CN208869478U - Waste water and waste residue utilization system in a kind of liquid phase method silicate production process - Google Patents
Waste water and waste residue utilization system in a kind of liquid phase method silicate production process Download PDFInfo
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- CN208869478U CN208869478U CN201821461854.XU CN201821461854U CN208869478U CN 208869478 U CN208869478 U CN 208869478U CN 201821461854 U CN201821461854 U CN 201821461854U CN 208869478 U CN208869478 U CN 208869478U
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- agitator tank
- inlet pipe
- filter press
- waste residue
- water
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Abstract
The utility model discloses waste water and waste residue utilization systems in a kind of liquid phase method silicate production process, including agitator tank and filter press, water inlet pipe is provided on agitator tank, air inlet pipe and feed pipe are provided with inlet valve and one end connection wastewater trough on water inlet pipe, are provided with intake valve in air inlet pipe, inlet valve and one end connection slag case are provided on feed pipe, opening valve is provided on agitator tank, filter press is connect with agitator tank, and filter press also connects water reuse tank and waste residue utilization tank simultaneously.Using agitator tank, secondary treatment has been carried out to waste residue, make wherein available silicate sufficiently dissolve；It using filter press, realizes and is separated by solid-liquid separation, the waste water after enabling clarification and the filter residue after drying obtain secondary use, protect environment, improve the utilization rate of resource, are conducive to the sustainable development of enterprise.
Description
Technical field
The utility model belong in silicate manufacturing field more particularly to a kind of liquid phase method silicate production process waste water and
Waste residue utilization system.
Background technique
Liquid phase method silicic acid technology of threonates is to be passed through high temperature and high pressure steam, directly using quartz sand and hydroxide as raw material
Reaction generates liquid silicon hydrochlorate.In process of production, a large amount of waste water and waste residue can be generated, arbitrarily discharge and accumulation, both polluted
Environment, and the serious waste of resource is caused, it is unfavorable for the development of enterprise.
Utility model content
In order to solve problem above, the utility model provides waste water and waste residue in a kind of liquid phase method silicate production process
Utilize system.
The utility model is realized in this way: waste water and waste residue utilization system in a kind of liquid phase method silicate production process,
Including agitator tank and filter press, it is provided with water inlet pipe, air inlet pipe and feed pipe on the agitator tank, is provided on the water inlet pipe
Inlet valve and one end connection wastewater trough, described air inlet pipe one end is provided with intake valve and agitator tank bottom is goed deep into the end of air inlet pipe
Portion is provided with inlet valve and one end connection slag case on the feed pipe, is provided with opening valve, the filters pressing on the agitator tank
Machine is connect with agitator tank, and kinetic pump is provided between the opening valve and filter press of the agitator tank, and the filter press is to stirring
Material in tank is separated by solid-liquid separation, and the filter press also connects water reuse tank and waste residue utilization tank, clear waste water simultaneously
It collects to water reuse tank, for adjusting the concentration of modified water glass, filter residue is dried up through compressed air, is collected to waste residue utilization
Tank, the raw materials for production as cement.
Preferably, the agitator tank is internally provided with blender, and outside is provided with motor, and the blender is connected to the motor
It connects, material is stirred.
Preferably, the water inlet pipe, air inlet pipe and feed pipe are made of seamless steel pipe.
Preferably, it is provided with pressure monitoring table and temperature monitoring table on the agitator tank, be respectively used in monitoring agitator tank
Pressure and temperature.
The beneficial effects of the utility model are: having carried out secondary treatment to waste residue using agitator tank, make wherein available
Silicate sufficiently dissolves；It using filter press, realizes and is separated by solid-liquid separation, the waste water after enabling clarification and the filter residue after drying obtain two
Secondary utilization, protects environment, improves the utilization rate of resource, is conducive to the sustainable development of enterprise.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
In figure: 1. agitator tanks；2. filter press；3. water inlet pipe；4. air inlet pipe；5. feed pipe；6. inlet valve；7. wastewater trough；
8. intake valve；9. inlet valve；10. slag case；11. opening valve；12. water reuse tank；13. waste residue utilization tank；14. blender；
15. motor；16. pressure monitoring table；17. temperature monitoring table；18. kinetic pump.
Specific embodiment
It is further to the utility model with reference to the accompanying drawing in order to be more clearly understood that the technical solution of the utility model
Explanation.
Waste water and waste residue utilization system in a kind of liquid phase method silicate production process as shown in Figure 1, including 1 He of agitator tank
Filter press 2 is provided with water inlet pipe 3, air inlet pipe 4 and feed pipe 5 on the agitator tank 1, is provided with inlet valve on the water inlet pipe 3
6 and one end connect wastewater trough 7, described 4 one end of air inlet pipe is provided with intake valve 8 and 1 bottom of agitator tank is goed deep into the end of air inlet pipe 4
Portion is provided with inlet valve 9 and one end connection slag case 10 on the feed pipe 5, is provided with opening valve 11 on the agitator tank 1,
The filter press 2 is connect with agitator tank 1, and is provided with kinetic pump 18 between the opening valve 11 and filter press 2 of the agitator tank 1,
The filter press 2 is separated by solid-liquid separation the material in agitator tank 1, and the filter press 2 is gone back while connecting 12 He of water reuse tank
Waste residue utilization tank 13, clear wastewater collection to water reuse tank 12, for adjusting the concentration of modified water glass, filter residue is through compressing
Air blow drying is collected to waste residue utilization tank 13, the raw materials for production as cement.
The agitator tank 1 is internally provided with blender 14, and outside is provided with motor 15, the blender 14 and 15 phase of motor
Connection, is stirred material.
The water inlet pipe 3, air inlet pipe 4 and feed pipe 5 are made of seamless steel pipe.
It is provided with pressure monitoring table 16 and temperature monitoring table 17 on the agitator tank 1, is respectively used in monitoring agitator tank 1
Pressure and temperature.
Inlet valve 6 is opened, the waste water in wastewater trough 7 is squeezed into agitator tank 1, opens inlet valve 9, it will be in slag case 10
Waste residue is put into agitator tank 1, starts to stir, and opens intake valve 8, is passed through steam and is heated to 50 DEG C or so, stirs 30 minutes, make
Available silicate sufficiently dissolves in waste residue；Turn on the power pump 18, and the material in agitator tank 1 is pumped into filter press 2, filter press
2 start to work, after being recycled to waste water clarification, by clear wastewater collection to water reuse tank 12, after filters pressing, with compression
Air blow drying filter residue, will be in dry residue collection to waste residue utilization tank 13.System described in the utility model can be used for silicon
The production of sour sodium can be used for the production of potassium silicate.
The above description is only a preferred embodiment of the present invention, therefore all according to described in the utility model patent application range
The equivalent change or modification done of structure, feature and principle, be included in the scope of the utility model patent application.
Claims (4)
1. waste water and waste residue utilization system in a kind of liquid phase method silicate production process, including agitator tank and filter press, feature
It is, water inlet pipe, air inlet pipe and feed pipe is provided on the agitator tank, inlet valve is provided on the water inlet pipe and one end connects
Connect wastewater trough, pot bottom is deeply stirred in the end that described air inlet pipe one end is provided with intake valve and air inlet pipe, on the feed pipe
It is provided with inlet valve and one end connection slag case, is provided with opening valve on the agitator tank, the filter press is connect with agitator tank,
And kinetic pump is provided between the opening valve and filter press of the agitator tank, the filter press consolidates the material in agitator tank
Liquid separation, the filter press also connect water reuse tank and waste residue utilization tank simultaneously.
2. waste water and waste residue utilization system in a kind of liquid phase method silicate production process according to claim 1, feature
It is, the agitator tank is internally provided with blender, and outside is provided with motor, and the blender, which is connected to the motor, to be connect.
3. waste water and waste residue utilization system in a kind of liquid phase method silicate production process according to claim 1, feature
It is, the water inlet pipe, air inlet pipe and feed pipe are made of seamless steel pipe.
4. waste water and waste residue utilization system in a kind of liquid phase method silicate production process according to claim 1, feature
It is, pressure monitoring table and temperature monitoring table is provided on the agitator tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821461854.XU CN208869478U (en) | 2018-09-07 | 2018-09-07 | Waste water and waste residue utilization system in a kind of liquid phase method silicate production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821461854.XU CN208869478U (en) | 2018-09-07 | 2018-09-07 | Waste water and waste residue utilization system in a kind of liquid phase method silicate production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208869478U true CN208869478U (en) | 2019-05-17 |
Family
ID=66467020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821461854.XU Active CN208869478U (en) | 2018-09-07 | 2018-09-07 | Waste water and waste residue utilization system in a kind of liquid phase method silicate production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208869478U (en) |
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2018
- 2018-09-07 CN CN201821461854.XU patent/CN208869478U/en active Active
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