CN106745795A - A kind of full-automatic wastewater processes bio-synergistic device - Google Patents
A kind of full-automatic wastewater processes bio-synergistic device Download PDFInfo
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- CN106745795A CN106745795A CN201610616377.9A CN201610616377A CN106745795A CN 106745795 A CN106745795 A CN 106745795A CN 201610616377 A CN201610616377 A CN 201610616377A CN 106745795 A CN106745795 A CN 106745795A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/348—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
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- Biological Treatment Of Waste Water (AREA)
Abstract
The present invention relates to a kind of full-automatic wastewater treatment bio-synergistic device, including organic frame, control unit, inlet unit, waste water unit, acid-base accommodation unit, strain unit, nutrient solution unit, nutrient solution unit, dispensing unit, aeration unit, cycling element;The culture bucket bucket wall of the nutrient solution unit is by respective magnetic valve and acid-base accommodation unit, strain unit, the pipeline joint of nutrient solution unit, the pipeline of the inlet unit, the pipeline of waste water unit are connected directly between on culture bucket bucket wall, the pipeline for delivering unit, the pipeline of the cycling element are connected by the both sides mouth of pipe of three-way pipe with the delivery outlet of nutrient solution unit respectively, and the jet aerator of the aeration unit is connected on the pipeline section of return culture bucket of circulation line.The present invention has concentrated all links in treatment wastewater biological synergy:In-place activation, culture, the processing step of domestication, then the step of persistently adding microorganism is realized by double settings for cultivating buckets, multiple steps can link up by once, achieve significant progress.
Description
Technical field
The present invention relates to the treatment of a kind of water, waste water, sewage or mud, bio-synergistic device is processed more specifically to a kind of full-automatic wastewater.
Background technology
Useless Organic substance in water is converted into simple inorganic matter by the main decomposition by microorganism of biological wastewater treatment, is purified waste water.Further to improve the decomposition of microorganism, bio-synergistic technology is introduced again, being introduced in wastewater treatment process has the complex microbial community of efficient degradation ability to specific pollutants, improve micro organism quantity, improve microbiological paper method, enhancing waste water system improves water treatment effect to the degradation capability of specific pollutants, enhancing stable water outlet, while system recovery can also be accelerated.But it is difficult in specific implementation process, trace it to its cause, expansion in the prior art to microorganism is numerous, reinforcing, culture, domestication etc. can not be managed collectively, and fluctuation of service causes the inactivation of microorganism, cultivation cycle is long, poor processing effect, hinders the further development of bio-synergistic.This is the problem that this application is expected to solve.
The content of the invention
The purpose of the present invention is directed to prior art weak point and provides a kind of full-automatic wastewater treatment bio-synergistic device.Device energy in-place activation, culture, the acclimated microorganism, and persistently can be added in Waste Water Treatment, so as to greatly improve the effect of continued biological synergy, reduce the cost of bio-synergistic.
The purpose of the present invention can be realized by following measures:A kind of full-automatic wastewater processes bio-synergistic device, including organic frame, control unit, inlet unit, waste water unit, characterized in that, also acid-base accommodation unit, strain unit, nutrient solution unit, nutrient solution unit, deliver unit, aeration unit, cycling element, wherein:
The acid-base accommodation unit adjusts pipeline containing alkali lye, acid solution adjusts pipeline, pH sensors, soda acid control module, the alkali lye regulation pipe route alkali storage tank, and connected alkali lye measuring pump, alkali lye delivery outlet is constituted, the sour basin of acid solution regulation pipe route, and connected acid solution measuring pump, acid solution delivery outlet is constituted, soda acid control module by alkali lye measuring pump control signal port, the signal port of the alkali lye magnetic valve on culture bucket bucket wall, acid solution measuring pump control signal port, the signal port of the acid solution magnetic valve on culture bucket bucket wall, pH sensor signals output port is constituted;
The strain unit adds pipeline, strain and adds control module containing strain, the strain adds pipeline and is added delivery outlet and constituted by strain basin and connected strain measuring pump, strain, and strain adds control module and is made up of the signal port of strain magnetic valve on culture bucket bucket wall, the control signal port of strain measuring pump;
The nutrient solution unit adds pipeline, nutrient solution and adds control module containing nutrient solution, the nutrient solution adds pipeline and is made up of nutrition liquid storage tank and connected nutrient solution measuring pump, nutrient input outlet spout, and nutrient solution adds control module and is made up of the signal port of nutrition liquid electromagnetic valve on culture bucket bucket wall, the control signal port of nutrient solution measuring pump;
The inlet unit contains inlet pipeline, inlet pipeline control module, the inlet pipeline by concatenation connection city's water supply interface, active carbon filter, ultra filtration filter, entering water electromagnetic valve, flowmeter, inlet channel outlet constitute, the inlet pipeline control module is made up of the metrical information port of flowmeter, the control signal port of entering water electromagnetic valve;
The waste water unit contains waste line, waste line control module, the waste line adds pump group and adds the metrical information port of pump, the control signal port of waste water magnetic valve by waste water metering into, the waste line control module and constitutes by the waste water interface of concatenation connection, waste water magnetic valve, effluent filter, waste water metering;
Dispensing unit pipeline containing dispensing, dispensing control module, the pipeline of delivering is made up of import and export side with the dispensing measuring pump for delivering magnetic valve, the dispensing control module is discharged the control signal port of magnetic valve by culture bucket, delivers the metrical information port of measuring pump, delivers measuring pump, and the control signal port of the dispensing magnetic valve of import and export side constitutes;
The cycling element contains circulation line, loop control module, the circulation line is made up of the circulating electromagnetic valve that is sequentially connected, circulation measuring pump, the pipeline section that is recycled back into cultivating bucket, and the loop control module is made up of the control signal port of the metrical information port of circulation measuring pump, the culture bucket discharge control signal port of magnetic valve, circulating electromagnetic valve;
The aeration unit contains aerating pipelines, aeration control module, the aerating pipelines are made up of dissolving oxidation sensors and the air inlet screen, air compressor, aeration electromagnetic valve and the jet aerator that are sequentially connected, and aeration control module is made up of the control signal port of the information output port of dissolving oxidation sensors, air compressor VFC port, aeration electromagnetic valve;
The culture unit is containing two culture buckets of alternate run,Electromagnetic Heating unit,Temperature control modules,Culture bucket selection control module,The culture bucket is three layers of wall construction,Intraformational bed is Electromagnetic Heating layer,Outside sandwich is heat-insulation layer,Culture bucket bucket wall is respectively equipped with and adjusts pipeline with alkali lye,Acid solution adjusts pipeline,Strain adds pipeline,Nutrient solution adds the alkali lye magnetic valve of pipeline joint,Acid solution magnetic valve,Strain magnetic valve,Nutrition liquid electromagnetic valve,Culture Tong Zhou centers are provided with perforated pipe,The port of export that perforated pipe overhangs culture bucket bucket bottom is provided with culture discharge magnetic valve,The Electromagnetic Heating unit is by heater element,Electric transducer,Temperature sensor is constituted,Heater element is along the intraformational bed distribution of culture bucket,The temperature control modules are by electrothermal transducer switch control terminal mouthful,Temperature sensor information output port is constituted,Culture bucket selects control module by alkali lye solenoid valve control signal port,Acid solution solenoid valve control signal port,Strain solenoid valve control signal port,Nutrient solution solenoid valve control signal port constitutes;
The culture bucket bucket wall adjusts pipeline by respective magnetic valve with alkali lye, acid solution adjusts pipeline, strain adds pipeline, nutrient solution adds pipeline joint, the inlet pipeline, waste line is connected directly between on culture bucket bucket wall, the dispensing magnetic valve for delivering measuring pump inlet side, the circulating electromagnetic valve of the circulation line inlet side is discharged magnetic valve delivery outlet and is connected by the both sides mouth of pipe of three-way pipe with culture bucket respectively, the jet aerator of the aerating pipelines is connected on the pipeline section for being recycled back into cultivate bucket of circulation line, circulation line with aerating pipelines by being inserted into after jet aerator cultivated on the bucket wall of bucket altogether by road;
The soda acid control module, strain add control module, nutrient solution and add the microprocessor that control module, inlet pipeline control module, waste line control module, dispensing control module, loop control module, aeration control module, temperature control modules, the input/output port of culture bucket selection control module connect control unit.
The pH sensors are arranged at the height of culture cylinder barrel 1/2 of nutrient solution unit.
The dissolving oxidation sensors of the aeration control module are arranged on the bucket wall of the culture height of bucket 1/2.
Aperture on the culture bucket axle central hole pipe sets up along helix.
The horizontal pipeline section for being recycled back into cultivating bucket pipeline section enters culture bucket at the culture height of bucket 2/3, tangentially.
The mesh of the aerating pipelines air inlet screen is 0.1 μm.
The inlet pipeline is connected directly between at the height of culture bucket bucket wall 3/4.
The waste line is connected directly between on culture bucket bucket wall at 2/3 height.
Compared with prior art, as a result of a kind of full-automatic wastewater treatment bio-synergistic device and method proposed by the present invention, have the following advantages that:1)The present invention has concentrated all links in treatment wastewater biological synergy:In-place activation, culture, domestication processing step, then by it is double culture buckets settings realize the step of persistently adding microorganism, multiple steps can link up by once, it is convenient, efficient, install and it is easy to maintenance, reduce production cost, achieve significant progress;2)Unit of the invention can such as be changed different strains, configure different nutrient solutions, select different dispensing modes according to field condition from main regulation, carry out the setting of individual character, save the time of aided process, improve work efficiency.
Brief description of the drawings:
Fig. 1 is one embodiment structural representation proposed by the present invention.
Specific embodiment:
Specific embodiment is elaborated below in conjunction with the accompanying drawings:In one embodiment of the present of invention shown in Fig. 1, a kind of full-automatic wastewater processes bio-synergistic device, including organic frame 1, control unit 2, inlet unit 7, waste water unit 8, acid-base accommodation unit 3, strain unit 5, nutrient solution unit 6, nutrient solution unit 9, dispensing unit 10, aeration unit 12, cycling element 11, wherein:
The acid-base accommodation unit adjusts pipeline containing alkali lye, acid solution adjusts pipeline, pH sensors, soda acid control module, the alkali lye regulation pipe route alkali storage tank 3a, and connected alkali lye measuring pump 3c, alkali lye delivery outlet is constituted, the sour basin 4a of acid solution regulation pipe route, and connected acid solution measuring pump 4c, acid solution delivery outlet is constituted, soda acid control module by alkali lye measuring pump 3c control signal port, alkali lye magnetic valve 3b on culture bucket bucket wall, acid solution measuring pump 4c control signals port, soda acid magnetic valve 4b on culture bucket bucket wall, pH sensor signals output port is constituted.The pH sensors are arranged at the height of culture cylinder barrel 1/2 of nutrient solution unit.Signal is provided in this structure by pH sensors to be adjusted, when lower bound of the training oxygen environment pH value less than setting range, automatically open up alkali lye measuring pump 3c and alkali lye magnetic valve 3b, metering adds alkali lye, until culture environment pH value reaches the lower limit of the scope of setting, alkali lye magnetic valve 3b and alkali lye measuring pump 3c is closed;When environment pH is prescribed a time limit higher than the height of setting range, acid solution measuring pump 4c and soda acid magnetic valve 4b is automatically opened up, metering adds acid solution, until lower limit of the environment pH less than setting range, closes soda acid magnetic valve 4b and acid solution measuring pump 4c.Generally, the pH control ranges of culture environment need to carry out personalized setting according to the strain of culture in control panel.
The strain unit 5 adds pipeline, strain and adds control module containing strain, the strain adds pipeline and is added delivery outlet and constituted by strain basin 5a and connected strain measuring pump 5c, strain, and strain adds control module and is made up of the signal port of strain magnetic valve 5b on culture bucket bucket wall, the control signal port of strain measuring pump 5c.In this configuration, when a cultivation cycle starts, strain measuring pump and strain magnetic valve are opened, metering adds strain.When dosage reaches the quantity of setting, measuring pump and strain magnetic valve are automatically switched off.
The nutrient solution unit 6 adds pipeline, nutrient solution and adds control module containing nutrient solution, the nutrient solution adds pipeline and is made up of nutrition liquid storage tank 6a and connected nutrient solution measuring pump 6c, nutrient input outlet spout, and nutrient solution adds control module and is made up of the signal port of nutrition liquid electromagnetic valve 6b on culture bucket bucket wall, the control signal port of nutrient solution measuring pump 6c.In this structure, when one is cultivated batch starts, under the control of nutrient solution control module, nutrient solution measuring pump and nutrition liquid electromagnetic valve are opened, metering adds nutrient solution.After adding end, nutrient solution measuring pump and nutrition liquid electromagnetic valve are automatically switched off.Nutrient solution prescription and dosage need to carry out personalized setting according to specific bio-synergistic method in control panel.
The inlet unit 7 contains inlet pipeline, inlet pipeline control module, the inlet pipeline is made up of the city water supply interface 7a of concatenation connection, active carbon filter 7b, ultra filtration filter 7c, entering water electromagnetic valve 7d, flowmeter 7e, inlet channel outlet, and the inlet pipeline control module is made up of the metrical information port of flowmeter 7e, the control signal port of entering water electromagnetic valve 7d.The inlet pipeline is connected directly between at the height of culture bucket bucket wall 3/4.Active carbon filter in this structure can remove the chlorine residue of municipal tap water end, and ultra filtration filter can remove the microorganism in municipal tap water, prevent from introducing miscellaneous bacteria in incubation.Amount of inlet water need to carry out personalized setting according to specific bio-synergistic method in control panel.
The waste water unit 8 contains waste line, waste line control module, the waste line is added pump 8d and is constituted by the waste water interface 8a of concatenation connection, waste water magnetic valve 8b, effluent filter 8c, waste water metering, and the waste line control module adds the metrical information port of pump 8d, the control signal port of waste water magnetic valve 8b and constitutes by waste water metering.The outlet that the waste water metering adds pump is connected directly between on culture bucket bucket wall at 2/3 height.In this structure, when one is cultivated batch proceeds to the domestication stage, automatically open up waste water metering and add pump and waste water magnetic valve, metering adds waste water, after adding end, is automatically switched off metering and adds pump and waste water magnetic valve.Waste water dosage need to carry out personalized setting according to specific bio-synergistic method in control panel.
Dispensing unit 10 pipeline containing dispensing, dispensing control module, the pipeline of delivering is made up of import and export side with the dispensing measuring pump 10b for delivering magnetic valve 10a, 10c, and the control module of delivering is made up of the control signal port of culture bucket discharge magnetic valve 9c, the metrical information port for delivering measuring pump 10b, the control signal port of dispensing magnetic valve 10a, 10c of import and export side of delivering measuring pump.In this structure, in order to reduce influence of the pressure change to microorganism, metering adds pump and uses peristaltic pump.The dosage of bio-synergistic bacterium solution need to be set according to bio-synergistic method in control panel.
The cycling element 11 contains circulation line, loop control module, the circulation line is made up of the circulating electromagnetic valve 11a that is sequentially connected, circulation measuring pump 11b, the pipeline section 11c that is recycled back into cultivating bucket, and the loop control module is made up of the metrical information port of circulation measuring pump 11b, the control signal port of culture bucket discharge magnetic valve 9c, the control signal port of circulating electromagnetic valve 11a.The horizontal pipeline section for being recycled back into cultivating bucket pipeline section tangentially enters culture bucket at the culture height of bucket 2/3.
The aeration unit 12 contains aerating pipelines, aeration control module, the aerating pipelines are made up of dissolving oxidation sensors 9f and the air inlet screen 12a, air compressor 12b, aeration electromagnetic valve 12d and the jet aerator 12e that are sequentially connected, and aeration control module constitutes by the control signal port of the information output port of dissolving oxidation sensors 9f, air compressor 12b VFC port, aeration electromagnetic valve 12d.The dissolving oxidation sensors of the aeration control module are arranged on the bucket wall of the culture height of bucket 1/2.The mesh of the aerating pipelines air inlet screen is 0.1 μm, can avoid the miscellaneous bacteria being introduced into because of aeration in air.In this structure, air compressor goes out the suction nozzle that gas tank is connected to jet-flow aeration, the effect for improving jet-flow aeration, and compared with traditional Aeration fan and micro-pore aeration, dissolved oxygen concentration in increase system greatly reduces aeration failure.When the information that dissolving oxidation sensors are obtained:When dissolved oxygen is less than culture control range lower limit, aeration control module automatically speeds up compressor operation, until dissolved oxygen reaches culture control range lower limit.When dissolved oxygen is higher than the culture control range upper limit, aeration control module automatic retarding compressor operation, until dissolved oxygen is less than the control range upper limit.The dissolved oxygen control range of culture environment need to carry out personalized setting according to the strain of culture in control panel.
The culture unit 9 is containing two culture bucket 9a of alternate run,Electromagnetic Heating unit,Temperature control modules,Culture bucket selection control module,The culture bucket 9a is three layers of wall construction,Intraformational bed is Electromagnetic Heating layer,Outside sandwich is heat-insulation layer,Culture bucket bucket wall is respectively equipped with and adjusts pipeline with alkali lye,Acid solution adjusts pipeline,Strain adds pipeline,Nutrient solution adds the alkali lye magnetic valve 3b of pipeline joint,Acid solution magnetic valve 4b,Strain magnetic valve 5b,Nutrition liquid electromagnetic valve 6b,Culture Tong Zhou centers are provided with perforated pipe 9b,The port of export that perforated pipe overhangs culture bucket bucket bottom is provided with culture discharge magnetic valve 9c,The Electromagnetic Heating unit is by heater element,Electric transducer,Temperature sensor is constituted,Heater element is along culture bucket 9a intraformational bed distributions,The temperature control modules are by electrothermal transducer switch control terminal mouthful,Temperature sensor information output port is constituted,Culture bucket selects control module by alkali lye solenoid valve control signal port 3b,Acid solution magnetic valve 4b control signals port,Strain magnetic valve 5b control signals port,Nutrition liquid electromagnetic valve 6b control signals port constitutes.Aperture on the culture bucket axle central hole pipe sets up along helix.In this structure, it is uniformly heated using the culture bucket of Electromagnetic Heating mode, medium is heated also evenly in culture bucket, and the efficiency of heating surface is also higher.When lower limit of the culture environment temperature less than control temperature range, Electromagnetic Heating switch is automatically opened up, until cultivation temperature reaches the lower limit of control temperature range.The temperature controlling range of culture environment need to carry out personalized setting according to the strain of culture in control panel.Culture bucket selection control module in this structure is so work, and two culture buckets are designed with respective alkali lye magnetic valve, acid solution magnetic valve, strain magnetic valve, nutrition liquid electromagnetic valve, the magnetic valve of itself is opened during selection.
9a barrels of wall of the culture bucket adjusts pipeline by respective magnetic valve with alkali lye, acid solution adjusts pipeline, strain adds pipeline, nutrient solution adds pipeline joint, the inlet pipeline, waste line is connected directly between on culture 9a barrels of wall of bucket, the dispensing magnetic valve 10c for delivering measuring pump 10b inlet sides, the circulating electromagnetic valve 11a of the circulation line inlet side discharges magnetic valve 9c delivery outlets and is connected by the both sides mouth of pipe of three-way pipe with culture bucket 9a respectively, the jet aerator 12e of the aerating pipelines is connected on the pipeline section 11c for being recycled back into cultivate bucket of circulation line, circulation line with aerating pipelines by being inserted into after jet aerator 12e cultivated on the bucket wall of bucket 9a altogether by road.In this structure, show possess the bio-synergistic function that in-place activation, training are closed, tamed, microorganism is continuously added to Waste Water Treatment completely.
The soda acid control module, strain add control module, nutrient solution and add the microprocessor that control module, inlet pipeline control module, waste line control module, dispensing control module, loop control module, aeration control module, temperature control modules, the input/output port of culture bucket selection control module connect control unit.In this structure, connected with the microprocessor of control unit by the input/output port of each unit control module, realize the Automatic Control of the present apparatus.
Above-described embodiment is not construed as limiting the invention, all technical schemes obtained in the form of equivalent or equivalent transformation, is within the scope of the present invention.
Claims (8)
1. a kind of full-automatic wastewater processes bio-synergistic device, including organic frame, control unit, inlet unit, waste water unit, characterized in that, also acid-base accommodation unit, strain unit, nutrient solution unit, nutrient solution unit, deliver unit, aeration unit, cycling element, wherein:
The acid-base accommodation unit adjusts pipeline containing alkali lye, acid solution adjusts pipeline, pH sensors, soda acid control module, the alkali lye regulation pipe route alkali storage tank, and connected alkali lye measuring pump, alkali lye delivery outlet is constituted, the sour basin of acid solution regulation pipe route, and connected acid solution measuring pump, acid solution delivery outlet is constituted, soda acid control module by alkali lye measuring pump control signal port, the signal port of the alkali lye magnetic valve on culture bucket bucket wall, acid solution measuring pump control signal port, the signal port of the acid solution magnetic valve on culture bucket bucket wall, pH sensor signals output port is constituted;
The strain unit adds pipeline, strain and adds control module containing strain, the strain adds pipeline and is added delivery outlet and constituted by strain basin and connected strain measuring pump, strain, and strain adds control module and is made up of the signal port of strain magnetic valve on culture bucket bucket wall, the control signal port of strain measuring pump;
The nutrient solution unit adds pipeline, nutrient solution and adds control module containing nutrient solution, the nutrient solution adds pipeline and is made up of nutrition liquid storage tank and connected nutrient solution measuring pump, nutrient input outlet spout, and nutrient solution adds control module and is made up of the signal port of nutrition liquid electromagnetic valve on culture bucket bucket wall, the control signal port of nutrient solution measuring pump;
The inlet unit contains inlet pipeline, inlet pipeline control module, the inlet pipeline by concatenation connection city's water supply interface, active carbon filter, ultra filtration filter, entering water electromagnetic valve, flowmeter, inlet channel outlet constitute, the inlet pipeline control module is made up of the metrical information port of flowmeter, the control signal port of entering water electromagnetic valve;
The waste water unit contains waste line, waste line control module, the waste line adds pump group and adds the metrical information port of pump, the control signal port of waste water magnetic valve by waste water metering into, the waste line control module and constitutes by the waste water interface of concatenation connection, waste water magnetic valve, effluent filter, waste water metering;
Dispensing unit pipeline containing dispensing, dispensing control module, the pipeline of delivering is made up of import and export side with the dispensing measuring pump for delivering magnetic valve, the dispensing control module is discharged the control signal port of magnetic valve by culture bucket, delivers the metrical information port of measuring pump, delivers measuring pump, and the control signal port of the dispensing magnetic valve of import and export side constitutes;
The cycling element contains circulation line, loop control module, the circulation line is made up of the circulating electromagnetic valve that is sequentially connected, circulation measuring pump, the pipeline section that is recycled back into cultivating bucket, and the loop control module is made up of the control signal port of the metrical information port of circulation measuring pump, the culture bucket discharge control signal port of magnetic valve, circulating electromagnetic valve;
The aeration unit contains aerating pipelines, aeration control module, the aerating pipelines are made up of dissolving oxidation sensors and the air inlet screen, air compressor, aeration electromagnetic valve and the jet aerator that are sequentially connected, and aeration control module is made up of the control signal port of the information output port of dissolving oxidation sensors, air compressor VFC port, aeration electromagnetic valve;
The culture unit is containing two culture buckets of alternate run,Electromagnetic Heating unit,Temperature control modules,Culture bucket selection control module,The culture bucket is three layers of wall construction,Intraformational bed is Electromagnetic Heating layer,Outside sandwich is heat-insulation layer,Culture bucket bucket wall is respectively equipped with and adjusts pipeline with alkali lye,Acid solution adjusts pipeline,Strain adds pipeline,Nutrient solution adds the alkali lye magnetic valve of pipeline joint,Acid solution magnetic valve,Strain magnetic valve,Nutrition liquid electromagnetic valve,Culture Tong Zhou centers are provided with perforated pipe,The port of export that perforated pipe overhangs culture bucket bucket bottom is provided with culture discharge magnetic valve,The Electromagnetic Heating unit is by heater element,Electric transducer,Temperature sensor is constituted,Heater element is along the intraformational bed distribution of culture bucket,The temperature control modules are by electrothermal transducer switch control terminal mouthful,Temperature sensor information output port is constituted,Culture bucket selects control module by alkali lye solenoid valve control signal port,Acid solution solenoid valve control signal port,Strain solenoid valve control signal port,Nutrient solution solenoid valve control signal port constitutes;
The culture bucket bucket wall adjusts pipeline by respective magnetic valve with alkali lye, acid solution adjusts pipeline, strain adds pipeline, nutrient solution adds pipeline joint, the inlet pipeline, waste line is connected directly between on culture bucket bucket wall, the dispensing magnetic valve for delivering measuring pump inlet side, the circulating electromagnetic valve of the circulation line inlet side is discharged magnetic valve delivery outlet and is connected by the both sides mouth of pipe of three-way pipe with culture bucket respectively, the jet aerator of the aerating pipelines is connected on the pipeline section for being recycled back into cultivate bucket of circulation line, circulation line with aerating pipelines by being inserted into after jet aerator cultivated on the bucket wall of bucket altogether by road;
The soda acid control module, strain add control module, nutrient solution and add the microprocessor that control module, inlet pipeline control module, waste line control module, dispensing control module, loop control module, aeration control module, temperature control modules, the input/output port of culture bucket selection control module connect control unit.
2. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the pH sensors are arranged at the height of culture cylinder barrel 1/2 of nutrient solution unit.
3. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the dissolving oxidation sensors of the aeration control module are arranged on the bucket wall of the culture height of bucket 1/2.
4. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the aperture on the culture bucket axle central hole pipe sets up along helix.
5. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the horizontal pipeline section for being recycled back into cultivating bucket pipeline section tangentially enters culture bucket at the culture height of bucket 2/3.
6. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the mesh of the aerating pipelines air inlet screen is 0.1 μm.
7. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the inlet pipeline is connected directly between at the height of culture bucket bucket wall 3/4.
8. full-automatic wastewater according to claim 1 processes bio-synergistic system, it is characterised in that the outlet that the waste water metering adds pump is connected directly between on culture bucket bucket wall at 2/3 height.
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CN108148745A (en) * | 2018-03-16 | 2018-06-12 | 沈阳东源环境科技有限公司 | A kind of device using a variety of livestock products coprocultures purification aerobic bacteria |
CN109576133A (en) * | 2018-12-26 | 2019-04-05 | 湖北省长江水生态研究院有限责任公司 | A kind of microbial bacterial agent culture apparatus and cultural method |
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Application publication date: 20170531 |