CN203487002U - Water-based ink wastewater purification treatment device - Google Patents
Water-based ink wastewater purification treatment device Download PDFInfo
- Publication number
- CN203487002U CN203487002U CN201320495315.9U CN201320495315U CN203487002U CN 203487002 U CN203487002 U CN 203487002U CN 201320495315 U CN201320495315 U CN 201320495315U CN 203487002 U CN203487002 U CN 203487002U
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- CN
- China
- Prior art keywords
- tank
- pond
- purification treatment
- water
- wastewater purification
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- Expired - Fee Related
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 239000002351 wastewater Substances 0.000 title claims abstract description 19
- 238000000746 purification Methods 0.000 title claims abstract description 18
- 238000004062 sedimentation Methods 0.000 claims abstract description 14
- 239000010802 sludge Substances 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000005276 aerator Methods 0.000 claims abstract description 9
- 238000005273 aeration Methods 0.000 claims abstract description 5
- 230000015271 coagulation Effects 0.000 claims description 14
- 238000005345 coagulation Methods 0.000 claims description 14
- 230000001112 coagulating effect Effects 0.000 abstract 2
- 239000000945 filler Substances 0.000 abstract 2
- 230000000903 blocking effect Effects 0.000 abstract 1
- 239000010865 sewage Substances 0.000 description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- SEPPVOUBHWNCAW-FNORWQNLSA-N (E)-4-oxonon-2-enal Chemical compound CCCCCC(=O)\C=C\C=O SEPPVOUBHWNCAW-FNORWQNLSA-N 0.000 description 1
- LLBZPESJRQGYMB-UHFFFAOYSA-N 4-one Natural products O1C(C(=O)CC)CC(C)C11C2(C)CCC(C3(C)C(C(C)(CO)C(OC4C(C(O)C(O)C(COC5C(C(O)C(O)CO5)OC5C(C(OC6C(C(O)C(O)C(CO)O6)O)C(O)C(CO)O5)OC5C(C(O)C(O)C(C)O5)O)O4)O)CC3)CC3)=C3C2(C)CC1 LLBZPESJRQGYMB-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Images
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to a water-based ink wastewater purification treatment device. The water-based ink wastewater purification treatment device is characterized in that an adjusting tank with a grid, an aerator and a lift pump, a pH coarse adjustment tank, a pH fine adjustment tank, a primary coagulating tank, a secondary coagulating tank, a filter with a sloping plate, a primary sedimentation tank of a sludge pump, an anaerobic tank with a combination filler, an aerobiotic tank with an aerator and a combination filler, a secondary sedimentation tank with a central flow guiding pipe, a flow blocking plate, an effluent weir and a sludge pump and a yielding water tank are sequentially arranged along a purification treatment technological process, an air blower is used for aeration, connecting pipes are arranged between the adjacent tanks, the height falling from high to low exists between the adjacent tanks, and the primary sedimentation tank and the secondary sedimentation tank are connected to a filter press through a pipeline with the sludge pump. The water-based ink wastewater purification treatment device has the advantages of small dosage, low operating cost, simple and convenient operation, full-automatic operation and no secondary pollution; and yielding water is stable and reaches the standard.
Description
Technical field
The utility model relates to a kind of wastewater purification treatment equipment, and particularly a kind of water color ink wastewater purification treatment equipment, belongs to sewage treatment area.
Background technology
At present, what domestic packed in cases industry generally adopted is water color ink printing technology, in process of production, need to change ink cleaning of graphic arts equipment and can produce a certain amount of printing ink wastewater.Because COD and the colourity of water color ink waste water are generally all very high, not possessing can directly biochemical treatment condition, even if adopt tens times of direct thin up way dilutions even hundred times, thousands of times, the COD of waste water and colourity are also difficult to reach emission standard, have increased again pollution volume, intractability and the processing cost of waste water simultaneously; Adopt to burn, transport outward buried method and also make cost for wastewater treatment very high, easily cause secondary pollution, allow enterprise be difficult to bear.
Utility model content
The purpose of this utility model is to overcome the shortcoming of prior art, provides a kind of high treatment effect, cheaply water color ink wastewater purification treatment equipment.
The purpose of this utility model is achieved through the following technical solutions: a kind of water color ink wastewater purification treatment equipment, it is characterized in that: along purification process technique flow process, be followed successively by with grid, aerator, the equalizing tank of lift pump, PH coarse adjustment pond, PH accurate adjustment pond, one-level coagulation basin, two-stage coagulation pond, with swash plate strainer, the preliminary sedimentation tank of sludge pump, anaerobic pond with combined stuffing, with aerator, the Aerobic Pond of combined stuffing, with center thrust-augmenting nozzle, flow-stopping plate, effluent weir, the second pond of sludge pump, outlet sump, adopt gas blower to carry out aeration, between each adjacent pool, there are connecting water pipe and height fall from high to low, wherein preliminary sedimentation tank is connected with pressure filter through the pipeline of sludge pump is installed with second pond.
Described grid adopts automatically middle grid, and interval of grid strip is 40mm.
Described gas blower adopts rotary blower.
Described pressure filter adopts plate-and-frame filter press.
The utlity model has following advantage: dosage is few, running cost is low; Easy and simple to handle, fully automatic operation; Do not produce secondary pollution; Stable water outlet is up to standard.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1-equalizing tank, 101-grid, 102 aeration tanks, 103-lift pump, 2-PH coarse adjustment pond, 3-PH accurate adjustment pond, 4-one-level coagulation basin, 5-two-stage coagulation pond, 6-preliminary sedimentation tank, 601 hypotenuse strainers, 602-sludge pump, 7-anaerobic pond, 701-combined stuffing, 8-Aerobic Pond, 801-aerator, 9-second pond, 901 center thrust-augmenting nozzles, 902-flow-stopping plate, 903-effluent weir, 10-outlet sump, 11-gas blower, 12-pressure filter.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further described, but protection domain of the present utility model is not limited to the following stated.
As shown in Figure 1, a kind of water color ink wastewater purification treatment equipment: be followed successively by the equalizing tank 1 with grid 101, aerator 102, lift pump 103 along purification process technique flow process, PH coarse adjustment pond 2, PH accurate adjustment pond 3, one-level coagulation basin 4, two-stage coagulation pond 5, preliminary sedimentation tank 6 with swash plate strainer 601, sludge pump 602, anaerobic pond 7 with combined stuffing 701, Aerobic Pond 8 with aerator 801, combined stuffing 701, with the second pond 9 of center thrust-augmenting nozzle 901, flow-stopping plate 902, effluent weir 903, sludge pump 602, outlet sump 10.Adopt gas blower 11 to carry out aeration, between each adjacent pool, there are connecting water pipe and height fall from high to low, wherein preliminary sedimentation tank 6 is connected with pressure filter 12 through the pipeline of sludge pump is installed with second pond 9, grid 101 adopts automatically middle grid, interval of grid strip is 40mm, gas blower 11 adopts rotary blower, and pressure filter 12 adopts plate-and-frame filter press.
The utility model technical process is as follows: sewage is introduced into equalizing tank 1, in equalizing tank, be provided with mechanical grille 101, after sewage, enter successively PH coarse adjustment pond 2, PH accurate adjustment pond 3, one-level coagulation basin 4, two-stage coagulation pond 5, in PH equalizing tank, mainly add sodium hydroxide, in coagulation basin, mainly add PAM and PAC, in coagulation basin water outlet, contain great quantity of floc suspended substance, therefore sewage enters preliminary sedimentation tank 6, preliminary sedimentation tank 6 adopts ramp type settling tank, enter afterwards anaerobic pond 7, macromolecule contaminant is degraded to small molecules pollutent, then enter Aerobic Pond 8, most of pollutent is removed at Aerobic Pond 8, Aerobic Pond 8 water outlets enter second pond 9, last sewage enters outlet sump 10 after precipitation.
The day processing waste water ability 100t of now take is example, the in the situation that of surplus with due regard to, each pond reference volume is as follows: equalizing tank 1 is that 50m3, PH coarse adjustment pond 2 are 3 m3, PH accurate adjustment pond 3 is 3 m3, one-level coagulation basin 4 is 3m3, and two-stage coagulation pond 5 is that 3 m3, preliminary sedimentation tank 6 are that 12m3, anaerobic pond 7 are that 20m3, Aerobic Pond 8 are that 50m3, second pond 9 are that 12m3, outlet sump 10 are 6m3.Grid 101 is selected automatically middle grid, interval of grid strip 40mm, and lift pump 103 and sludge pump 602 all adopt WQ10-7-0.75 type, and gas blower 11 is HC-501 type, and dosing adopts volume pump metering dosing, and pressure filter 12 is XMY30/630-UB type.
Claims (4)
1. a water color ink wastewater purification treatment equipment, it is characterized in that: along purification process technique flow process, be followed successively by with grid, aerator, the equalizing tank of lift pump, PH coarse adjustment pond, PH accurate adjustment pond, one-level coagulation basin, two-stage coagulation pond, with swash plate strainer, the preliminary sedimentation tank of sludge pump, anaerobic pond with combined stuffing, with aerator, the Aerobic Pond of combined stuffing, with center thrust-augmenting nozzle, flow-stopping plate, effluent weir, the second pond of sludge pump, outlet sump, adopt gas blower to carry out aeration, between each adjacent pool, there are connecting water pipe and height fall from high to low, wherein preliminary sedimentation tank is connected with pressure filter through the pipeline of sludge pump is installed with second pond.
2. a kind of water color ink wastewater purification treatment equipment according to claim 1, is characterized in that: described grid adopts automatically middle grid, and interval of grid strip is 40mm.
3. a kind of water color ink wastewater purification treatment equipment according to claim 1, is characterized in that: described gas blower adopts rotary blower.
4. a kind of water color ink wastewater purification treatment equipment according to claim 1, is characterized in that: described pressure filter adopts plate-and-frame filter press.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320495315.9U CN203487002U (en) | 2013-08-14 | 2013-08-14 | Water-based ink wastewater purification treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320495315.9U CN203487002U (en) | 2013-08-14 | 2013-08-14 | Water-based ink wastewater purification treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203487002U true CN203487002U (en) | 2014-03-19 |
Family
ID=50257847
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320495315.9U Expired - Fee Related CN203487002U (en) | 2013-08-14 | 2013-08-14 | Water-based ink wastewater purification treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203487002U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105800864A (en) * | 2015-05-27 | 2016-07-27 | 苏州澄江环境科技有限公司 | Zero discharge method for waste liquid of water-based ink |
| CN105819615A (en) * | 2015-05-27 | 2016-08-03 | 苏州澄江环境科技有限公司 | Method for processing water-based ink waste liquid |
-
2013
- 2013-08-14 CN CN201320495315.9U patent/CN203487002U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105800864A (en) * | 2015-05-27 | 2016-07-27 | 苏州澄江环境科技有限公司 | Zero discharge method for waste liquid of water-based ink |
| CN105819615A (en) * | 2015-05-27 | 2016-08-03 | 苏州澄江环境科技有限公司 | Method for processing water-based ink waste liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| 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: 20140319 |