CN202898136U - Sewage treatment system for processing artificial granite and quartzite - Google Patents
Sewage treatment system for processing artificial granite and quartzite Download PDFInfo
- Publication number
- CN202898136U CN202898136U CN 201220398465 CN201220398465U CN202898136U CN 202898136 U CN202898136 U CN 202898136U CN 201220398465 CN201220398465 CN 201220398465 CN 201220398465 U CN201220398465 U CN 201220398465U CN 202898136 U CN202898136 U CN 202898136U
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- sewage
- tower
- quartzite
- pump
- sewage treatment
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Abstract
The utility model relates to a sewage treatment system for processing artificial granite and quartzite, which comprises a sewage tank (1), a chemical adding device (2), a sewage tower (3) and a water purifying tower (4), wherein the front end of the sewage tank (1) is connected to a guide groove; a grid (11) is arranged at the joint; a submerged sewage pump (12) is arranged in the sewage tank (1); the sewage pump (12) and the sewage tower (3) are connected through a sewage pipe (9); an effluent weir (13) is arranged on the top of the sewage tower (3); the effluent weir (13) is connected to the water purifying tower (4); a pipeline (15) on the top of the water purifying tower (4) is communicated with a clean-water tank; sludge at the bottoms of the sewage tower (3) and the water purifying tower (4) is discharged into a sludge stirring tank (18) through pipelines; the bottom of the sludge stirring tank (18) is connected with a sludge pump (21) through a mud pumping pipeline (20); and the other end of the sludge pump (21) is connected to a pressure filter (22). The sewage treatment system disclosed by the utility model is flexible in combination manner, small in occupation area, high in circulating water purification degree and high in treatment capacity; due to automatic intelligent control, the sewage treatment system is few in maintenance people and low in labour intensity; and in addition, due to connection by adopting the closed pipeline, the field environment is ensured to be tidy.
Description
Technical field
The utility model relates to a kind of Sewage treatment systems, particularly relates to a kind of Sewage treatment systems for the processing of stonite's quartzite.
Background technology
Produce a large amount of sewage in the processing of stone production process, the treatment process that generally adopts at present is a plurality of settling tanks or settling box series connection, and mud sediment is in the bottom, and the water of clarification is supplied with production plant by water pump and used.But existing Sewage treatment systems exists that operation cost is high, recycled-water quality is poor and to problems such as environments.
The utility model content
The utility model provides a kind of employing closed conduit to connect, and array mode is flexible, and floor space is little, and the recirculating water purification degree is high, and treatment capacity is large, stonite's quartzite Sewage treatment systems that environmental pollution is little.
For achieving the above object, technical solution of the present utility model is, a kind of stonite's quartzite Sewage treatment systems is provided, comprise sewage lagoon, chemicals dosing plant, sewage tower and water purification tower, described sewage lagoon front end connects the guiding ditch, and be provided with grid in the junction, and the liquid sewage pump is arranged in the described sewage lagoon, be connected by waste pipe between described residual sea water pump and the described sewage tower; Described sewage top of tower is provided with effluent weir, described effluent weir is connected to described water purification tower, described water purification top of tower has device for cleaning pipeline toward clean water basin, described sewage tower and described water purification tower bottom mud all enter the sludge agitation pond by pipeline, described agitated pool bottom is connected with sludge pump by the extraction mud pipe road, and the described sludge pump the other end connects pressure filter.
Technique scheme can be preferably, and described chemicals dosing plant comprises agitator, volume pump (6), loading pipeline, and described volume pump is connected with magnetic valve, and described loading pipeline is connected with described waste pipe respectively and check valve is set before tie point.
Technique scheme can be preferably, and described two residual sea water pumps are opened simultaneously or closed with corresponding described magnetic valve, and described residual sea water pump is not opened simultaneously.
Technique scheme can be preferably, and described sewage tower bottom is tapered and operated pneumatic valve control discharging sediment is installed, and described water purification tower bottom is provided with operated pneumatic valve control discharging sediment, and operated pneumatic valve is connected with air compressor with operated pneumatic valve and is connected.
Technique scheme can preferably, be provided with sludge stirring machine in the described agitated pool.
Technique scheme can be preferably, and described all pipelines adopt closed connection.
Technique scheme can be preferably, and described system controls automatically by centralized control unit.
This Sewage treatment systems array mode is flexible, and floor space is little, and the recirculating water purification degree is high, and treatment capacity is large; The control of employing automatic intelligent, the maintenance personnel is few, and labour intensity is low; The employing closed conduit connects, and guarantees that the place environment is clean and tidy, is applicable to the relevant enterprise of all kinds of scales; System integrates precipitation, concentrated, pressure-filtering deslagging, and multiple functional, technique is advanced, and treatment effect is good.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment
Embodiment 1:
Sewage treatment systems principle of work of the present utility model is, the sewage that processing stonite quartzite emits is flowed to sewage lagoon 1 through the guiding ditch, larger buoyancy aid is removed in sewage lagoon 1 preposition grid 11 debris retainings, and sewage pumps to sewage tower 3 by liquid sewage pump 12; After simultaneously chemicals dosing plant 2 prepares medicament and tap water in proportion, inject waste pipe 9 by loading pipeline 7 quantitatively by volume pump 6, send into sewage tower 3 in company with sewage, volume pump 6 pressure must be greater than hydraulic pressure in the waste pipe 9, it is clean that loading pipeline 7 requires to keep, suitably anticorrosion, loading pipeline 7 be provided with check valve 10 before waste pipe 9 is connected with sewage recoil after preventing termination of pumping; Magnetic valve 8 and residual sea water pump 12 correspondences are opened or are closed, and two pipelines do not use simultaneously; Polymerization acceleration precipitation occurs because of the chemical flocculation effect of liquid in sewage tower 3 interior sewage, suspension is layering in tower, the upper strata is limpider, lower floor is muddy, the upper strata clear water overflows to water purification tower 4 by effluent weir 13, lower floor's thickened sludge is deposited in tower base cone section, is discharged into sludge agitation pond 18 by the operated pneumatic valve 14 at the bottom of the tower; Treated sewage obtains more clear water matter after by secondary sedimentation in water purification tower 4, but direct circulation for the production of, water purification tower 4 bottom mud also are discharged into sludge agitation pond 18 when operated pneumatic valve 16 is opened; The open and close of operated pneumatic valve 14 and operated pneumatic valve 16 are by air compressor 17 controls; Sludge sump 18 interior mud will ceaselessly stir, and prevent the homogeneous chemical composition before reacted mud continues flocculation sediment and guarantees sludge dewatering; Mud pumps to pressure filter 22 filtrations by sludge pump 21 by extraction mud pipe road 20 after stirring, and sludge pump 21 pressure are larger, and filter cake is more dried, but the filter cloth loss is larger simultaneously, and general stone industry recommendation operating pressure is 0.4-0.6Mpa; In pressure filter 22 each filter chamber, form relatively drier filter cake, filter cake outward transport landfill disposal, the clear water after pressure filter 22 filters flows into the tank recycle; All pipelines of system adopt closed connection.
This Sewage treatment systems is controlled automatically by control center, its stable performance, and reliable in action, level of automation is high.Automatically the algorithm of control is as follows: sewage reaches certain in limited time upper in the sewage lagoon 1, and liquid sewage pump 12 is opened (note: the flow of residual sea water pump 12 must greater than sewage flow rate) automatically, and sewage reaches certain and prescribes a time limit residual sea water pump 12 auto stops down; Magnetic valve 8 and residual sea water pump 12 correspondences are opened or are closed, and two pipelines do not use simultaneously; Sewage and liquid are after the 3 interior abundant reactions of sewage tower and layering, thickened sludge is piled up by tower base cone section, tower bottom operated pneumatic valve 14 is subjected to mud agitated pool 18 bounds control autoshutdown and unlatching, and in limited time, operated pneumatic valve is opened under agitated pool 18 interior mud reach, mud discharging is in agitated pool 18 in the tower, prescribe a time limit when agitated pool 18 interior mud reach, operated pneumatic valve is closed, and stops to discharge mud, can guarantee like this sewage reaction times abundance in the tower, effluent weir 13 flows out all the time than clear water matter; Agitated pool 18 interior stirrers 19 are forbidden idle running work under anhydrous state; Water purification tower 4 bottom operated pneumatic valves 16 can be controlled time opening discharging mud to agitated pool 18 by system; The open and close of operated pneumatic valve 14 and operated pneumatic valve 16 are by air compressor 17 controls; Prescribe a time limit when agitated pool 18 interior mud reach, sludge pump 21 is opened.
Claims (7)
1. stonite's quartzite Sewage treatment systems, comprise sewage lagoon (1), chemicals dosing plant (2), sewage tower (3) and water purification tower (4), it is characterized in that: described sewage lagoon (1) front end connects the guiding ditch, and be provided with grid (11) in the junction, liquid sewage pump (12) is arranged in the described sewage lagoon (1), be connected by waste pipe (9) between described residual sea water pump (12) and the described sewage tower (3); Described sewage tower (3) top is provided with effluent weir (13), described effluent weir (13) is connected to described water purification tower (4), described water purification tower (4) top has pipeline (15) to lead to clean water basin, described sewage tower (3) and described water purification tower (4) bottom mud all enter sludge agitation pond (18) by pipeline, described agitated pool (18) bottom is connected with sludge pump (21) by extraction mud pipe road (20), and described sludge pump (21) the other end connects pressure filter (22).
2. stonite's quartzite Sewage treatment systems according to claim 1, it is characterized in that: described chemicals dosing plant (2) comprises agitator (5), volume pump (6), loading pipeline (7), described volume pump (6) is connected with magnetic valve (8), and described loading pipeline (7) is connected with described waste pipe (9) respectively and check valve (10) is set before tie point.
3. stonite's quartzite Sewage treatment systems according to claim 1, it is characterized in that: two residual sea water pumps (12) are opened simultaneously or are closed with corresponding described magnetic valve (8), and described residual sea water pump (12) is not opened simultaneously.
4. stonite's quartzite Sewage treatment systems according to claim 1, it is characterized in that: described sewage tower (3) bottom is tapered and operated pneumatic valve (14) control discharging sediment is installed, described water purification tower (4) bottom is provided with operated pneumatic valve (16) control discharging sediment, and operated pneumatic valve (14) is connected 16 with operated pneumatic valve) be connected with air compressor (17) respectively.
5. stonite's quartzite Sewage treatment systems according to claim 1 is characterized in that: be provided with sludge stirring machine (19) in the described agitated pool (18).
6. stonite's quartzite Sewage treatment systems according to claim 1, it is characterized in that: all pipelines adopt closed connection.
7. stonite's quartzite Sewage treatment systems according to claim 1, it is characterized in that: system controls automatically by centralized control unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220398465 CN202898136U (en) | 2012-08-13 | 2012-08-13 | Sewage treatment system for processing artificial granite and quartzite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220398465 CN202898136U (en) | 2012-08-13 | 2012-08-13 | Sewage treatment system for processing artificial granite and quartzite |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202898136U true CN202898136U (en) | 2013-04-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220398465 Expired - Fee Related CN202898136U (en) | 2012-08-13 | 2012-08-13 | Sewage treatment system for processing artificial granite and quartzite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202898136U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103601312A (en) * | 2013-10-22 | 2014-02-26 | 徐连波 | Stone material sewage treatment system and method thereof |
| CN107986514A (en) * | 2018-01-09 | 2018-05-04 | 佛山市沙污净环保科技有限公司 | A kind of full-automation separation of solid and liquid sewage disposal system and method |
-
2012
- 2012-08-13 CN CN 201220398465 patent/CN202898136U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103601312A (en) * | 2013-10-22 | 2014-02-26 | 徐连波 | Stone material sewage treatment system and method thereof |
| CN107986514A (en) * | 2018-01-09 | 2018-05-04 | 佛山市沙污净环保科技有限公司 | A kind of full-automation separation of solid and liquid sewage disposal system and method |
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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: 20130424 Termination date: 20140813 |
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| EXPY | Termination of patent right or utility model |