reagent import of retort 1 by behind switch-valve and the force (forcing) pump.Be connected with first air flotation slot 5 in the outlet of retort 1, the solid outlet of first air flotation slot 5 links to each other with pressure filter 7 by behind the switch-valve, the liquid exit of first air flotation slot 5 links to each other with second air flotation slot 6 by behind switch-valve and the force (forcing) pump, the solid outlet of second air flotation slot 6 links to each other with pressure filter 7 by switch-valve, the air outlet of second air flotation slot 6 links to each other with first charcoal canister 8 with force (forcing) pump by switch-valve, and first charcoal canister 8 links to each other with second charcoal canister 9 by switch-valve.
All be provided with force (forcing) pump in the present embodiment between each storage tank and the retort, also can force (forcing) pump be set, utilize difference of altitude to realize flow of matter between each tank body by gravity.
Charcoal canister structure in the present embodiment is in series by two charcoal canisters, also can be in series by three or more charcoal canisters.

Claims (6)

1. emulsion treatment unit, it is characterized in that: comprise retort, the waste liquid import of retort links to each other with the waste liquid storage tank, be connected with emulsion splitter storage tank and coagulating agent storage tank in the reagent import of retort, be connected with first air flotation slot in the outlet of retort, the solid outlet of first air flotation slot links to each other with pressure filter, the liquid exit of first air flotation slot links to each other with second air flotation slot, the solid outlet of second air flotation slot links to each other with described pressure filter, and the air outlet of second air flotation slot links to each other with the charcoal canister structure.
2. emulsion treatment unit according to claim 1 is characterized in that: described activated carbon canister structure is made up of placed in-line first charcoal canister and second charcoal canister, and the import of first charcoal canister links to each other with the air outlet of second air flotation slot.
3. emulsion treatment unit according to claim 1 and 2 is characterized in that: all be disposed with switch-valve and force (forcing) pump between described retort and waste liquid storage tank, emulsion splitter storage tank and the coagulating agent storage tank.
4. emulsion treatment unit according to claim 1 is characterized in that: be disposed with switch-valve and force (forcing) pump between the described retort and first air flotation slot.
5. emulsion treatment unit according to claim 1 is characterized in that: be disposed with switch-valve and force (forcing) pump between described first air flotation slot and second air flotation slot.
6. emulsion treatment unit according to claim 1 is characterized in that: be disposed with switch-valve and force (forcing) pump between described second air flotation slot and the charcoal canister structure.
CN 201320045521 2013-01-28 2013-01-28 Emulsion treatment device Expired - Fee Related CN203095754U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320045521 CN203095754U (en) 2013-01-28 2013-01-28 Emulsion treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320045521 CN203095754U (en) 2013-01-28 2013-01-28 Emulsion treatment device

Publications (1)

Publication Number Publication Date
CN203095754U true CN203095754U (en) 2013-07-31

Family

ID=48847173

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320045521 Expired - Fee Related CN203095754U (en) 2013-01-28 2013-01-28 Emulsion treatment device

Country Status (1)

Country Link
CN (1) CN203095754U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103979728A (en) * 2014-05-26 2014-08-13 安泰科技股份有限公司 Treatment device and treatment process for waste emulsion
CN105924135A (en) * 2016-04-28 2016-09-07 河南天辰环保科技股份有限公司 Sintered brick

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103979728A (en) * 2014-05-26 2014-08-13 安泰科技股份有限公司 Treatment device and treatment process for waste emulsion
CN103979728B (en) * 2014-05-26 2015-09-23 安泰科技股份有限公司 The treatment unit of waste emulsified mixture and treatment process
CN105924135A (en) * 2016-04-28 2016-09-07 河南天辰环保科技股份有限公司 Sintered brick
CN105924135B (en) * 2016-04-28 2018-10-02 河南中环信环保科技股份有限公司 A kind of fired brick

Similar Documents

Publication Publication Date Title
CN101880071B (en) Continuous high ammonia-nitrogen tail water deep treatment system and treatment method
MY169753A (en) Method for treating a waste stream using a bioreactor and a membrane filter
CN203095754U (en) Emulsion treatment device
RU2008137783A (en) WASTE WATER TREATMENT METHOD
CN103736319B (en) A kind of break milk separation water treatment system and method
CN112876036A (en) Ultrasonic-based oily sludge treatment system and process
CN205275333U (en) Oil field extraction water composite treatment system
CN104355439A (en) Oilfield sewage treatment device
CN203683272U (en) Treatment device for waste drilling fluid
CN204637922U (en) A kind of cold analysis still device for recovering tail gas
CN205295111U (en) Crude oil pipeline fatlute preliminary treatment ware
CN204138463U (en) A kind of drilling mud Waste Water Treatment
CN204865554U (en) Portable filter equipment
CN204778924U (en) Active carbon filter equipment
CN203648249U (en) Fire-resistant oil regeneration tank
CN103316892A (en) Kitchen garbage recycling method and device thereof
CN204454756U (en) A kind of waste disposal plant
CN204022512U (en) A kind of reverse osmosis wastewater treatment equipment efficiently
CN202829636U (en) Device for processing reverse osmosis concentrated brine by using decompressing membrane distillation
CN208561957U (en) A kind of system that COD being removed in depth from nickel cobalt raffinate
CN202988792U (en) Sodium methoxide wastewater treatment device
CN104016496B (en) Water treatment device for absorbing and separating low concentration metal ion and organic small molecular pollutant
CN204550340U (en) A kind of novel oilfield fracturing liquid wastewater treatment equipment
CN204569632U (en) A kind of new device being applicable to emulsifying liquid waste water and being separated
CN105457339B (en) Oil-water separation method and device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130731

Termination date: 20150128

EXPY Termination of patent right or utility model