CN105417692A - Water distribution temperature control and automatic stirring and mixing apparatus used for water treatment anaerobic acidification technology - Google Patents
Water distribution temperature control and automatic stirring and mixing apparatus used for water treatment anaerobic acidification technology Download PDFInfo
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- CN105417692A CN105417692A CN201510664909.1A CN201510664909A CN105417692A CN 105417692 A CN105417692 A CN 105417692A CN 201510664909 A CN201510664909 A CN 201510664909A CN 105417692 A CN105417692 A CN 105417692A
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- water
- automatic stirring
- anaerobic
- cloth
- interchanger
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 187
- 238000003756 stirring Methods 0.000 title claims abstract description 56
- 230000020477 pH reduction Effects 0.000 title claims abstract description 22
- 238000002156 mixing Methods 0.000 title claims abstract description 19
- 238000005516 engineering process Methods 0.000 title abstract description 5
- 238000000034 method Methods 0.000 claims description 35
- 239000004744 fabric Substances 0.000 claims description 33
- 239000002253 acid Substances 0.000 claims description 28
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 14
- 241000894006 Bacteria Species 0.000 abstract description 11
- 239000002351 wastewater Substances 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 2
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 230000035939 shock Effects 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 5
- 239000010865 sewage Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000013632 homeostatic process Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The present invention provides a water distribution temperature control and automatic stirring and mixing apparatus used for a water treatment anaerobic acidification technology. The apparatus comprises an anaerobic acidification tank, a water temperature controlling component and an automatic stirring component, wherein the water temperature controlling component is connected to the anaerobic acidification tank, the automatic stirring component is connected to the water temperature controlling component, the water temperature controlling component comprises a circulating water connecting pipe, a heat exchanger and a thermostatic heater, the circulating water connecting pipe connects a circulating water outlet in the anaerobic acidification tank with a heat exchanger, and the heat exchanger is connected to the thermostatic heater. Compared with the prior art, the water distribution temperature control and automatic stirring and mixing apparatus provided by the present invention is used in the water treatment anaerobic acidification technology. The apparatus can control the inlet water temperature in a constant predetermined order-of-magnitude range, and water and bacteria in a tank in the water distribution and anaerobic acidification technology are in contact with each other fully and mixed uniformly by the automatic stirring component. In addition, the apparatus is high in shock loading resistance, low in power consumption and high in volume load treatment capability, self circulating in the material tank can be realized, and the CODcr elimination rate in wastewater can reach 75-80%.
Description
Technical field
The present invention relates to sewage treatment area, the cloth water temp of particularly a kind of water treatment Removal Rate in Anaerobic Acid application controls and automatic stirring mixing device.
Background technology
Many industrial trades have the used water difficult to degradate discharging middle and high difficulty, this kind of waste water organic loading is high, biological degradability is poor, majority contains toxicant, produce larger threat to environment and human health after being discharged into natural water, be a difficult problem for wastewater treatment always.Removal Rate in Anaerobic Acid can by the organic matter degradation of macromole in sewage and not easily biochemical degradation for being easy to biodegradable small organic molecule.Small organic molecule is easily entered in thalline by cytolemma and carries out biochemical metabolism, and follow-up aerobic unit or anaerobic unit were processed with less energy consumption and the shorter residence time.Therefore, in sewage disposal particularly During Industrial Wastewater Treatment Process, Removal Rate in Anaerobic Acid is used widely.
The Removal Rate in Anaerobic Acid of prior art is in process high-concentration waste water process, and the water distribution of former water, can not water distribution continuously uniformly often because the precipitation of mud produces and to block and water distribution is affected, and water is fully contacted with bacterium.Reaching water to intake fully to contact with bacterium, fully mixing, also need to arrange stirring system in addition, thus perplex the CODcr clearance in Removal Rate in Anaerobic Acid waste water always.
Summary of the invention
For the problems referred to above, the cloth water temp that the invention provides the application of a kind of water treatment Removal Rate in Anaerobic Acid controls and automatic stirring mixing device, this device can control inflow temperature, water distribution is fully contacted with bacterium with the water in tank in Removal Rate in Anaerobic Acid, mix, improve the CODcr clearance in waste water.
The technical solution used in the present invention is:
A kind of cloth water temp of water treatment Removal Rate in Anaerobic Acid application controls and automatic stirring mixing device, comprise anaerobic acidification tank, water temperature control unit and automatic stirring assembly, water temperature control unit is connected with anaerobic acidification tank, automatic stirring assembly is connected with water temperature control unit, water temperature control unit comprises recirculated water pipe connecting, interchanger and constent temperature heater, circulating water outlet in recirculated water pipe connecting connection anaerobic acidification tank and interchanger, interchanger is connected with constent temperature heater.
Preferably, interchanger comprises multi-turn interchanger ring pipe, and the layering of interchanger ring pipe is superimposed upon in constent temperature heater.
Preferably, constent temperature heater comprises a thermostatic container, the layering of interchanger ring pipe is superimposed upon in thermostatic container, and thermostatic container heats the recirculated water flowed out from anaerobic acidification tank or lowers the temperature, and the circulating water temperature of outflow is controlled within the scope of a set order of magnitude.
Preferably, automatic stirring assembly comprises stirring pump, Venturi water controller and water distribution agitator, stirring pump is connected with constent temperature heater, Venturi water controller connects stirring pump and water distribution agitator, the water that self-constant temperature well heater flows out stirs through automatic stirring assembly, make water distribution fully contact with the water in tank in Removal Rate in Anaerobic Acid, bacterium, mix, improve the CODcr clearance in waste water.
More preferably, automatic stirring assembly comprises process water water inlet pipe further, Venturi water controller is connected with process water water inlet pipe, Venturi water controller sucks process water in process water water inlet pipe, process water is flow in water distribution agitator, makes to mix with the water that self-constant temperature well heater flows out through process water.
More preferably, process water water inlet pipe comprises a process water inlet, and process water inlet is arranged on the bottom of anaerobic acidification tank.
More preferably, water distribution agitator comprises a closed annular pipeline, a cloth water inlet and multiple cloth water out, cloth water inlet is arranged on one end of closed duct, cloth water inlet is communicated with Venturi water controller, cloth water out annularly pipeline tangent to periphery direction arrange, water like this after water distribution agitator stirs sprays according to tangential direction at cloth water out, drives tank inner bottom part water, bacterium rotation, impels water, bacterium fully contacts, mixes.
Compared with prior art, beneficial effect of the present invention is: the cloth water temp that the invention provides the application of a kind of water treatment Removal Rate in Anaerobic Acid controls and automatic stirring mixing device, be applied in water treatment Removal Rate in Anaerobic Acid, this device can control inflow temperature, inflow temperature is made to control within the scope of the given amount level of a homeostasis, and the water utilizing automatic stirring assembly to make in water distribution and Removal Rate in Anaerobic Acid in tank, bacterium fully contacts, mix, capacity of resisting impact load is strong in addition, repeats itself in material pot can be realized, energy consumption is low, volumetric loading processing power is high, in waste water, CODcr clearance can reach 75-80%.
Accompanying drawing explanation
Fig. 1 is that the cloth water temp of a kind of water treatment Removal Rate in Anaerobic Acid application provided by the invention controls the schematic diagram with automatic stirring mixing device.
Embodiment
With reference to the accompanying drawings preferred implementation provided by the invention is illustrated.
Fig. 1, for the cloth water temp of a kind of water treatment Removal Rate in Anaerobic Acid application provided by the invention controls the preferred implementation with automatic stirring mixing device.As shown in Figure 1, the cloth water temp of this water treatment Removal Rate in Anaerobic Acid application controls and automatic stirring mixing device, be applied in water treatment Removal Rate in Anaerobic Acid, this device comprises anaerobic acidification tank 10, water temperature control unit 20 and automatic stirring assembly 30, water temperature control unit 20 is connected with anaerobic acidification tank 10, automatic stirring assembly 30 is connected with water temperature control unit 20, water temperature control unit 20 controls inflow temperature, inflow temperature is made to control within the scope of the given amount level of a homeostasis, water in the water that the automatic stirring assembly 30 pairs of water temperature control units 20 flow out and Removal Rate in Anaerobic Acid in tank, make the water in tank in water distribution and Removal Rate in Anaerobic Acid, bacterium fully contacts, mix, improve the CODcr clearance in waste water.
Water temperature control unit 20 comprises recirculated water pipe connecting 21, interchanger 22 and constent temperature heater 23, and recirculated water pipe connecting 21 connects circulating water outlet 11 in anaerobic acidification tank 10 and interchanger 22, and interchanger 22 is connected with constent temperature heater 23.Interchanger 22 comprises multi-turn interchanger ring pipe, and the layering of interchanger ring pipe is superimposed upon in constent temperature heater 23.Constent temperature heater 23 comprises a thermostatic container, and the layering of interchanger ring pipe is superimposed upon in thermostatic container, and thermostatic container heats the recirculated water flowed out from anaerobic acidification tank or lowers the temperature, and the circulating water temperature of outflow is controlled within the scope of a set order of magnitude.
Automatic stirring assembly 30 comprises stirring pump 31, Venturi water controller 32 and water distribution agitator 33, stirring pump 31 is connected with constent temperature heater 23, Venturi water controller 32 connects stirring pump 31 and water distribution agitator 33, the water that self-constant temperature well heater 23 flows out stirs through automatic stirring assembly 30, water distribution is mixed with the water in tank in Removal Rate in Anaerobic Acid, improves the CODcr clearance in waste water.
Automatic stirring assembly 30 comprises process water water inlet pipe 34 further, Venturi water controller 32 is connected with process water water inlet pipe 34, Venturi water controller 32 sucks process water in process water water inlet pipe 34, process water is flow in water distribution agitator 33, makes to mix with the water that self-constant temperature well heater 23 flows out through process water.Process water water inlet pipe 34 comprises a process water inlet 341, and process water inlet 341 is arranged on the bottom of anaerobic acidification tank 10.
Water distribution agitator 33 comprises a closed annular pipeline, a cloth water inlet and multiple cloth water out, cloth water inlet is arranged on one end of closed duct, cloth water inlet is communicated with Venturi water controller 32, cloth water out annularly pipeline tangent to periphery direction arrange, water like this after water distribution agitator stirs sprays according to tangential direction at cloth water out, drive tank inner bottom part water, bacterium rotation, impel water, bacterium fully contacts, mix.
It should be noted that described Venturi water controller 32 adds water is the power utilizing water inlet stirring pump 31, makes Venturi water controller 32 suction port produce the characteristic of negative pressure, sucks and suck process water in the process that recirculated water is uniformly mixed in process water water inlet pipe 34.
This cloth water temp controls: the water that the circulating water outlet 11 of anaerobic acidification tank 10 flows out enters interchanger 22 through the recirculated water pipe connecting 21 of water temperature control unit must in interchanger ring pipe, constent temperature heater 23 is a thermostatic container, the interchanger ring pipe layering of interchanger 22 is superimposed upon in thermostatic container, circulating water heating in thermostatic container heat exchanger ring pipe or cooling, make the circulating water temperature of outflow control within the scope of a set order of magnitude; The recirculated water that self-constant temperature well heater 23 flows out flows in the stirring pump 31 of automatic stirring assembly 30, Venturi water controller 32 is entered after stirring pump 31 pressurizes, Venturi water controller 32 sucks process water from process water water inlet pipe 34, by the circulating water flow after process water and process in water distribution agitator 33, finally tangentially spray at the cloth water out of water distribution agitator 33, form power, such realization is to recirculated water and the stirring processing water, water distribution is mixed with the water in tank in Removal Rate in Anaerobic Acid, improves the CODcr clearance in waste water.
In sum, technical scheme of the present invention can fully effectively realize foregoing invention object, and structure of the present invention and the principle of work and power are all verified in an embodiment fully, effect and the object of expection can be reached, under the prerequisite not deviating from principle of the present invention and essence, various changes or modifications can be made to inventive embodiment.Therefore, the present invention includes all in patent claim mention all replacement contents in scope, any equivalence change done in the present patent application the scope of the claims, within the scope of the claims all belonging to this case application.
Claims (7)
1. the cloth water temp of a water treatment Removal Rate in Anaerobic Acid application controls and automatic stirring mixing device, it is characterized in that, comprise: anaerobic acidification tank, water temperature control unit and automatic stirring assembly, water temperature control unit is connected with anaerobic acidification tank, automatic stirring assembly is connected with water temperature control unit, water temperature control unit comprises recirculated water pipe connecting, interchanger and constent temperature heater, and the circulating water outlet in recirculated water pipe connecting connection anaerobic acidification tank and interchanger, interchanger is connected with constent temperature heater.
2. the cloth water temp of water treatment Removal Rate in Anaerobic Acid application according to claim 1 controls and automatic stirring mixing device, and it is characterized in that: interchanger comprises multi-turn interchanger ring pipe, the layering of interchanger ring pipe is superimposed upon in constent temperature heater.
3. the cloth water temp of water treatment Removal Rate in Anaerobic Acid application according to claim 2 controls and automatic stirring mixing device, and it is characterized in that: constent temperature heater comprises a thermostatic container, the layering of interchanger ring pipe is superimposed upon in thermostatic container.
4. the cloth water temp of water treatment Removal Rate in Anaerobic Acid application according to claim 1 controls and automatic stirring mixing device, it is characterized in that: automatic stirring assembly comprises stirring pump, Venturi water controller and water distribution agitator, stirring pump is connected with constent temperature heater, and Venturi water controller connects stirring pump and water distribution agitator.
5. the cloth water temp of water treatment Removal Rate in Anaerobic Acid application according to claim 4 controls and automatic stirring mixing device, it is characterized in that: automatic stirring assembly comprises process water water inlet pipe further, Venturi water controller is connected with process water water inlet pipe, and Venturi water controller sucks process water in process water water inlet pipe.
6. the cloth water temp of water treatment Removal Rate in Anaerobic Acid application according to claim 5 controls and automatic stirring mixing device, it is characterized in that: process water water inlet pipe comprises a process water inlet, and process water inlet is arranged on the bottom of anaerobic acidification tank.
7. the cloth water temp of water treatment Removal Rate in Anaerobic Acid application according to claim 5 controls and automatic stirring mixing device, it is characterized in that: water distribution agitator comprises a closed annular pipeline, a cloth water inlet and multiple cloth water out, cloth water inlet is arranged on one end of closed duct, and cloth water inlet is communicated with Venturi water controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510664909.1A CN105417692A (en) | 2015-10-14 | 2015-10-14 | Water distribution temperature control and automatic stirring and mixing apparatus used for water treatment anaerobic acidification technology |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510664909.1A CN105417692A (en) | 2015-10-14 | 2015-10-14 | Water distribution temperature control and automatic stirring and mixing apparatus used for water treatment anaerobic acidification technology |
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| CN105417692A true CN105417692A (en) | 2016-03-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510664909.1A Pending CN105417692A (en) | 2015-10-14 | 2015-10-14 | Water distribution temperature control and automatic stirring and mixing apparatus used for water treatment anaerobic acidification technology |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797627A (en) * | 2016-04-29 | 2016-07-27 | 苏州优迪邦智能科技股份有限公司 | Water purifying solution generator |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07108295A (en) * | 1993-10-13 | 1995-04-25 | Shinichi Nakamura | Pressurized aeration treatment device for waste water |
| JPH09248592A (en) * | 1996-03-13 | 1997-09-22 | Maezawa Ind Inc | Waste water treating device |
| CN2741973Y (en) * | 2004-11-22 | 2005-11-23 | 马三剑 | High efficiency combined water distributor |
| CN101982430A (en) * | 2010-10-19 | 2011-03-02 | 江苏省环境科学研究院 | Novel concentric anaerobic baffled hydrolytic reactor |
| CN102120646A (en) * | 2011-04-14 | 2011-07-13 | 北京杰佳洁环境技术有限责任公司 | Efficient anaerobic biological tower reactor |
| CN102897911A (en) * | 2012-11-05 | 2013-01-30 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN202808476U (en) * | 2012-03-23 | 2013-03-20 | 太平洋水处理工程有限公司 | Emptying-free anaerobic water distribution device |
| CN203498161U (en) * | 2013-10-10 | 2014-03-26 | 肇庆福田化学工业有限公司 | Anaerobic tank for resin sewage treatment |
-
2015
- 2015-10-14 CN CN201510664909.1A patent/CN105417692A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07108295A (en) * | 1993-10-13 | 1995-04-25 | Shinichi Nakamura | Pressurized aeration treatment device for waste water |
| JPH09248592A (en) * | 1996-03-13 | 1997-09-22 | Maezawa Ind Inc | Waste water treating device |
| CN2741973Y (en) * | 2004-11-22 | 2005-11-23 | 马三剑 | High efficiency combined water distributor |
| CN101982430A (en) * | 2010-10-19 | 2011-03-02 | 江苏省环境科学研究院 | Novel concentric anaerobic baffled hydrolytic reactor |
| CN102120646A (en) * | 2011-04-14 | 2011-07-13 | 北京杰佳洁环境技术有限责任公司 | Efficient anaerobic biological tower reactor |
| CN202808476U (en) * | 2012-03-23 | 2013-03-20 | 太平洋水处理工程有限公司 | Emptying-free anaerobic water distribution device |
| CN102897911A (en) * | 2012-11-05 | 2013-01-30 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN203498161U (en) * | 2013-10-10 | 2014-03-26 | 肇庆福田化学工业有限公司 | Anaerobic tank for resin sewage treatment |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797627A (en) * | 2016-04-29 | 2016-07-27 | 苏州优迪邦智能科技股份有限公司 | Water purifying solution generator |
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Application publication date: 20160323 |
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