CN205313256U - Modular emulsion effluent treatment plant - Google Patents
Modular emulsion effluent treatment plant Download PDFInfo
- Publication number
- CN205313256U CN205313256U CN201521132115.2U CN201521132115U CN205313256U CN 205313256 U CN205313256 U CN 205313256U CN 201521132115 U CN201521132115 U CN 201521132115U CN 205313256 U CN205313256 U CN 205313256U
- Authority
- CN
- China
- Prior art keywords
- emulsion
- breakdown
- case
- waste water
- dosing pump
- 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
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a modular emulsion effluent treatment plant. Breakdown of emulsion charge device is connected with the breakdown of emulsion case, breakdown of emulsion case, oil removal case, air supporting case connect gradually, PAC charge device, PAM charge device are connected with the air supporting case respectively. The utility model discloses a to the reasonable combination of physics, chemical treatment emulsion waste water, has replaced the traditional ceramics membrane and has handled exist in the emulsion waste water not enough, reduced the production volume of waste water, it is reliable to go out water stabilization of water quality, automated procedures are high, greatly reduced the energy consumption.
Description
Technical field:
This utility model belongs to field of waste water treatment, processes device particularly to a kind of combination type emulsifying liquid waste water.
Background technology:
Domestic current major part emulsion adopts the mode of ceramic membrane filter to process, by the centrifugation of ceramic membrane, by pressure, the moisture content in emulsion is drained into aftertreatment device process further, emulsion is back to leading portion and again concentrates, when emulsion is concentrated to finite concentration, moisture cannot separate, and the emulsion outward transport after concentration processes.
But in actual use, need ceramic membrane is carried out pickling, alkali cleaning, hot water wash after running a period of time, in the winter time in running, in addition it is also necessary to emulsion is heated, otherwise treating capacity is extremely difficult to design load, whole process equipment manufacturing cost is high, maintenance cost is big, complex operation, and cycles of concentration only has about 50%, enterprise still needs to spend most expense for processing concentrated emulsion, and enterprise causes bigger financial burden.
It is disclosed in the information of this background section and is merely intended to increase the understanding to general background of the present utility model, and be not construed as admitting or imply in any form that this information structure is for prior art that persons skilled in the art are known.
Utility model content:
The purpose of this utility model is in that to provide a kind of combination type emulsifying liquid waste water to process device, thus overcoming above-mentioned defect of the prior art.
For achieving the above object, this utility model provides
Combination type emulsifying liquid waste water processes device, including: breakdown of emulsion chemicals dosing plant, breakdown of emulsion case, oil removal case, PAC chemicals dosing plant, PAM chemicals dosing plant, air buoyancy tank; Described breakdown of emulsion chemicals dosing plant is connected with breakdown of emulsion case, and described breakdown of emulsion case, oil removal case, air buoyancy tank are sequentially connected with, and described PAC chemicals dosing plant, PAM chemicals dosing plant are connected with air buoyancy tank respectively.
Preferably, in technical scheme, breakdown of emulsion chemicals dosing plant includes dosing pump, demulsifier batch meter, and described demulsifier batch meter is connected with dosing pump, and dosing pump is connected with breakdown of emulsion case.
Preferably, in technical scheme, PAC chemicals dosing plant includes dosing pump, PAC batch meter, and described PAC batch meter is connected with dosing pump, and dosing pump is connected with air buoyancy tank.
Preferably, in technical scheme, PAM chemicals dosing plant includes dosing pump, PAM batch meter, and described PAM batch meter is connected with dosing pump, and dosing pump is connected with air buoyancy tank.
Compared with prior art, this utility model has the advantages that
Using combination type emulsifying liquid processing device to replace ceramic membrane, system investments is little, outer handling of entrusting is low, and the treating capacity of waste oil is about the 1/10 of pottery film processing system;Without operation bidirectional personnel, only need to regularly add medicament; The oil concentration separating water can be controlled in below 10 mg/litre.
Accompanying drawing illustrates:
Fig. 1 is this utility model structural representation;
Main Reference Numerals illustrates:
1-breakdown of emulsion chemicals dosing plant, 2-breakdown of emulsion case, 3-oil removal case, 4-PAC chemicals dosing plant, 5-PAM chemicals dosing plant, 6-air buoyancy tank, 10-dosing pump, 11-demulsifier batch meter, 40-dosing pump, 41-PAC batch meter, 50-dosing pump, 51-PAM batch meter.
Detailed description of the invention:
Below detailed description of the invention of the present utility model is described in detail, it is to be understood that protection domain of the present utility model is not by the restriction of detailed description of the invention.
Explicitly indicate that unless otherwise other, otherwise in entire disclosure and claims, term " includes " or its conversion will be understood to comprise the element or ingredient stated at such as " comprising " or " including " etc., and does not get rid of other element or other ingredient.
As it is shown in figure 1, combination type emulsifying liquid waste water processes device, including: breakdown of emulsion chemicals dosing plant 1, breakdown of emulsion case 2, oil removal case 3, PAC chemicals dosing plant 4, PAM chemicals dosing plant 5, air buoyancy tank 6, described breakdown of emulsion chemicals dosing plant has two sets, described breakdown of emulsion chemicals dosing plant 1 includes dosing pump 10, demulsifier batch meter 11, described demulsifier batch meter 11 is connected with dosing pump 10, dosing pump 10 is connected with breakdown of emulsion case 2, described breakdown of emulsion case 2, oil removal case 3, air buoyancy tank 6 is sequentially connected with, described PAC chemicals dosing plant 4 includes dosing pump 40, PAC batch meter 41, described PAC batch meter 41 is connected with dosing pump 40, dosing pump 40 is connected with air buoyancy tank 6, described PAM chemicals dosing plant 5 includes dosing pump 50, PAM batch meter 51, described PAM batch meter 51 is connected with dosing pump 50, dosing pump 50 is connected with air buoyancy tank 6.
Emulsifying liquid waste water is thoroughly processed by physicochemical method. System and the linkage of emulsion elevator pump, when emulsion elevator pump works, demulsifier is added from trend breakdown of emulsion case 2, after agitated reaction, enter oil removal case 3, major part oily substance is got rid of, water outlet is again from flowing into air buoyancy tank 6, by adding PAC, PAM flocculant, making the proportion oil content less than 1 get rid of with the form of little molecular suspension thing, water outlet enters back into aftertreatment device and processes.
The aforementioned description to specific illustrative embodiment of the present utility model illustrates that and the purpose of illustration. These describe and are not wishing to be defined to this utility model disclosed precise forms, and it will be apparent that according to above-mentioned instruction, it is possible to carry out much changing and change. Purpose exemplary embodiment selected and describe is in that to explain certain principles of the present utility model and practical application thereof, so that those skilled in the art is capable of and utilizes various different exemplary of the present utility model and various different selection and change. Scope of the present utility model is intended to be limited by claims and equivalents thereof.
Claims (4)
1. combination type emulsifying liquid waste water processes device, it is characterised in that: including: breakdown of emulsion chemicals dosing plant, breakdown of emulsion case, oil removal case, PAC chemicals dosing plant, PAM chemicals dosing plant, air buoyancy tank; Described breakdown of emulsion chemicals dosing plant is connected with breakdown of emulsion case, and described breakdown of emulsion case, oil removal case, air buoyancy tank are sequentially connected with, and described PAC chemicals dosing plant, PAM chemicals dosing plant are connected with air buoyancy tank respectively.
2. combination type emulsifying liquid waste water according to claim 1 processes device, it is characterised in that: described breakdown of emulsion chemicals dosing plant includes dosing pump, demulsifier batch meter, and described demulsifier batch meter is connected with dosing pump, and dosing pump is connected with breakdown of emulsion case.
3. combination type emulsifying liquid waste water according to claim 1 processes device, it is characterised in that: described PAC chemicals dosing plant includes dosing pump, PAC batch meter, and described PAC batch meter is connected with dosing pump, and dosing pump is connected with air buoyancy tank.
4. combination type emulsifying liquid waste water according to claim 1 processes device, it is characterised in that: described PAM chemicals dosing plant includes dosing pump, PAM batch meter, and described PAM batch meter is connected with dosing pump, and dosing pump is connected with air buoyancy tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521132115.2U CN205313256U (en) | 2015-12-30 | 2015-12-30 | Modular emulsion effluent treatment plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521132115.2U CN205313256U (en) | 2015-12-30 | 2015-12-30 | Modular emulsion effluent treatment plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205313256U true CN205313256U (en) | 2016-06-15 |
Family
ID=56200119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521132115.2U Expired - Fee Related CN205313256U (en) | 2015-12-30 | 2015-12-30 | Modular emulsion effluent treatment plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205313256U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111330511A (en) * | 2018-12-18 | 2020-06-26 | 福建钦榕环保科技有限公司 | Demulsifier injection device for landfill leachate pretreatment with high use efficiency |
-
2015
- 2015-12-30 CN CN201521132115.2U patent/CN205313256U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111330511A (en) * | 2018-12-18 | 2020-06-26 | 福建钦榕环保科技有限公司 | Demulsifier injection device for landfill leachate pretreatment with high use efficiency |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104496123B (en) | A kind of micro-algae is disposed of sewage autocontrol method | |
| CN205313256U (en) | Modular emulsion effluent treatment plant | |
| CN204198506U (en) | Emulsifying liquid waste water treatment system | |
| CN105384279A (en) | System and method for processing wastewater generated during regeneration of SCR denitration catalyst | |
| CN205528198U (en) | Domestic sewage treatment system | |
| CN205556364U (en) | Heavy metal wastewater electro -deposition circulation processing system | |
| CN205398330U (en) | Domestic sewage treatment system | |
| CN105936567B (en) | A kind of OMBR integrated sewage treatment recycling devices | |
| CN109052816A (en) | A kind of cosmetics waste water treatment process | |
| CN202744374U (en) | Device for full-automatically treating dimethyl sulfoxide waste water | |
| CN205892838U (en) | Hydrogen peroxide handles wastewater systems | |
| CN206417964U (en) | A kind of weaving mill water process circulatory system | |
| CN204281444U (en) | Waste water rainwater cyclic utilization system | |
| CN205676153U (en) | Alkylation waste acid recycling system | |
| CN205710159U (en) | A kind of recovery system of electroplating wastewater | |
| CN205442857U (en) | Paint produce's water treatment facilities | |
| CN206751623U (en) | A kind of industrial waste water disposal device | |
| CN203803332U (en) | Dye synthesis exhaust gas treatment system | |
| CN203625176U (en) | Offset printing ink sewage treatment system | |
| CN209242842U (en) | A kind of small water wastewater zero discharge processing equipment | |
| CN203653385U (en) | Hospital wastewater treatment system | |
| CN209178162U (en) | RO energy saving of system device | |
| CN202924864U (en) | Membrane treatment system for emulsion waste water | |
| CN205838754U (en) | One heavy metal species mixing wastewater treatment equipment | |
| CN203530078U (en) | Centralized refined diatomite sanitary sewage treatment equipment |
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: 20160615 Termination date: 20191230 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |