CN203513453U - Mass energy conversion treatment device for production waste water - Google Patents
Mass energy conversion treatment device for production waste water Download PDFInfo
- Publication number
- CN203513453U CN203513453U CN201320543906.9U CN201320543906U CN203513453U CN 203513453 U CN203513453 U CN 203513453U CN 201320543906 U CN201320543906 U CN 201320543906U CN 203513453 U CN203513453 U CN 203513453U
- Authority
- CN
- China
- Prior art keywords
- energy conversion
- concentration
- mass energy
- sludge
- waste water
- 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
Images
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a mass energy conversion treatment device for production waste water. The mass energy conversion treatment device is characterized by comprising a sludge thickening and dewatering device, wherein a thickened mass energy conversion tank is arranged at the rear end of the sludge thickening and dewatering device; a filter tank back-flushing waste water pre-thickening after-treatment device comprises a sludge discharging tank, a thickening tank, a balance tank and a dewatering machine room, which are connected in sequence; a supernatant outlet of the thickening tank, an emergency sludge discharging outlet of the balance tank and a filtrate outlet of the dewatering machine room are connected with the input end of the thickened mass energy conversion tank; the filtrate end of the thickened mass energy conversion tank is connected with the raw water end. According to the mass energy conversion treatment device, the sludge thickening and dewatering device is combined with the thickened mass energy conversion tank, so that the functions of concentrating and dewatering production sludge water, realizing standard emission and converting organic matters in the production waste water into biological energy sources are achieved.
Description
Technical field
The utility model is a kind of factory effluent characteristic energy changes treatment unit relating in water supply and sewage work, specifically a kind of factory effluent characteristic energy changes treatment unit that is applied to waterworks or Sewage Plant sludge from sedimentation tank water and filter back washing waste water.For sludge from sedimentation tank water and filter back washing waste water, adopt the optimum combination of concentrated, dehydration and characteristic energy changes to embody the minimizing of factory effluent and the treatment unit of resource utilization.
Background technology
In the water inlet of China city tap-water factory and Sewage Plant, contain gas chromatography and inorganics, after treatment process, most of as producing by product, discharge technical process, with the form of factory effluent, exist.Because the factory effluent water yield is large, contained for water inlet enrichment pollution substance after production technique is concentrated, become environment and social concern that city tap-water factory and Sewage Plant must solve.
At present, the processing problem that all relates to factory effluent in waterworks and Designing Sewage Treatment Plant operational process, in factory effluent, contained mud is by concentrated, natural mummification or mechanical dehydration, and making to produce mud can, with the form outward transport of solid body, reduce the impact on surrounding environment as far as possible.The main drawback of above-mentioned technology is that factory effluent drain time is generally comparatively concentrated, need to regulate and store; Nature mummification need the long period, rainy season sludge drying weak effect; Mechanical dehydration investment cost is high, and running cost is higher, and supernatant liquor and dehydration filtrate is the more difficult emission standard that reaches often, and owing to generally need adding coagulant aids in dehydration, affects the disposal of dewatered sludge; Main is that large amount of organic becomes environmental pressure again as pollutent.Artificial water-vegetation environmental is built in the water surrounding regulation of rising in recent years main employing, patent of invention as authorized in applicant, application number is 200610116070.9 " a kind of concentration mass energy conversion pool ", utilize plant to absorb and microbiological deterioration principle, solidify in the water of place to go the pollutents such as organism, but for the utilization of biomass energy insufficient, and because silt content is high, process load lower, often need very large floor space.
Utility model content
The purpose of this utility model is to provide a kind of factory effluent characteristic energy changes treatment unit, be suitable for the organism mass-energy conversion treatment device under different sludge treatment concentration technology conditions, when solving the thickening of production spoil disposal water, realize organism in sludge treatment technique water outlet qualified discharge and water and be converted into the effect that bioenergy further reclaims.
To achieve these goals, the technical solution of the utility model is: a kind of factory effluent characteristic energy changes treatment unit, it is characterized in that described treatment unit comprises sludge thicking dewatering equipment, the rear end of described sludge thicking dewatering equipment is also provided with concentration mass energy conversion pool, described sludge thicking dewatering equipment comprises the spoil disposal pond connecting successively, concentration basin, counterbalance cell, dehydration machine room, the supernatant liquor outlet of concentration basin, the emergent spoil disposal outlet of counterbalance cell is connected with the filtrate outlet of dehydration machine room and the input terminus of concentration mass energy conversion pool, the filtrate end of concentration mass energy conversion pool is connected with former water end (W.E.).
According to filter back washing waste water Different treatments, treatment unit is divided into filter back washing waste water pre-concentration after-treatment device, filter back washing waste water direct reuse treatment unit and sludge from sedimentation tank water and mixes concentration device three classes with filter back washing waste water.Wherein for filter back washing waste water pre-concentration after-treatment device, described factory effluent characteristic energy changes treatment unit also comprises the blowoff basin being connected with filter back washing waste water end, the pre-concentration pond being connected with blowoff basin, the supernatant liquor outlet in pre-concentration pond is connected with the input terminus of concentration mass energy conversion pool, and the thickened sludge exit end in pre-concentration pond is connected with the input terminus of concentration basin.For filter back washing waste water direct reuse treatment unit, described factory effluent characteristic energy changes treatment unit comprises the blowoff basin being connected with filter back washing waste water end, and the outlet of blowoff basin is connected with the input terminus of former water end (W.E.) and concentration mass energy conversion pool simultaneously.For sludge from sedimentation tank water, mix concentration device with filter back washing waste water, the input terminus in described spoil disposal pond is also connected with filter back washing waste water end.
The utility model combines sludge thicking dewatering equipment and concentration mass energy conversion pool, and in the thickening of realization production spoil disposal water, treatment unit qualified discharge and factory effluent, organism is converted into the function of bioenergy.The utility model, first according to filter back washing waste water Different treatments, by treatment unit classification, then according to different operational conditionss and requirement, forms the complete process system that three cover treatment unit form.The advantage of this device is to adapt to different places situation and operating requirement, when solving the thickening of production spoil disposal water, realizes organism in sludge treatment equipment water outlet qualified discharge and factory effluent and is converted into the effect that bioenergy further reclaims.
Accompanying drawing explanation
Fig. 1 is that the utility model is for filter back washing waste water pre-concentration after-treatment device schematic diagram.
Fig. 2 is for filter back washing waste water direct reuse treatment unit schematic diagram.
Embodiment
Below in conjunction with accompanying drawing, the utility model will be further described.
The utility model is a kind of factory effluent characteristic energy changes treatment unit, first according to filter back washing waste water Different treatments, treatment unit is divided into filter back washing waste water pre-concentration after-treatment device, filter back washing waste water direct reuse treatment unit and sludge from sedimentation tank water and mixes concentration device three classes with filter back washing waste water.
In filter back washing waste water pre-concentration after-treatment device, sludge from sedimentation tank water 1 first enters spoil disposal pond 2 and regulates and stores, and then evenly entering concentration basin 3, to carry out mud concentrated, and thickened sludge enters the interior storage of counterbalance cell 4, evenly enter again dehydration machine room 5 and dewater, deviate from mud and carry out dewatered sludge disposal 6; Filter back washing waste water 12 first enters blowoff basin 13 and regulates and stores, and then evenly enters pre-concentration pond 14 and carries out pre-concentration, and thickened sludge and 2 water outlets of spoil disposal pond enter in the lump concentration basin 3 and concentrate; Concentration basin 3 supernatant liquors, pre-concentration pond 14 supernatant liquors, the emergent spoil disposal of counterbalance cell 4 and dehydration machine room 5 filtrates enter concentration mass energy conversion pool 7 and deepen processing, and partial organic substances is converted into bioenergy and reclaims 8, and all the other mud carry out sludge drying and dispose 9; Concentration mass energy conversion pool 7 filtrates can be made former water conservancy with 10, also can up to standardly enter river water 11.In filter back washing waste water direct reuse treatment unit, sludge from sedimentation tank water 1 first enters spoil disposal pond 2 and regulates and stores, and then evenly entering concentration basin 3, to carry out mud concentrated, and thickened sludge enters the interior storage of counterbalance cell 4, evenly enter again dehydration machine room 5 and dewater, deviate from mud and carry out dewatered sludge disposal 6; Filter back washing waste water 12 first enters blowoff basin 13 and regulates and stores, and then can directly enter production treatment scheme and do former water conservancy with 10; Concentration basin 3 supernatant liquors, blowoff basin 13 water outlets, the emergent spoil disposal of counterbalance cell 4 and dehydration machine room 5 filtrates enter concentration mass energy conversion pool 7 and deepen processing, and partial organic substances is converted into bioenergy and reclaims 8, and all the other mud carry out sludge drying and dispose 9; Concentration mass energy conversion pool 7 filtrates can be made former water conservancy with 10, also can up to standardly enter river water 11.Sludge from sedimentation tank water mixes in concentration device with filter back washing waste water, together with after sludge from sedimentation tank water 1 first mixes with filter back washing waste water 12, entering spoil disposal pond 2 regulates and stores, then evenly entering concentration basin 3, to carry out mud concentrated, thickened sludge enters the interior storage of counterbalance cell 4, evenly enter again dehydration machine room 5 and dewater, deviate from mud and carry out dewatered sludge disposal 6; Concentration basin supernatant liquor 3, the emergent spoil disposal of counterbalance cell 4 and dehydration machine room 5 filtrates enter concentration mass energy conversion pool 7 and deepen processing, and partial organic substances is converted into bioenergy and reclaims 8, and all the other mud carry out sludge drying and dispose 9; Concentration mass energy conversion pool 7 filtrates can be made former water conservancy with 10, also can up to standardly enter river water 11.
Wherein spoil disposal pond, blowoff basin, concentration basin, pre-concentration pond, counterbalance cell, dehydration machine room and concentration mass energy conversion pool are prior art, no longer describe in detail.
Claims (4)
1. a factory effluent characteristic energy changes treatment unit, it is characterized in that described characteristic energy changes treatment unit comprises sludge thicking dewatering equipment, the rear end of described sludge thicking dewatering equipment is also provided with concentration mass energy conversion pool, described sludge thicking dewatering equipment comprises spoil disposal pond, concentration basin, counterbalance cell, the dehydration machine room connecting successively, the emergent spoil disposal outlet of the supernatant liquor outlet of concentration basin, counterbalance cell is connected with the filtrate outlet of dehydration machine room and the input terminus of concentration mass energy conversion pool, and the filtrate end of concentration mass energy conversion pool is connected with former water end (W.E.).
2. factory effluent characteristic energy changes treatment unit as claimed in claim 1, it is characterized in that described factory effluent characteristic energy changes treatment unit also comprises the blowoff basin being connected with filter back washing waste water end, the pre-concentration pond being connected with blowoff basin, the supernatant liquor outlet in pre-concentration pond is connected with the input terminus of concentration mass energy conversion pool, and the thickened sludge exit end in pre-concentration pond is connected with the input terminus of concentration basin.
3. factory effluent characteristic energy changes treatment unit as claimed in claim 1, it is characterized in that described factory effluent characteristic energy changes treatment unit comprises the blowoff basin being connected with filter back washing waste water end, the outlet of blowoff basin is connected with the input terminus of former water end (W.E.) and concentration mass energy conversion pool simultaneously.
4. factory effluent characteristic energy changes treatment unit as claimed in claim 1, is characterized in that the input terminus in described spoil disposal pond is also connected with filter back washing waste water end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320543906.9U CN203513453U (en) | 2013-09-03 | 2013-09-03 | Mass energy conversion treatment device for production waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320543906.9U CN203513453U (en) | 2013-09-03 | 2013-09-03 | Mass energy conversion treatment device for production waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203513453U true CN203513453U (en) | 2014-04-02 |
Family
ID=50372411
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320543906.9U Expired - Fee Related CN203513453U (en) | 2013-09-03 | 2013-09-03 | Mass energy conversion treatment device for production waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203513453U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104140166A (en) * | 2014-07-30 | 2014-11-12 | 上海市政工程设计研究总院（集团）有限公司 | Seasonal high-turbidity raw water treatment process |
| CN105254161A (en) * | 2015-10-23 | 2016-01-20 | 上海市政工程设计研究总院（集团）有限公司 | Sludge water treatment composite structure building system |
-
2013
- 2013-09-03 CN CN201320543906.9U patent/CN203513453U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104140166A (en) * | 2014-07-30 | 2014-11-12 | 上海市政工程设计研究总院（集团）有限公司 | Seasonal high-turbidity raw water treatment process |
| CN104973707A (en) * | 2014-07-30 | 2015-10-14 | 上海市政工程设计研究总院（集团）有限公司 | Seasonal high turbidity raw water processing technology |
| CN104140166B (en) * | 2014-07-30 | 2016-02-24 | 上海市政工程设计研究总院（集团）有限公司 | Seasonal high turbid original sub-block technique |
| CN104973707B (en) * | 2014-07-30 | 2018-04-20 | 上海市政工程设计研究总院（集团）有限公司 | A kind of seasonal high turbid original sub-block technique |
| CN105254161A (en) * | 2015-10-23 | 2016-01-20 | 上海市政工程设计研究总院（集团）有限公司 | Sludge water treatment composite structure building system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103172244B (en) | Recycling treatment method of water-submerged manure in breeding industry | |
| CN101948231B (en) | High-concentration anaerobic sludge digestion treatment process for carrying out mechanical dewatering on sludge | |
| CN103332831A (en) | Comprehensive erythromycin thiocyanate mushroom dreg waste water disposal system and method | |
| CN204454832U (en) | Cultivating wastewater purification reclaiming system | |
| CN103553274A (en) | Treatment process of industrial wastewater of medium density fiber | |
| CN202849208U (en) | Wastewater treatment system during production of white spirit | |
| CN104418481A (en) | Mass-energy transformation treatment process for production wastewater | |
| CN204752314U (en) | Lateral aeration biological filter tank structure | |
| CN203513453U (en) | Mass energy conversion treatment device for production waste water | |
| CN204550363U (en) | Miniature City septic tank ight soil recycling sludge is dissolved station | |
| CN109851094A (en) | A kind of animal wastes water dirt method for separating and processing | |
| CN203976579U (en) | A kind of sun power microkinetic sewage disposal device | |
| CN105565598A (en) | Method for comprehensively treating and utilizing cassava vinasse waste water and industrial sludge | |
| CN205170624U (en) | Environmental protection sewage treatment system | |
| CN204325072U (en) | A kind of integrated wastewater recycling treatment system | |
| CN203568940U (en) | Pulping sewage recycling system | |
| CN208949114U (en) | Sludge anaerobic treatment system | |
| CN102276120A (en) | Sewage treatment zero emission technical device utilizing solar septic tank | |
| CN103395951B (en) | System capable of utilizing acid to neutralize slags and dehydrated aluminum sludge to treat nitrogenous wastewater and method thereof | |
| CN207775018U (en) | A effluent disposal system for organic synthesis | |
| CN204058089U (en) | Seasonal high turbid original sub-block device | |
| CN201240978Y (en) | Combined type sewage in situ processing system | |
| CN104355487A (en) | Ecological sewage treatment method | |
| CN203593658U (en) | Sewage treatment device capable of collecting sludge and methane | |
| CN203440213U (en) | Filtering layer reactor and wastewater treatment device |
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: 20140402 Termination date: 20210903 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |