CN215480260U - Standardized water treatment system - Google Patents
Standardized water treatment system Download PDFInfo
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- CN215480260U CN215480260U CN202122164600.XU CN202122164600U CN215480260U CN 215480260 U CN215480260 U CN 215480260U CN 202122164600 U CN202122164600 U CN 202122164600U CN 215480260 U CN215480260 U CN 215480260U
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- sewage
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- treatment system
- pump
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 91
- 239000010865 sewage Substances 0.000 claims abstract description 74
- 239000004576 sand Substances 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 17
- 238000005406 washing Methods 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 9
- 239000013049 sediment Substances 0.000 claims abstract description 9
- 239000004575 stone Substances 0.000 claims abstract description 6
- 239000003814 drug Substances 0.000 claims description 15
- 238000002360 preparation method Methods 0.000 claims description 14
- 238000003860 storage Methods 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 5
- 239000010802 sludge Substances 0.000 claims description 4
- 238000005189 flocculation Methods 0.000 claims description 3
- 230000016615 flocculation Effects 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 230000008569 process Effects 0.000 abstract description 8
- 238000001914 filtration Methods 0.000 abstract description 5
- 125000004122 cyclic group Chemical group 0.000 abstract description 3
- 238000001125 extrusion Methods 0.000 abstract description 2
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 238000011268 retreatment Methods 0.000 abstract 1
- 238000011001 backwashing Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000008570 general process Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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Abstract
The utility model relates to the field of sewage treatment of artificial sandstone crushing production lines, and provides a standardized water treatment system. Aims to solve the problems of complex process flow and low treatment efficiency of the traditional water treatment system due to the production line. The main scheme includes that clean water basin (1) supplies water for shale shaker (4) and washes the building stones, the drainage of shale shaker (4) is sent into spiral sand washing unit (6,7), sewage collecting pit (8) are sent into in the drainage of spiral sand washing unit (6,7), send to in sewage transfer pond (14) after the sewage pressurization of sewage collecting pit (8) through integrative unit of tailings (9, 10) are handled, sewage in sewage transfer pond (14) is through sediment stuff pump (15) pressurization entering concentration tank (16), the overflow clear water in concentration tank (16) top is through wet return to filtering ponds (19), send into pressure filter (18) with the mud that has flocculated in concentration tank (16) bottom, the clear water that pressure filter (18) extrusion filtered out flows back to sewage transfer pond (14) and recycles. This application has the ability to sewage retreatment, has improved the cyclic utilization ability to the water resource, has reduced the environmental pollution of similar production line.
Description
Technical Field
The utility model relates to a standardized water treatment system, and belongs to the field of sewage treatment of artificial sandstone crushing production lines.
Background
The water treatment system is a matched environment-friendly facility on a gravel aggregate production line, is one of main component systems of a gravel wet production line, and mainly has the functions of removing sludge from gravel materials needing to be screened in the running process of a vibrating screen machine and correspondingly treating sewage generated in the running process of the whole production line, so that the sewage treated by the water treatment system is recycled, and the purposes of removing water pollution and protecting the environment are achieved.
The water treatment system leads to the process flow complicated, the treatment effeciency is low because of the reason of production line in the past, through to similar systematic study in the past, this water treatment system has reached the technology and has simplified, has reduced customer's application and use cost to the efficiency to sewage treatment obtains promoting, and the mud cake water content is low, and water cyclic utilization is better.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the problems of complex process flow and low treatment efficiency of the traditional water treatment system due to the production line.
In order to achieve the above purpose, the utility model adopts the technical scheme that:
the utility model provides a standardized water processing system, the clean water basin supplies water for the shale shaker and washes the building stones, the spiral washed sand unit is sent into in the drainage of shale shaker, the sewage collecting pit is sent into to the drainage of spiral washed sand unit, send to in the sewage transfer pond after the integrative unit of tailings is handled after the sewage pressurization of sewage collecting pit, sewage in the sewage transfer pond is through sediment stuff pump pressurization entering concentrator bowl, the clear water that overflows in the concentrator bowl top is to the filtering ponds through the wet return, send into the pressure filter with the mud that the concentrator bowl bottom has flocculated, the clear water that the pressure filter extrusion was filtered out flows back to sewage transfer pond circulation and is used.
Among the above-mentioned technical scheme, the clear water is carried to the production line in the shale shaker top through the water supply trunk line and is washed the building stones in the clear water pump extraction clean water basin, and the shale shaker drainage gets into spiral sand washing unit through the shuttle groove, spiral sand washing unit sets up the both sides at sewage collecting pit, and spiral sand washing unit drainage assembles in the sewage collecting pit of the integrative unit below of tailings through the drain pipe, set up a stealthily dirty pump in the sewage collecting pit and pressurize in the integrative unit processing back of tailings through blowdown trunk line to sewage transfer pond, pressurize through the sediment stuff pump and get into the concentrate tank and temporarily store up.
In the technical scheme, the site is cleaned to generate sewage which is gathered in the sewage collecting tank through the drainage ditch.
Among the above-mentioned technical scheme, the sediment stuff pump pumps the concentration tank after with the sewage pressurization in the sewage transfer pond and stores temporarily, and the special pump of pressure filter sends into the pressure filter with the mud that the concentration tank bottom has flocculated.
Among the above-mentioned technical scheme, still include PAM medicament preparation facilities, clear water send to PAM medicament preparation facilities in with the poly acetamide stir the back send the sediment stuff pump with sewage after intensive mixing get into the concentration jar flocculation and precipitation.
Among the above-mentioned technical scheme, PAM medicament preparation facilities overflow pipe directly discharges into sewage transfer pond with the evacuation pipeline.
Among the above-mentioned technical scheme, send the clear water to the water storage tank through the immersible pump, the clear water in the water storage tank is sent to among the PAM medicament preparation facilities again and is stirred with the polypropionamide after filtration purification, and PAM medicament preparation facilities sends into the pipeline in front of the sediment stuff pump through the medicament pump pressurization of medicament that the stirring is good.
Among the above-mentioned technical scheme, still include concentrated jar recoil cleaning system, open the gate valve of concentrated jar recoil washing pipeline, open the clear water pump for the clear water in clear water pond reaches concentrated jar recoil interface through DN200 pipeline, opens corresponding gate valve and washes tank bottoms and pressure filter feed pipeline.
Among the above-mentioned technical scheme, spiral sand washer group includes first spiral sand washer and second spiral sand washer.
Among the above-mentioned technical scheme, integrative unit of tailings includes integrative unit of first tailings and the integrative unit of second tailings.
Because the utility model adopts the technical scheme, the utility model has the following beneficial effects:
this water treatment system has reached the technology and has simplified, has reduced customer's application and use cost to obtain promoting sewage treatment's efficiency, the mud cake water content is low, and water cyclic utilization is better.
Drawings
FIG. 1 is a general process flow diagram in example 1 of the present invention;
FIG. 2 is a process flow chart of a water supply and drainage system of a filter press workshop in example 1 of the present invention;
FIG. 3 is a process flow diagram of a multi-angle drainage part of the production line in embodiment 1 of the present invention;
FIG. 4 shows a part of a feed water pipe of a vibrating screen in embodiment 1 of the present invention;
FIG. 5 is a process flow chart of the water supply and drainage part of the filter press in example 1 of the present invention;
in the figure: 1. a clean water tank; 2. a clean water pump; 3. a main water supply pipeline of the production line; 4. vibrating screen; 5. a shuttle groove; 6. a first spiral sand washer; 7. a second spiral sand washer; 8. a sewage collection tank; 9. a first tailings all-in-one machine; 10. a second tailings all-in-one machine; 11. a drainage ditch; 12. a submersible sewage pump; 13. a main sewage pipeline; 14. a sewage transfer tank; 15. a slurry pump; 16. a concentration tank; 17. a pump dedicated for filter presses; 18. a filter press; 19. a filtration tank; 20. a submersible pump; 21. a water storage tank; 22. a PAM medicament preparation device; 23. a medicament pump.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described with reference to the accompanying drawings. In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, are merely for convenience in describing the present invention and simplifying the description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention.
referring to fig. 2 and 5, sewage is flocculated, a slurry pump 15 pressurizes the sewage in the sewage transfer tank 14 and pumps the sewage into a concentration tank 16 for temporary storage, and a special pump 17 for a filter press sends the flocculated sludge at the bottom of the concentration tank 16 to a filter press 18; the sewage treatment and the water drainage are carried out, and clear water overflowing from the top of the concentration tank 16 naturally flows into the filtering tank 19 through a water return pipe; the clear water squeezed and filtered by the filter press 18 flows back to the sewage transfer tank 14 for recycling.
Referring to fig. 5, the PAM apparatus supplies water, clear water is sent to the water storage tank 21 by the submersible pump 20, and the clear water in the water storage tank 21 is filtered and purified and then sent to the PAM agent preparation apparatus 22 to be stirred with the polypropionamide; the PAM medicament preparation facilities 22 passes through the medicament pump 23 and sends into the pipeline in front of the sediment stuff pump 15 the medicament pressurization that stirs, gets into the thickening jar 16 flocculation and precipitation behind stirring with the help of sediment stuff pump 15 and the sewage intensive mixing. The overflow pipeline and the emptying pipeline of the PAM reagent preparation device 22 are directly discharged into the sewage transfer tank 14 for recycling.
Referring to fig. 2 and 5, in the concentration tank backwashing system, the gate valve of the concentration tank backwashing pipeline is opened, the clean water pump 2 is opened, so that clean water in the clean water tank reaches two backwashing interfaces of the 16 backwashing interfaces of the concentration tank through the DN200 pipeline, one concentration tank emptying interface is opened, and the corresponding gate valve is opened to flush the tank bottom and the filter press feeding pipeline.
The foregoing shows and describes the general principles, essential features, and advantages of the utility model. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the utility model as claimed. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (10)
1. A standardized water treatment system, characterized by: the method comprises the steps that water is supplied to a vibrating screen (4) by a clean water tank (1) to wash stone materials, the drained water of the vibrating screen (4) is sent to a spiral sand washing unit (6,7), the drained water of the spiral sand washing unit (6,7) is sent to a sewage collecting tank (8), the sewage of the sewage collecting tank (8) is pressurized and then sent to a sewage transfer tank (14) after being treated by a tailing integrated unit (9, 10), the sewage in the sewage transfer tank (14) is pressurized by a slurry pump (15) and then enters a concentration tank (16), clear water overflowing from the top of the concentration tank (16) flows to a filter tank (19) through a water return pipe, the flocculated sludge at the bottom of the concentration tank (16) is sent to a filter press (18), and the clear water squeezed and filtered by the filter press (18) flows back to the sewage transfer tank (14) for recycling.
2. A standardized water treatment system according to claim 1 wherein: clear water is carried to shale shaker (4) top and is washed the building stones in the production line through main water supply line (3) in clean water pump (2) extraction clean water basin (1), and shale shaker (4) drainage gets into spiral sand washing unit (6,7) through shuttle groove (5), spiral sand washing unit (6,7) set up the both sides in sewage collecting pit (8), and spiral sand washing unit (6,7) drainage assembles in sewage collecting pit (8) of tailing integrative unit (9, 10) below through the drain pipe, set up a stealthily dirty pump (12) in sewage collecting pit (8) and pressurize for sewage and in tailing integrative unit (9, 10) are handled in blowdown main water line (13) to sewage transfer pond (14), pressurize through sediment stuff pump (15) and get into concentrated jar (16) and store temporarily.
3. A standardized water treatment system according to claim 2 wherein: the sewage generated by site cleaning is gathered in the sewage collecting tank (8) through the drainage ditch (11).
4. The standardized water treatment system according to the claim 1, wherein the slurry pump (15) pressurizes the sewage in the sewage transfer tank (14) and then pumps the sewage into the concentration tank (16) for temporary storage, and the special pump (17) for the filter press feeds the flocculated sludge at the bottom of the concentration tank (16) into the filter press (18).
5. A standardized water treatment system according to claim 1 wherein: the system also comprises a PAM medicament preparation device, clear water is sent to the PAM medicament preparation device (22) to be stirred with the polypropionamide, and then sent to a slurry pump (15) to be fully mixed with sewage, and then sent to a concentration tank (16) for flocculation and precipitation.
6. A standardized water treatment system according to claim 5 wherein: and an overflow pipeline and an emptying pipeline of the PAM medicament preparation device (22) are directly discharged into the sewage transfer tank (14).
7. The standardized water treatment system according to claim 5, wherein the clear water is sent to the water storage tank (21) through the submersible pump (20), the clear water in the water storage tank (21) is filtered and purified and then sent to the PAM agent preparation device (22) to be stirred with the polypropionamide, and the PAM agent preparation device (22) pressurizes and sends the stirred agent into the pipeline in front of the slurry pump (15) through the agent pump (23).
8. The standardized water treatment system according to any one of claims 1 to 7, further comprising a concentration tank backflushing cleaning system, wherein a gate valve of a concentration tank backflushing cleaning pipeline is opened, the clean water pump (2) is opened, so that clean water in the clean water tank reaches a backflushing interface of the concentration tank (16) through a DN200 pipeline, and a corresponding gate valve is opened to flush the tank bottom and a filter press feeding pipeline.
9. A standardized water treatment system according to claim 1 characterized in that the screw washer group (6,7) comprises a first screw washer (6) and a second screw washer (7).
10. A standardised water treatment system according to claim 1, characterised in that the tailing-integrated aggregate (9, 10) comprises a first tailing-integrated aggregate (9) and a second tailing-integrated aggregate (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122164600.XU CN215480260U (en) | 2021-09-08 | 2021-09-08 | Standardized water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122164600.XU CN215480260U (en) | 2021-09-08 | 2021-09-08 | Standardized water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215480260U true CN215480260U (en) | 2022-01-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202122164600.XU Active CN215480260U (en) | 2021-09-08 | 2021-09-08 | Standardized water treatment system |
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| Country | Link |
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| CN (1) | CN215480260U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113603272A (en) * | 2021-09-08 | 2021-11-05 | 成都大宏立机器股份有限公司 | Standardized water treatment system |
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- 2021-09-08 CN CN202122164600.XU patent/CN215480260U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113603272A (en) * | 2021-09-08 | 2021-11-05 | 成都大宏立机器股份有限公司 | Standardized water treatment system |
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