CN215798941U - Waste emulsion treatment system - Google Patents
Waste emulsion treatment system Download PDFInfo
- Publication number
- CN215798941U CN215798941U CN202121670728.7U CN202121670728U CN215798941U CN 215798941 U CN215798941 U CN 215798941U CN 202121670728 U CN202121670728 U CN 202121670728U CN 215798941 U CN215798941 U CN 215798941U
- Authority
- CN
- China
- Prior art keywords
- membrane filtration
- filtration system
- continuous membrane
- emulsion
- sludge
- 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.)
- Active
Links
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to the field of emulsion treatment systems, in particular to a waste emulsion treatment system. This system includes useless emulsion collecting vat, equalizing basin, electric flocculation reaction unit, oil-water knockout drum, one-level continuous membrane filtration system, second grade continuous membrane filtration system, sludge thickening tank, the horizontal transport mechanism of mud waterlogging caused by excessive rainfall, useless emulsion collecting vat, equalizing basin, electric flocculation reaction unit, oil-water knockout drum, one-level continuous membrane filtration system, second grade continuous membrane filtration system, sludge thickening tank loop through the body and establish ties together, and the horizontal transport mechanism of mud waterlogging caused by excessive rainfall is located the mud discharge mouth department of sludge thickening tank. The utility model discloses a carry out purification treatment to useless emulsion through useless emulsion collecting vat, equalizing basin, electric flocculation reaction unit, oil-water knockout drum, one-level continuous membrane filtration system, second grade continuous membrane filtration system. The compressed sludge is automatically conveyed out to other stations through a sludge concentration tank and a sludge draining transverse conveying mechanism. The efficiency of system treatment mud has been improved to this application.
Description
Technical Field
The utility model relates to the field of emulsion treatment systems, in particular to a waste emulsion treatment system.
Background
The emulsified waste liquid is produced mainly by the processes of mechanical processing, electroplating and automobile accessory production, and its main components are base oil, emulsifier, additive and water. The emulsion can be rancid, go bad and influence the use effect in the use process, so the emulsion needs to be replaced regularly. The emulsion belongs to hazardous waste, is extremely harmful to the environment, is not allowed to be directly discharged, and needs to be uniformly collected and treated by a hazardous waste disposal company. However, the efficiency of the existing emulsion for treating the sludge is low.
SUMMERY OF THE UTILITY MODEL
The utility model provides a waste emulsion treatment system, aiming at overcoming the defect of low sludge transportation efficiency of the existing emulsion treatment system.
The technical scheme adopted by the utility model for solving the technical problems is as follows: the utility model provides a useless emulsion processing system, includes useless emulsion collecting vat, equalizing basin, electric flocculation reaction unit, oil-water knockout drum, one-level continuous membrane filtration system, second grade continuous membrane filtration system, sludge thickening tank, the horizontal transport mechanism of mud waterlogging caused by excessive rainfall, useless emulsion collecting vat, equalizing basin, electric flocculation reaction unit, oil-water knockout drum, one-level continuous membrane filtration system, second grade continuous membrane filtration system, sludge thickening tank loop through the body and establish ties together, and the horizontal transport mechanism of mud waterlogging caused by excessive rainfall is located the mud discharge mouth department of sludge thickening tank.
According to another embodiment of the utility model, the sludge draining transverse conveying mechanism is composed of a mesh belt chain wheel, a box body and a conveying mesh belt, wherein a plurality of mesh belt chain wheels are respectively and rotatably connected to two ends of the box body, a shaft of the mesh belt chain wheel at one end is fixed on an output shaft of a motor, and all the mesh belt chain wheels are matched on the conveying mesh belt.
According to another embodiment of the present invention, further comprising a lift pump mounted to the tube.
According to another embodiment of the present invention, further comprising using an inorganic ceramic membrane in the primary continuous membrane filtration system.
According to another embodiment of the present invention, further comprising using an inorganic ceramic membrane in the secondary continuous membrane filtration system.
According to another embodiment of the utility model, the device further comprises a grid arranged at the material inlet of the waste emulsion collecting tank.
According to another embodiment of the present invention, the waste emulsion collecting tank is further provided with a waste compressing mechanism.
According to another embodiment of the utility model, the waste compressing mechanism is composed of a single-rod cylinder and a pressing plate, wherein the cylinder body of the single-rod cylinder is fixed on the waste emulsion collecting tank, and the pressing plate is fixed on the piston rod of the single-rod cylinder.
The beneficial effects of the utility model are that the utility model purifies the waste emulsion through a waste emulsion collecting tank, an adjusting tank, an electric flocculation reaction device, an oil-water separating tank, a primary continuous membrane filtration system and a secondary continuous membrane filtration system. The compressed sludge is automatically conveyed out to other stations through a sludge concentration tank and a sludge draining transverse conveying mechanism. The efficiency of system treatment mud has been improved to this application.
Drawings
The utility model is further illustrated with reference to the following figures and examples.
FIG. 1 is a schematic structural view of the present invention;
in the figure, 1, a waste emulsion collecting tank, 2, an adjusting tank, 3, an electric flocculation reaction device, 4, an oil-water separation tank, 5, a primary continuous membrane filtration system, 6, a secondary continuous membrane filtration system, 7, a sludge concentration tank, 8, a sludge draining transverse conveying mechanism, 9, a grid, 10, a waste compression mechanism, 11, a pipe body, 12, a lifting pump, 81, a mesh belt chain wheel, 82, a box body and 83 are conveying mesh belts.
Detailed Description
Fig. 1 is a schematic structural view of the present invention.
The utility model provides a useless emulsion processing system, includes useless emulsion collecting vat 1, equalizing basin 2, electric flocculation reaction unit 3, oil water separating tank 4, one-level continuous membrane filtration system 5, second grade continuous membrane filtration system 6, sludge thickening tank 7, the horizontal transport mechanism 8 of mud waterlogging caused by excessive rainfall, useless emulsion collecting vat 1, equalizing basin 2, electric flocculation reaction unit 3, oil water separating tank 4, one-level continuous membrane filtration system 5, second grade continuous membrane filtration system 6, sludge thickening tank 7 loop through body 11 and establish ties together, and the horizontal transport mechanism 8 of mud waterlogging caused by excessive rainfall is located the mud discharge mouth department of sludge thickening tank 7.
The sludge draining transverse conveying mechanism 8 consists of a mesh belt chain wheel 81, a box body 82 and a conveying mesh belt 83, wherein two ends of the box body 82 are respectively and rotatably connected with a plurality of mesh belt chain wheels 81, the shaft of the mesh belt chain wheel 81 at one end is fixed on the output shaft of a motor, and all the mesh belt chain wheels 81 are matched on the conveying mesh belt 83. The motor drives the mesh belt chain wheel 81 to rotate, and can drive the conveying mesh belt 83 to circularly drive. After the sludge falls onto the mesh belt 83, the sludge is carried forward by the mesh belt 83 and conveyed horizontally. During the conveying process, the moisture in the sludge can fall down through the meshes of the conveying mesh belt 83, so as to achieve the purpose of draining.
The tube 11 is provided with a lift pump 12.
An inorganic ceramic membrane is adopted in the primary continuous membrane filtration system 5.
An inorganic ceramic membrane is adopted in the secondary continuous membrane filtration system 6.
And a grid 9 is arranged at a feed inlet of the waste emulsion collecting tank 1.
A waste compressing mechanism 10 is arranged in the waste emulsion collecting tank 1.
The waste compressing mechanism 10 is composed of a single-rod cylinder and a pressing plate, the cylinder body of the single-rod cylinder is fixed on the waste emulsion collecting tank 1, and the pressing plate is fixed on the piston rod of the single-rod cylinder
The single-rod cylinder can drive the pressing plate to move downwards, and waste blocked by the grating 9 can be compressed and compressed.
As shown in fig. 1, firstly, the waste emulsion is introduced into a waste emulsion collecting tank 1 from a factory, and wastes with large volume are isolated by a grating 9. The waste emulsion is then pumped by lift pump 12 into conditioning tank 2 to adjust the pH to 8-9. Then the waste emulsion is pumped into an electric flocculation reaction device 3 for flocculation. Then, the emulsion is pumped into the oil-water separation tank 4 to separate oil from water. And pumping the emulsion into a first-stage continuous membrane filtration system 5 for filtration, and pumping the emulsion into a second-stage continuous membrane filtration system 6 for filtration. Then the sludge is compressed in the sludge concentration tank 7. And finally, discharging the sludge onto a sludge draining transverse conveying mechanism 8, and conveying the sludge to other stations.
Claims (8)
1. The utility model provides a useless emulsion processing system, characterized by, includes useless emulsion collecting vat (1), equalizing basin (2), electric flocculation reaction unit (3), oil-water separation jar (4), one-level continuous membrane filtration system (5), second grade continuous membrane filtration system (6), sludge thickening tank (7), the horizontal transport mechanism of mud waterlogging caused by excessive rainfall (8), useless emulsion collecting vat (1), equalizing basin (2), electric flocculation reaction unit (3), oil-water separation jar (4), one-level continuous membrane filtration system (5), second grade continuous membrane filtration system (6), sludge thickening tank (7) loop through body (11) and establish ties together, and the horizontal transport mechanism of mud waterlogging caused by excessive rainfall (8) are located the sludge discharge mouth department of sludge thickening tank (7).
2. The waste emulsion treatment system according to claim 1, wherein the sludge draining transverse conveying mechanism (8) comprises a mesh belt sprocket (81), a box body (82) and a conveying mesh belt (83), wherein a plurality of mesh belt sprockets (81) are respectively and rotatably connected to two ends of the box body (82), a shaft of the mesh belt sprocket (81) at one end is fixed on an output shaft of a motor, and all the mesh belt sprockets (81) are matched on the conveying mesh belt (83).
3. A waste emulsion processing system according to claim 1, wherein a lift pump (12) is mounted on the pipe body (11).
4. The waste emulsion treatment system according to claim 1, wherein an inorganic ceramic membrane is used in the primary continuous membrane filtration system (5).
5. The waste emulsion treatment system of claim 1, wherein an inorganic ceramic membrane is used in the secondary continuous membrane filtration system (6).
6. The waste emulsion treatment system according to claim 1, wherein a grid (9) is installed at a feed inlet of the waste emulsion collecting tank (1).
7. A waste emulsion processing system according to claim 1, wherein a waste compressing mechanism (10) is mounted in the waste emulsion collecting tank (1).
8. The waste emulsion processing system according to claim 7, wherein the waste compressing mechanism (10) comprises a single-rod cylinder and a pressing plate, wherein a cylinder body of the single-rod cylinder is fixed on the waste emulsion collecting tank (1), and the pressing plate is fixed on a piston rod of the single-rod cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202121670728.7U CN215798941U (en) | 2021-07-22 | 2021-07-22 | Waste emulsion treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202121670728.7U CN215798941U (en) | 2021-07-22 | 2021-07-22 | Waste emulsion treatment system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN215798941U true CN215798941U (en) | 2022-02-11 |
Family
ID=80183579
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202121670728.7U Active CN215798941U (en) | 2021-07-22 | 2021-07-22 | Waste emulsion treatment system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN215798941U (en) |
-
2021
- 2021-07-22 CN CN202121670728.7U patent/CN215798941U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110590092B (en) | River and lake sludge dewatering and solidifying integrated treatment process | |
CN209872690U (en) | Leachate treatment process device for garbage transfer station | |
CN109095742B (en) | Efficient dewatering system and method for river and lake sludge | |
CN109020152B (en) | Movable mud dehydration and solidification system | |
CN210313987U (en) | Deep sludge dewatering system | |
CN209227654U (en) | A kind of small-sized river movable type ecological dredging device | |
CN215798941U (en) | Waste emulsion treatment system | |
CN203842384U (en) | Belt type concentration filter press | |
CN212504503U (en) | Miniaturized pipeline sludge treatment system | |
CN217220544U (en) | Sludge rapid settling and dewatering equipment | |
CN113429085B (en) | Sewage treatment system for pull arm vehicle-mounted mobile toilet and water recycling method | |
CN215799038U (en) | Efficient mud conveying type waste emulsion treatment system | |
CN211998978U (en) | Eddy current solid-liquid separation device | |
CN212246546U (en) | Coal slime waste water treatment mummification device | |
CN209735060U (en) | Novel tap water pretreatment system | |
CN216073398U (en) | Automatic arrange useless emulsion processing system of mud | |
CN220245724U (en) | High-concentration organic wastewater treatment device | |
CN110921799A (en) | Eddy current solid-liquid separation device | |
CN219326178U (en) | Garbage transfer station | |
CN215627529U (en) | High salt pipe network sludge press filtration system | |
CN215276150U (en) | Mud hydraulic pressure filters integrated processing system | |
CN212770170U (en) | Long-distance pipeline coal slurry conveying terminal coal slime wastewater treatment system | |
CN117105476B (en) | Efficient treatment method for kitchen floating sludge | |
CN220265547U (en) | Intelligent recycling device for construction slurry | |
CN211283996U (en) | High-concentration organic industrial wastewater treatment equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |