CN204958689U - Industry sewage purification system - Google Patents
Industry sewage purification system Download PDFInfo
- Publication number
- CN204958689U CN204958689U CN201520758184.8U CN201520758184U CN204958689U CN 204958689 U CN204958689 U CN 204958689U CN 201520758184 U CN201520758184 U CN 201520758184U CN 204958689 U CN204958689 U CN 204958689U
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- CN
- China
- Prior art keywords
- trailer
- purification system
- basin
- sewage purification
- pool
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 35
- 238000000746 purification Methods 0.000 title claims abstract description 18
- 239000010802 sludge Substances 0.000 claims abstract description 32
- 230000007062 hydrolysis Effects 0.000 claims abstract description 19
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 19
- 239000000835 fiber Substances 0.000 claims abstract description 13
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 230000020477 pH reduction Effects 0.000 claims description 18
- 230000015271 coagulation Effects 0.000 claims description 15
- 238000005345 coagulation Methods 0.000 claims description 15
- 238000004062 sedimentation Methods 0.000 claims description 15
- 230000003139 buffering effect Effects 0.000 claims description 10
- 230000003301 hydrolyzing effect Effects 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 3
- 239000000523 sample Substances 0.000 claims description 3
- 238000011282 treatment Methods 0.000 abstract description 8
- 238000001914 filtration Methods 0.000 abstract description 4
- 230000003647 oxidation Effects 0.000 abstract description 3
- 230000001112 coagulating effect Effects 0.000 abstract 3
- 238000000034 method Methods 0.000 description 5
- 239000006228 supernatant Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 239000005446 dissolved organic matter Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model relates to a sewage treatment plant specifically is an energy saving, reduces and takes up an area of and the effectual industry sewage purification system of the succinct simultaneous processing of work step, including the catch basin, line mixer, the coagulating basin, just heavy pond, hydrolysis -acidification pool, contact oxidation tank, two heavy buffer pools, fibre carousel filtering pond, sludge impoundment and pressure filter, the catch basin, line mixer, the coagulating basin, just heavy pond, hydrolysis -acidification pool, contact oxidation tank, two heavy buffer pools and fibre carousel filtering pond concatenate in proper order, be equipped with the dredge pump in the two heavy buffer pools, a slide rail, the trailer, the tow chain with inhale the mud pipe, the one end of dredge pump visits second grade buffer pool bottom, the other end is installed on the trailer, inhale the one end and dredge pump intercommunication of mud pipe, the other end communicates with coagulating basin and hydrolysis -acidification pool respectively, it installs on the tow chain to inhale the mud pipe, the slide rail is laid in second grade buffer pool top, trailer and slide rail sliding fit, the tow chain is also installed on the second grade buffer pool, pond and the sludge impoundment of just sinking communicates, the sludge impoundment still communicates respectively with catch basin and pressure filter respectively.
Description
Technical field
The utility model relates to Sewage treatment systems, is specifically related to a kind of industrial sewage purification system.
Background technology
Can produce a large amount of waste water in industrial production, these waste water, as directly discharged without process, will cause severe contamination to environment.Existing Sewage treatment systems due to structure too complicated, cost of investment is large, and treatment process is superfluous, and is not suitable for medium-sized and small enterprises application.
To the method for Industrial Waste Water Treatments in currently available technology, that the sewage of discharging from workshop can enter water collecting basin and to collect sewage and cushion, water collecting basin enters line mixer and starts dosing such as PAC and PAM after collecting sewage, sewage after dosing enters coagulation basin makes medicine and sewage carry out abundant mixed flocculation, sewage after mixed flocculation is sent into preliminary sedimentation tank and is precipitated, inorganic mud after precipitation is pumped in the first sludge sump by sludge pump, mud in first sludge sump is discharged by pressure filter, mud supernatant liquor gets back to water collecting basin by the mode of backflow, supernatant liquor in preliminary sedimentation tank enters in hydrolysis acidification pool and is retained and progressively change dissolved organic matter into by the non-dissolved organic matter in waste water, some are difficult to biological explanation macromolecular substance and are converted into the small-molecule substance being easy to degrade, contact-oxidation pool is sent into by the sewage of hydrolysis acidification pool acidifying, by biological contact oxidation process to organic cod various in sewage, SS and BOD etc. decompose, the sewage decomposed from contact-oxidation pool is again sent into two heavy Buffer Pools and is fully decomposed and cushion, to decompose and supernatant major part in sewage after buffering is fed through fibre turntable filter chamber and carries out last filtration, the sewage reaching Effluent criteria after filtration externally discharges, two heavy Buffer Pools fully decompose and lower floor's mud in cushioning is sent in the second sludge sump, supernatant liquor in second sludge sump carries out backflow and gets back in water collecting basin or coagulation basin or hydrolysis acidification pool, lower floor's mud is sent in pressure filter by sludge pump and is externally discharged.
Can find out that the Sewage treatment systems of currently available technology often adopts two sludge sumps for the collection of inorganic mud and organic mud by foregoing description, each sludge sump is externally discharged by multiple pump housing again, so not only floor space is comparatively large, energy consumption is also higher simultaneously.
Utility model content
For the problems of the prior art, the utility model provides a kind of save energy, reduces and take up an area and the succinct industrial sewage purification system that treatment effect is good simultaneously of algorithm.
For realizing above technical purpose, the technical solution of the utility model is: a kind of industrial sewage purification system, comprises water collecting basin, line mixer, coagulation basin, preliminary sedimentation tank, hydrolysis acidification pool, contact-oxidation pool, two heavy Buffer Pools, fibre turntable filter chamber, sludge sump and pressure filter, described water collecting basin, line mixer, coagulation basin, preliminary sedimentation tank, hydrolysis acidification pool, contact-oxidation pool, two heavy Buffer Pools and fibre turntable filter chamber are connected in series successively, are provided with excavating pump in described two heavy Buffer Pools, slide rail, trailer, drag chain and suction pipe, one end of described excavating pump probes into bottom level 2 buffering pond, the other end is arranged on trailer, one end of described suction pipe is communicated with excavating pump, the other end is communicated with hydrolysis acidification pool with coagulation basin respectively, described suction pipe is arranged on drag chain, described slide rail is laid on above level 2 buffering pond, described trailer and slide rail are slidably matched, described drag chain is also arranged on level 2 buffering pond, described preliminary sedimentation tank is communicated with sludge sump, and described sludge sump is also communicated with pressure filter with water collecting basin respectively respectively.
As improvement, described suction pipe is connected for removable with between drag chain.
As improvement, described fibre turntable filter chamber is communicated with suction pipe.
As improvement, described excavating pump is fixedly connected with trailer.
As improvement, in described hydrolysis acidification pool, be provided with hydrolyzing sludge reflux line.
As improvement, described water collecting basin, line mixer, coagulation basin, preliminary sedimentation tank are respectively two.
As can be seen from the above description, the utility model possesses following advantage: the utility model is by fixing excavating pump and trailer, the mode that trailer is connected with drag chain makes whole sludge pump can move in pond, the benefit of such design is no longer to need the second sludge sump, but directly by the water in this sludge pump and mud by drag chain be arranged on suction pipe on drag chain as required directly by other equipment interconnections in the mode of movement and Sewage treatment systems, such as Buffer Pool, acidification pool etc., not only no longer need a large amount of circuit design, and greatly saved cost and the floor space of construction, simultaneously because no longer need the design of other sludge sump to also save a large amount of energy.
Accompanying drawing explanation
Fig. 1 is the schematic block diagram of industrial sewage purification system of the present utility model.
Fig. 2 is the schematic flow sheet of industrial sewage purification system of the present utility model.
Fig. 3 is the structural representation of two heavy Buffer Pools of industrial sewage purification system of the present utility model.Fig. 4 is the structural representation of two heavy Buffer Pools of industrial sewage purification system of the present utility model.Fig. 5 is the close-up schematic view of the A of two heavy Buffer Pools of industrial sewage purification system of the present utility model.
Accompanying drawing illustrates: 1, water collecting basin, 2, line mixer, 3, coagulation basin, 4, preliminary sedimentation tank, 5, hydrolysis acidification pool, 6, contact-oxidation pool, 7, two heavy Buffer Pools, 8, fibre turntable filter chamber, 9, sludge sump, 10, pressure filter, 11, excavating pump, 12, slide rail, 13, trailer, 14, drag chain, 15, suction pipe.
Embodiment
As shown in Fig. 1 to 5, a kind of industrial sewage purification system, comprises water collecting basin 1, line mixer 2, coagulation basin 3, preliminary sedimentation tank 4, hydrolysis acidification pool 5, contact-oxidation pool 6, two heavy Buffer Pools 7, fibre turntable filter chamber 8, sludge sump 9 and pressure filter 10, described water collecting basin 1, line mixer 2, coagulation basin 3, preliminary sedimentation tank 4, hydrolysis acidification pool 5, contact-oxidation pool 6, two heavy Buffer Pools 7 and fibre turntable filter chamber 8 are connected in series successively, are provided with excavating pump 11 in described two heavy Buffer Pools 7, slide rail 12, trailer 13, drag chain 14 and suction pipe 15, one end of described excavating pump 11 probes into bottom level 2 buffering pond 7, the other end is arranged on trailer 13, one end of described suction pipe 15 is communicated with excavating pump 11, the other end is communicated with hydrolysis acidification pool 5 with coagulation basin 3 respectively, described suction pipe 15 is arranged on drag chain 14, described slide rail 12 is laid on above level 2 buffering pond 7, described trailer 13 is slidably matched with slide rail 12, described drag chain 14 is also arranged on level 2 buffering pond 7, described preliminary sedimentation tank 4 is communicated with sludge sump 9, and described sludge sump 9 is also communicated with pressure filter 10 with water collecting basin 1 respectively respectively.
Described suction pipe 15 is connected for removable with between drag chain 14.
Described fibre turntable filter chamber 8 is communicated with suction pipe 15.
Described excavating pump 11 is fixedly connected with trailer 14.
Hydrolyzing sludge reflux line is provided with in described hydrolysis acidification pool 5.
Described water collecting basin 1, line mixer 2, coagulation basin 3, preliminary sedimentation tank 4 are respectively two.
The utility model is by fixing excavating pump and trailer, the mode that trailer is connected with drag chain makes whole sludge pump can move in pond, the benefit of such design is no longer to need the second sludge sump, but directly by the water in this sludge pump and mud by drag chain be arranged on suction pipe on drag chain as required directly by other equipment interconnections in the mode of movement and Sewage treatment systems, such as Buffer Pool, acidification pool etc., not only no longer need a large amount of circuit design, and greatly saved cost and the floor space of construction, simultaneously because no longer need the design of other sludge sump to also save a large amount of energy.
Be understandable that, above about specific descriptions of the present utility model, the technical scheme described by the utility model embodiment is only not limited to for illustration of the utility model.Those of ordinary skill in the art should be appreciated that and still can modify to the utility model or equivalent replacement, to reach identical technique effect; Needs are used, all within protection domain of the present utility model as long as meet.
Claims (6)
1. an industrial sewage purification system, comprises water collecting basin (1), line mixer (2), coagulation basin (3), preliminary sedimentation tank (4), hydrolysis acidification pool (5), contact-oxidation pool (6), two heavy Buffer Pools (7), fibre turntable filter chamber (8), sludge sump (9) and pressure filter (10), described water collecting basin (1), line mixer (2), coagulation basin (3), preliminary sedimentation tank (4), hydrolysis acidification pool (5), contact-oxidation pool (6), two heavy Buffer Pools (7) and fibre turntable filter chamber (8) are connected in series successively, are provided with excavating pump (11) in described two heavy Buffer Pools (7), slide rail (12), trailer (13), drag chain (14) and suction pipe (15), one end of described excavating pump (11) probes into bottom, level 2 buffering pond (7), the other end is arranged on trailer (13), one end of described suction pipe (15) is communicated with excavating pump (11), the other end is communicated with hydrolysis acidification pool (5) with coagulation basin (3) respectively, described suction pipe (15) is arranged on drag chain (14), described slide rail (12) is laid on top, level 2 buffering pond (7), described trailer (13) and slide rail (12) are slidably matched, described drag chain (14) is also arranged on level 2 buffering pond (7), described preliminary sedimentation tank (4) is communicated with sludge sump (9), described sludge sump (9) is also communicated with pressure filter (10) with water collecting basin (1) respectively respectively.
2. industrial sewage purification system according to claim 1, is characterized in that: described suction pipe (15) is connected for removable with between drag chain (14).
3. industrial sewage purification system according to claim 1, is characterized in that: described fibre turntable filter chamber (8) is communicated with suction pipe (15).
4. industrial sewage purification system according to claim 1, is characterized in that: described excavating pump (11) is fixedly connected with trailer (14).
5. industrial sewage purification system according to claim 1, is characterized in that: be provided with hydrolyzing sludge reflux line in described hydrolysis acidification pool (5).
6. industrial sewage purification system according to claim 1, is characterized in that: described water collecting basin (1), line mixer (2), coagulation basin (3), preliminary sedimentation tank (4) are respectively two.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520758184.8U CN204958689U (en) | 2015-09-28 | 2015-09-28 | Industry sewage purification system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520758184.8U CN204958689U (en) | 2015-09-28 | 2015-09-28 | Industry sewage purification system |
Publications (1)
Publication Number | Publication Date |
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CN204958689U true CN204958689U (en) | 2016-01-13 |
Family
ID=55053769
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201520758184.8U Expired - Fee Related CN204958689U (en) | 2015-09-28 | 2015-09-28 | Industry sewage purification system |
Country Status (1)
Country | Link |
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CN (1) | CN204958689U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105084680A (en) * | 2015-09-28 | 2015-11-25 | 江苏泰源环保科技有限公司 | Industrial sewage purification system |
-
2015
- 2015-09-28 CN CN201520758184.8U patent/CN204958689U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105084680A (en) * | 2015-09-28 | 2015-11-25 | 江苏泰源环保科技有限公司 | Industrial sewage purification system |
CN105084680B (en) * | 2015-09-28 | 2019-02-01 | 江苏泰源环保科技股份有限公司 | Industrial sewage purification system |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee | ||
CP01 | Change in the name or title of a patent holder |
Address after: 214200 new North Road, industrial Street, Xinzhuang street, Wuxi, Jiangsu, Yixing Patentee after: JIANGSU TAIYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Address before: 214200 new North Road, industrial Street, Xinzhuang street, Wuxi, Jiangsu, Yixing Patentee before: JIANGSU TAIYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. |
|
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160113 Termination date: 20190928 |