CN107032486A - The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter - Google Patents

The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter Download PDF

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Publication number
CN107032486A
CN107032486A CN201710400957.9A CN201710400957A CN107032486A CN 107032486 A CN107032486 A CN 107032486A CN 201710400957 A CN201710400957 A CN 201710400957A CN 107032486 A CN107032486 A CN 107032486A
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China
Prior art keywords
water
filter tank
chip microcomputer
level sensor
inlet
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Withdrawn
Application number
CN201710400957.9A
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Chinese (zh)
Inventor
王敦球
秦建华
李稳
邓晨韵
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Guilin University of Technology
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Guilin University of Technology
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Priority to CN201710400957.9A priority Critical patent/CN107032486A/en
Publication of CN107032486A publication Critical patent/CN107032486A/en
Withdrawn legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/006Regulation methods for biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/2846Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/001Upstream control, i.e. monitoring for predictive control
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/02Temperature
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/08Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/28CH4
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/38Gas flow rate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/40Liquid flow rate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/42Liquid level
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/10Temperature conditions for biological treatment
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

A kind of Inlet and outlet water measurement and control system of up-flow anaerobic biofilter of the present invention, including filter tank, in addition to the detection means being arranged in filter tank, and the single-chip computer control system being connected with detection means;The detection means includes liquid level sensor, temperature sensor, level sensor, gas flowmeter;Each detection means is connected with single-chip microcomputer respectively, and its work is controlled by single-chip microcomputer.The present invention accurately controls water by detecting the water of Inlet and outlet water, reduces filter tank blocking, current short circuit phenomenon, improves the efficiency of its sewage disposal.

Description

The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter
Technical field
The present invention relates to sewage treatment control system, specifically a kind of Inlet and outlet water Detection & Controling of up-flow anaerobic biofilter System.
Background technology
In numerous treatment technologies of sewage, anaerobic bio-treated is reduced investment, starts quick, processing efficiently, without outer One of technology of power, is widely used always, and up-flow anaerobic biofilter (AF) is in traditional anaerobic activated sludge method On the basis of grow up, in recent years and more applied in Practical Project, particularly medium and small project.Up-flow anaerobism is given birth to Thing filter tank, water enters from reactor bottom, and after bottom of pond water distribution system is evenly arranged, waste water passes sequentially through the sludge blanket of suspension With the biological filter bed of material, organic matter is contacted with the microorganism on sludge and biomembrane, fixed, is then resolved, water is again from pond face Water outlet water charging system is uniformly discharged, into next level processor.
Experience have shown that, under identical condition of water quality and hydraulic detention time, the C0Dcr of up-flow anaerobic biofilter is gone Except rate is higher than down-flow anaerobic filter, it is confirmed as the anaerobic organism in high-rate anaerobic reactor, therefore practice Using up-flow anaerobic biofilter more in the filter tank.
In anaerobic biofilter there is very big difference in biosolids concentration with the difference of packed height.Up-flow anaerobism The biosolids concentration of biofilter bottom is sometimes tens times of its top biosolids concentration, and bottom part easily occurs and filled out Water stream channel blocking, current short circuit phenomenon, influence treatment effeciency between material.
In addition, the normal operation of anaerobic biofilter processing system depends on the relative equilibrium of production acid and methane phase speed, Organic loading is too high, then acid production rate is possible to more than methane phase with sour rate, so as to cause under the accumulation of volatile acid makes pH rapid Drop, hinders being normally carried out for methane phase stage, can cause " to be acidified " when serious.Because the capacity of whole processing system is limited , the water inlet of reactor need to be controlled strictly, otherwise will greatly prolong the startup time.Therefore up-flow anaerobic biofilter is entered It is imperative that water outlet is detected and controlled.
The content of the invention
In order to overcome the above-mentioned technical problem that up-flow anaerobic biofilter is present, the present invention provides a kind of up-flow anaerobism The Inlet and outlet water measurement and control system of biofilter, by detecting the water of Inlet and outlet water, and then accurately controls water, reduces filter tank Blocking, current short circuit phenomenon, improve the efficiency of its sewage disposal.
Realizing the technical scheme of the object of the invention is:
A kind of Inlet and outlet water measurement and control system of up-flow anaerobic biofilter, including filter tank, in addition to be arranged in filter tank Detection means, and the single-chip computer control system being connected with detection means;
The detection means includes liquid level sensor, temperature sensor, level sensor, gas flowmeter;
The inwall in the filter tank, is equidistantly provided with liquid level sensor, the change for detecting flow of inlet water from water inlet to delivery port Change the change with influent COD value;
The inwall in filter tank is additionally provided with temperature sensor, for detecting filter tank temperature, controls the water temperature in filter tank at 35-38 DEG C;
The bottom in filter tank sets water intaking valve, controls the size of inflow;
The top in filter tank sets and level sensor is set on buoy, buoy, and whether the water in detection filter tank reaches safety water volume model Enclose;
The top in filter tank is additionally provided with outlet valve, controls the size of water yield;
The top in filter tank sets water-sealed drainage bottle, is additionally provided with gas flowmeter and is connected with water-sealed drainage bottle, and water-sealed drainage bottle is collected filter and produced Gas and filter miscellaneous gas prevent influence detect, gas flowmeter detection gas in methane content;
The liquid level sensor, temperature sensor, level sensor, gas flowmeter, water intaking valve, outlet valve respectively with single-chip microcomputer Connection, its work is controlled by single-chip microcomputer;
The single-chip computer control system also includes the circuit anti-interference module being located in it.
The circuit anti-interference module is prior art.
The single-chip computer control system is used for field control, it is easy to attacked by various interference, therefore circuit anti-interference mould Block is important.Higher hamonic wave is filtered off by using wave filter and improves power supply wave shape, is constituted using small inductor bulky capacitor Filter network.In PCB design, digitally to separate, be connected respectively with power end ground wire, while widening power line with simulation And ground wire, and power line is used as far as possible, the trend of ground wire is consistent with the direction of data transfer, and the ground of all devices is connected into one Point, and ground connection is constituted loop, earth potential difference is reduced, so as to reduce interference, instruction redundancy finally is taken to important instruction, Data redundancy is taken to important data.
The specific works of the single-chip computer control system are:
1) after system energization, water intaking valve valve is opened, sewage is entered in filter tank by valve, and filter tank is marked with several waters Graduation mark, is the safety water volume that filter tank handles sewage;
2) when inflow is located at safety water volume scope, the level sensor on buoy, and the liquid level sensor of delivery port are passed Go out signal, feed back to single-chip microcomputer control centre, calculate and control water intaking valve and the size of outlet valve opening, allow water inlet and water outlet The flow velocity of mouth is consistent substantially;
3) when inflow is less than safety water volume scale, level sensor meeting outgoing signal to single-chip microcomputer control centre, single-chip microcomputer Control water intaking valve increases its opening, while single-chip microcomputer control centre can also send control command, reduces the opening of outlet valve, limitation Water discharge flow speed;
4) when water intake velocity is too fast, and water level exceedes safety water volume scale, level sensor meeting outgoing signal is controlled to single-chip microcomputer Center, single-chip microcomputer control water intaking valve reduces its opening, reduces inflow, while increasing water yield;If positioned at the liquid level of delivery port Sensor detect water quality can not outgoing signal up to standard, feed back to single-chip microcomputer control centre, control outlet valve is closed, and control into Water valve reduces its opening or closed, and sewage flows back to filter tank and carries out anaerobic reaction processing again, so moves in circles;
5) methane that up-flow anaerobic biofilter processing sewage is produced enters water-sealed drainage bottle, then passes in gas flowmeter, can be with The content of methane is measured, then passes single-chip microcomputer back, calculates and controls water intaking valve and the size of outlet valve opening;
6)The outgoing signal when temperature sensor detects filter tank temperature less than 35 DEG C, feeds back to single-chip microcomputer control centre, controls Center controls filter tank heating devices heat, when reaching 35-38 DEG C, stops heating;When temperature sensor detects filter tank temperature height Outgoing signal when 38 DEG C, feeds back to single-chip microcomputer control centre, calculates and controls water intaking valve and the size of outlet valve opening, passes through The big minor adjustment filter tank temperature of regulation turnover water reaches prescribed limit.
The growth and breeding optimum temperature range of microorganism is 35-38 DEG C in the anaerobic biofilter(Middle temperature), temperature is every Change in three hours can not be more than 1 DEG C, and temperature change is excessive, will directly affect the treatment effect of anaerobic biofilter.Accordingly, it would be desirable to Filter tank temperature is detected, in operation, by controlling its heater, the water temperature of anaerobic biofilter is strict controlled in 35-38 DEG C.
Anaerobic biofilter handles sewage, and the change of organic loading can be presented as change and the influent COD value of flow of inlet water Change.If the raising of organic loading is to be increased by inflow and produced, too high hydraulic load is it is also possible to make anaerobism The sludge loss rate of processing system is more than its growth rate, and then influences the treatment effeciency of whole system.
The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter of the present invention, water level and the temperature inspection of biofilter Survey is the important step for realizing Inlet and outlet water intelligent control, only accurately measures water level and temperature, by single-chip microcomputer and could be set Water and the time of Inlet and outlet water are calculated and control in software thereon.It is accurate in order to what is calculated and control, preferably with continuously setting Multiple liquid level sensors are put, but consider system cost, the present invention uses subsection setup liquid level sensor, essence is improved by software Degree, is shown on water level is shown using segmented.
The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter of the present invention, by detecting the water of Inlet and outlet water, And then water is accurately controlled, filter tank blocking, current short circuit phenomenon are reduced, the efficiency of its sewage disposal is improved.
Brief description of the drawings
Fig. 1 is structural representation of the invention;
Fig. 2 is control system module diagram of the present invention.
In figure, the gas of 1. filter tank, 2. water intaking valve, 3. outlet valve, 4. liquid level sensor, 5. level sensor, 6. water-sealed drainage bottle 7. The single-chip microcomputer of flowmeter body 8..
Embodiment
Present invention is further described with reference to embodiment and accompanying drawing, but is not limitation of the invention.
Reference picture 1-2, a kind of Inlet and outlet water measurement and control system of up-flow anaerobic biofilter, including filter tank 1, are also wrapped Include the detection means being arranged in filter tank 1, and the control system of single-chip microcomputer 8 being connected with detection means;
The detection means includes liquid level sensor 4, temperature sensor(Do not identified in figure), level sensor 5, gas flowmeter 7;
The inwall in the filter tank 1, equidistantly provided with five liquid level sensors 4 from water inlet to delivery port, for detecting feed water flow The change of amount and the change of influent COD value;
The inwall in filter tank 1 is additionally provided with temperature sensor(Do not identified in figure), for detecting filter tank temperature, the water temperature in control filter tank exists 35-38℃;
The bottom in filter tank 1 sets water intaking valve 2, controls the size of inflow;
The top in filter tank 1 sets and level sensor 5 is set on buoy, buoy, and whether the water in detection filter tank 1 reaches safety water volume Scope;
The top in filter tank 1 is additionally provided with outlet valve 3, controls the size of water yield;
The top in filter tank 1 sets water-sealed drainage bottle 6, is additionally provided with gas flowmeter 7 and is connected with water-sealed drainage bottle 6, and water-sealed drainage bottle 6 collects the mistake of filter tank 1 Filter the gas produced and filtering miscellaneous gas prevents influence from detecting, the methane content in the detection gas of gas flowmeter 7;
The liquid level sensor 4, temperature sensor, level sensor 5, gas flowmeter 7, water intaking valve 2, outlet valve 3 respectively with Single-chip microcomputer 8 is connected, and its work is controlled by single-chip microcomputer 8;
The control system of single-chip microcomputer 8 also includes the circuit anti-interference module being located in it.
The circuit anti-interference module is prior art.
The specific works of the control system of single-chip microcomputer 1 are:
1) after system energization, the valve of water intaking valve 2 is opened, sewage is entered in filter tank 1 by valve, and filter tank 1 is marked with several water Graduation mark is measured, is the safety water volume that filter tank 1 handles sewage;
2) when inflow is located at safety water volume scope, the level sensor 5 on buoy, and delivery port liquid level sensor 4 Outgoing signal, feeds back to the control centre of single-chip microcomputer 8, calculates and controls water intaking valve 1 and size that outlet valve 3 is open, allows water inlet It is consistent substantially with the flow velocity of delivery port;
3) when inflow is less than safety water volume scale, the meeting outgoing signal of level sensor 5 to the control centre of single-chip microcomputer 8, monolithic The control water intaking valve 1 of machine 8 increases its opening, while the control centre of single-chip microcomputer 1 can also send control command, reduces opening for outlet valve 3 Mouthful, limit Water discharge flow speed;
4) when water intake velocity is too fast, and water level exceedes safety water volume scale, the meeting outgoing signal of level sensor 5 is controlled to single-chip microcomputer 8 Center processed, the control water intaking valve 1 of single-chip microcomputer 8 reduces its opening, reduces inflow, while increasing water yield;If positioned at delivery port Liquid level sensor 4 detect water quality can not outgoing signal up to standard, feed back to the control centre of single-chip microcomputer 8, control outlet valve 3 is closed, And controlling water intaking valve 1 to reduce its opening or close, sewage flows back to filter tank 1 and carries out anaerobic reaction processing again, so circulates past It is multiple;
5) methane that up-flow anaerobic biofilter processing sewage is produced enters water-sealed drainage bottle 6, then passes in gas flowmeter 7, can To measure the content of methane, then pass single-chip microcomputer 8 back, calculate and control water intaking valve 1 and the size of the opening of outlet valve 3;
6)Work as temperature sensor(Do not identified in figure)Outgoing signal when detecting the temperature of filter tank 1 less than 35 DEG C, feeds back to single-chip microcomputer 8 Control centre, control centre's control heating devices heat of filter tank 1, when reaching 35-38 DEG C, stops heating;When temperature sensor inspection Outgoing signal when measuring the temperature of filter tank 1 higher than 38 DEG C, feeds back to the control centre of single-chip microcomputer 8, calculates and control water intaking valve 1 and water outlet The size that valve 3 is open, the big temperature of minor adjustment filter tank 1 that water is passed in and out by adjusting reaches prescribed limit.
The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter of the present invention, it is main to consider that water level is transported to reactor The influence of market condition.Sewage water in reactor is controlled by changing flow of inlet water.By the water for detecting Inlet and outlet water Amount, and then water is accurately controlled, filter tank blocking, current short circuit phenomenon are reduced, the efficiency of its sewage disposal is improved.

Claims (2)

1. a kind of Inlet and outlet water measurement and control system of up-flow anaerobic biofilter, including filter tank, it is characterised in that:Also include It is arranged on the detection means in filter tank, and the single-chip computer control system being connected with detection means;
The detection means includes liquid level sensor, temperature sensor, level sensor, gas flowmeter;
The inwall in the filter tank, is equidistantly provided with liquid level sensor, the change for detecting flow of inlet water from water inlet to delivery port Change the change with influent COD value;
The inwall in filter tank is additionally provided with temperature sensor, for detecting filter tank temperature, controls the water temperature in filter tank at 35-38 DEG C;
The bottom in filter tank sets water intaking valve, controls the size of inflow;
The top in filter tank sets and level sensor is set on buoy, buoy, and whether the water in detection filter tank reaches safety water volume model Enclose;
The top in filter tank is additionally provided with outlet valve, controls the size of water yield;
The top in filter tank sets water-sealed drainage bottle, is additionally provided with gas flowmeter and is connected with water-sealed drainage bottle, and water-sealed drainage bottle is collected filter and produced Gas and filter miscellaneous gas, gas flowmeter detection gas in methane content;
The liquid level sensor, temperature sensor, level sensor, gas flowmeter, water intaking valve, outlet valve respectively with single-chip microcomputer Connection, its work is controlled by single-chip microcomputer;
The single-chip computer control system also includes the circuit anti-interference module being located in it.
2. the Inlet and outlet water measurement and control system of up-flow anaerobic biofilter according to claim 1, it is characterised in that The work of the single-chip computer control system is specifically:
1) after system energization, water intaking valve valve is opened, sewage is entered in filter tank by valve, and filter tank is marked with several waters Graduation mark, is the safety water volume that filter tank handles sewage;
2) when inflow is located at safety water volume scope, the level sensor on buoy, and the liquid level sensor of delivery port are passed Go out signal, feed back to single-chip microcomputer control centre, calculate and control water intaking valve and the size of outlet valve opening, allow water inlet and water outlet The flow velocity of mouth is consistent substantially;
3) when inflow is less than safety water volume scale, level sensor meeting outgoing signal to single-chip microcomputer control centre, single-chip microcomputer Control water intaking valve increases its opening, while single-chip microcomputer control centre can also send control command, reduces the opening of outlet valve, limitation Water discharge flow speed;
4) when water intake velocity is too fast, and water level exceedes safety water volume scale, level sensor meeting outgoing signal is controlled to single-chip microcomputer Center, single-chip microcomputer control water intaking valve reduces its opening, reduces inflow, while increasing water yield;If positioned at the liquid level of delivery port Sensor detect water quality can not outgoing signal up to standard, feed back to single-chip microcomputer control centre, control outlet valve is closed, and control into Water valve reduces its opening or closed, and sewage flows back to filter tank and carries out anaerobic reaction processing again, so moves in circles;
5) methane that up-flow anaerobic biofilter processing sewage is produced enters water-sealed drainage bottle, then passes in gas flowmeter, can be with The content of methane is measured, then passes single-chip microcomputer back, calculates and controls water intaking valve and the size of outlet valve opening;
6)The outgoing signal when temperature sensor detects filter tank temperature less than 35 DEG C, feeds back to single-chip microcomputer control centre, controls Center controls filter tank heating devices heat, when reaching 35-38 DEG C, stops heating;
The outgoing signal when temperature sensor detects filter tank temperature higher than 38 DEG C, feeds back to single-chip microcomputer control centre, calculates simultaneously The size of water intaking valve and outlet valve opening is controlled, the size filter tank temperature that runoff investigation is passed in and out by adjusting reaches prescribed limit.
CN201710400957.9A 2017-05-31 2017-05-31 The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter Withdrawn CN107032486A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109661377A (en) * 2016-09-02 2019-04-19 巴格知识产权有限公司 Anaerobic purification device with variable water column
CN113104972A (en) * 2021-04-15 2021-07-13 桂林理工大学 Composite two-phase integrated anaerobic reaction system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62286595A (en) * 1986-06-03 1987-12-12 Toshiba Corp Apparatus for distribution control of inflow load of water treatment plant
CN103058359A (en) * 2013-01-29 2013-04-24 济南大学 Integral controller applied to aeration tank for sewage treatment
JP2013209497A (en) * 2012-03-30 2013-10-10 Metawater Co Ltd Methane fermentation gas purification system and methane fermentation gas purification method
CN206783400U (en) * 2017-05-31 2017-12-22 桂林理工大学 The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62286595A (en) * 1986-06-03 1987-12-12 Toshiba Corp Apparatus for distribution control of inflow load of water treatment plant
JP2013209497A (en) * 2012-03-30 2013-10-10 Metawater Co Ltd Methane fermentation gas purification system and methane fermentation gas purification method
CN103058359A (en) * 2013-01-29 2013-04-24 济南大学 Integral controller applied to aeration tank for sewage treatment
CN206783400U (en) * 2017-05-31 2017-12-22 桂林理工大学 The Inlet and outlet water measurement and control system of up-flow anaerobic biofilter

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
方雷等: "大中型沼气工程中的单片机应用", 《能源工程》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109661377A (en) * 2016-09-02 2019-04-19 巴格知识产权有限公司 Anaerobic purification device with variable water column
CN113104972A (en) * 2021-04-15 2021-07-13 桂林理工大学 Composite two-phase integrated anaerobic reaction system

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