CN112774453A - Automatic aeration control system and control method for ultrafiltration gas-water mixed membrane equipment - Google Patents

Automatic aeration control system and control method for ultrafiltration gas-water mixed membrane equipment Download PDF

Info

Publication number
CN112774453A
CN112774453A CN202011509259.0A CN202011509259A CN112774453A CN 112774453 A CN112774453 A CN 112774453A CN 202011509259 A CN202011509259 A CN 202011509259A CN 112774453 A CN112774453 A CN 112774453A
Authority
CN
China
Prior art keywords
gas
water mixed
ultrafiltration
control module
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN202011509259.0A
Other languages
Chinese (zh)
Other versions
CN112774453B (en
Inventor
陈泉学
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuhan Aqucell Membrane Technology Co ltd
Original Assignee
Wuhan Aqucell Membrane Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wuhan Aqucell Membrane Technology Co ltd filed Critical Wuhan Aqucell Membrane Technology Co ltd
Priority to CN202011509259.0A priority Critical patent/CN112774453B/en
Publication of CN112774453A publication Critical patent/CN112774453A/en
Application granted granted Critical
Publication of CN112774453B publication Critical patent/CN112774453B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/18Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/22Controlling or regulating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/008Control or steering systems not provided for elsewhere in subclass C02F
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Activated Sludge Processes (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention provides an automatic aeration control system and a control method for an ultrafiltration gas-water mixed membrane device, wherein the automatic control system comprises a gas flow detection unit, a gas pressure detection unit and a liquid pressure detection unit, the detection and comparison of gas pressure and liquid pressure are carried out through a control module so as to judge whether the system meets the aeration working condition, if not, the control module adjusts the air input of an air inlet pipeline, and if not, an alarm is given out, so that the problem of the system working is avoided. The invention can realize the automatic aeration operation of the ultrafiltration gas-water mixed membrane equipment, prevent the error easily caused by manual operation and reduce the investment of labor cost.

Description

Automatic aeration control system and control method for ultrafiltration gas-water mixed membrane equipment
Technical Field
The invention relates to the technical field of water treatment equipment, in particular to an automatic aeration control system and method for ultrafiltration gas-water mixed membrane equipment.
Background
The external pressure type gas-water mixed ultrafiltration membrane needs to be subjected to aeration operation periodically during operation, and bubbles generated by aeration can play a role in flushing the surface of an ultrafiltration membrane component in the process of rising in water, so that the pollution and blockage generated during the operation of the gas-water mixed membrane system can be effectively reduced through the aeration operation.
At present conventional aeration means is control air compressor's operating pressure, adopt preventing of manual control valve opening degree to aerate, the unable accurate regulation and control aeration rate of manual control, and then lead to excessive aeration or aeration not enough, this is fairly unfavorable to the steady operation of system, to enterprise's production simultaneously, it must increase the cost of labor to invest in the manpower in a large number to carry out manual aeration, unstable aeration control means makes the stability of equipment relatively poor, the frequency and the cost of later maintenance have been increased, still can influence the quality of water of final play water.
Disclosure of Invention
In view of the above, the present invention provides an automatic aeration control system and method for an ultrafiltration air-water mixing device, which can effectively monitor and control parameters of the aeration device.
The technical scheme of the invention is realized as follows: the invention provides an automatic aeration control system for ultrafiltration air-water mixed membrane equipment, which comprises the ultrafiltration air-water mixed membrane equipment, wherein a water inlet pipe and an air inlet pipe are communicated with the ultrafiltration air-water mixed membrane equipment, a proportional control valve is arranged on the air inlet pipe, the automatic aeration control system also comprises an air pressure sensor, a water pressure sensor, an air pressure transmitter, a water pressure transmitter, an A/D converter and a logic control module, the air pressure sensor is arranged in the air inlet pipe, the water pressure sensor is arranged in the ultrafiltration air-water mixed membrane equipment and is in signal connection with the A/D converter through the air pressure transmitter, the water pressure sensor is in signal connection with the A/D converter through the water pressure transmitter, the A/D converter is in signal connection with the logic control module, and the proportional control valve is in.
On the basis of the technical scheme, the air conditioner further comprises a flow sensor and a flow transmitter, wherein the flow sensor is installed in the air inlet pipe, and the flow sensor is in signal connection with the A/D converter through the flow transmitter.
On the basis of the above technical solution, preferably, the system further comprises a data transmission module and a data management platform, wherein the a/D converter is in signal connection with the data transmission module, and the data transmission module is in signal connection with the data management platform.
On the basis of the above technical solution, preferably, the mobile management terminal further comprises a data transmission module, and the data transmission module is in signal connection with the mobile management terminal.
The invention also provides a control method of the automatic aeration control system for the ultrafiltration air-water mixed membrane equipment, which comprises the following steps:
firstly, when aeration operation is started, a logic control module presets a pressure threshold value P, a gas pressure sensor collects gas pressure of a gas inlet pipeline, a water pressure sensor collects pressure of water in ultrafiltration gas-water mixed membrane equipment, the gas pressure and the water pressure are converted into electric signals respectively, the two kinds of pressure electric signals are transmitted to an A/D converter through a gas pressure transmitter and a water pressure transmitter respectively and are converted into analog-digital signals, and therefore an analog-digital signal value P1 for measuring gas pressure and an analog-digital signal value P2 for measuring water pressure are obtained;
step two, presetting an intake flow target value L by the logic control module, simultaneously collecting the flow of gas in an intake pipe by the flow sensor and obtaining a flow signal, converting the flow signal into an analog-digital signal value L1 of the gas flow by the A/D converter, and adjusting the opening of the proportional control valve by the logic control module according to the preset intake flow target value L;
step three, the A/D converter transmits the converted analog-digital signal values P1 and P2 to a logic control module respectively, the logic control module compares P with P1 and P2, and when at least one of P1 and P2 is larger than P, the logic control module gives an alarm;
step four, when the P1 and the P2 are not more than P, the logic control module continuously compares the P1 and the P2, when the P1 is more than P2+ n, the logic control module carries out aeration control according to preset aeration time T, when the aeration time is over, the proportional control valve is controlled to be closed, and when the P1 is not more than P2+ n, the step five is carried out;
step five, the logic control module controls the opening of the proportional control valve to increase, then the step four is repeated, and when the opening of the proportional control valve reaches the maximum and p1 is not more than p2+ n, the logic control module gives an alarm
Further preferably, the first step further comprises the step of transmitting the measured gas pressure modulus signal value p1 and the measured water pressure modulus signal value p2 to the data management platform and the mobile management terminal respectively through the data transmission module.
On the basis of the above technical solution, preferably, the first step further includes that the mobile management terminal presets a pressure threshold P for the logic control module through the data transmission module.
On the basis of the above technical solution, preferably, the second step further includes that the analog-to-digital signal value l1 of the gas flow is respectively transmitted to the data management platform and the mobile management terminal through the data transmission module.
On the basis of the above technical solution, preferably, the second step further includes that the mobile management terminal presets the intake air flow target value L to the logic control module through the data transmission module.
On the basis of the above technical solution, preferably, in step four, n is 0.05 MPa.
Compared with the prior art, the automatic aeration control system and the control method of the ultrafiltration air-water mixed membrane equipment have the following beneficial effects:
(1) the control system can realize automatic aeration control and early warning on the gas-water mixed membrane equipment, achieves the effect of automatically controlling aeration through the preset aeration time, pressure threshold and flow threshold, and automatically gives an alarm when the system is in the non-safe operation parameter range, so that the safety is high;
(2) the whole device also adopts a remote data management platform and a mobile management terminal to manage data and control parameters, so that remote operation and monitoring of operators are realized, and the device adapts to the development law of the future big data era;
(3) the control method of the invention can lead the aeration system to work within a preset safety range value, and the system has a corresponding feedback adjustment process, can adjust the working parameters to the allowable range as far as possible for normal work, and can automatically give an alarm if the working parameters do not meet the requirement.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.
FIG. 1 is a connection diagram of an automatic aeration control system for an ultrafiltration gas-water mixed membrane apparatus according to the present invention.
In the figure: the system comprises 1-ultrafiltration air-water mixed membrane equipment, 2-proportion regulation control valves, 3-air pressure sensors, 4-water pressure sensors, 5-air pressure transmitters, 6-water pressure transmitters, 7-A/D converters, 8-logic control modules, 9-flow sensors, 10-flow transmitters, 11-water inlet pipes, 12-air inlet pipes, 13-data transmission modules, 14-data management platforms and 15-mobile management terminals.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention.
As shown in figure 1, the automatic aeration control system for the ultrafiltration air-water mixed membrane device comprises an ultrafiltration air-water mixed membrane device 1, wherein the ultrafiltration air-water mixed membrane device 1 is used for water treatment and comprises a main container, a plurality of membrane components are arranged in the container, an aeration device is arranged below the membrane components and is communicated with the outside through an air inlet pipe 12, and the main container is communicated with the outside through an water inlet pipe 11.
The device also comprises a proportional control valve 2, an air pressure sensor 3, a water pressure sensor 4, an air pressure transmitter 5, a water pressure transmitter 6, an A/D converter 7, a logic control module 8, a flow sensor 9, a flow transmitter 10, a data transmission module 13, a data management platform 14 and a mobile management terminal 15, wherein the flow sensor 9 and the air pressure sensor 3 are both arranged in an air inlet pipe 12, the proportional control valve 2 is also arranged on the air inlet pipe 12, the water pressure sensor 4 is arranged in a main container, the proportional control valve 2 is in signal connection with the A/D converter 7, the air pressure sensor 3 is in signal connection with the A/D converter 7 through the air pressure transmitter 5, the water pressure sensor 4 is in signal connection with the A/D converter 7 through the water pressure transmitter 6, and the flow sensor 9 is in signal connection with the A/D converter 7 through the flow, the signal sensor 7 is in signal connection with the logic control module 8, the A/D converter 7 is also in signal connection with the data transmission module 13, and the data transmission module 13 is in signal connection with the data management platform 14 and the mobile management terminal 15 respectively.
The proportional control valve 2 is used for controlling the opening of the air inlet pipe 12 so as to control and adjust the aeration amount and the aeration pressure value, and the proportional control valve 2 is installed on the air inlet pipe 12.
The air pressure sensor 3 is used for detecting the pressure value in the air inlet pipe 12, so that the aeration pressure and the water pressure can be compared, and the aeration state can be monitored in real time.
Water pressure sensor 4 is used for detecting the water pressure in the main container, and water pressure contrasts with atmospheric pressure, can real time monitoring in the mixed membrane equipment of ultrafiltration air water whether membrane module need carry out aeration treatment, and water pressure sensor 4 installs inside the main container.
The flow sensor 9 is used for detecting a gas flow value in the gas inlet pipe 12 and collecting and monitoring the gas flow value as an equipment parameter, and the flow sensor 9 is installed in the gas inlet pipe 12.
The air pressure transmitter 5, the water pressure transmitter 6 and the flow transmitter 10 are all used for receiving detection signals of the air pressure sensor 3, the water pressure sensor 4 and the flow sensor 9, converting corresponding detection models into standard signals and transmitting the standard signals to the A/D converter 7.
The A/D converter 7 is used for converting the electric signal of the transmitter into a modulus signal so as to facilitate the processing of the signal by the logic control module 8, and the A/D converter 7 is respectively in signal connection with the logic control module 8, the proportional control valve 2 and the data transmission module 13.
The logic control module 8 is used for receiving and processing the signal and sending a corresponding control signal to control the operation of the proportional control valve 2, the logic control module 8 also has a basic alarm function, and specifically, the logic control module 8 is a PLC single chip microcomputer.
The water inlet pipe 11 is used for inputting water to be treated into the ultrafiltration gas-water mixed membrane device 1.
The air inlet pipe 12 is used for inputting air to the aeration equipment in the ultrafiltration air-water mixed membrane equipment 1 for aeration.
The data transmission module 13 is used for sending the signal passing through the a/D converter 7 to the outside or receiving an external signal and sending the signal to the logic control module 8 or the proportional control valve 2 through the a/D converter 7.
The data management platform 14 is used to collect, store and manage the signals from the data transmission module 13.
The mobile management terminal 15 is used for collecting, storing, monitoring, managing and monitoring signals from the data transmission module 13, and the mobile management terminal 15 can also send control signals to the data transmission module 13 so as to directly control the proportional control valve 2 and the logic control module 8.
The invention also provides an automatic aeration control method for the ultrafiltration gas-water mixed membrane equipment, which comprises the following steps:
the logic control module 8 is preset through the mobile management terminal 15, or parameters are directly preset through the logic control module 8, the preset parameters comprise a pressure threshold value P, a gas flow target value L and an aeration working duration T, when aeration operation is required, the gas pressure P1 of the gas inlet pipe 12 is collected by the gas pressure sensor 3, the water pressure P2 of the ultrafiltration gas-water mixed membrane device is collected by the water pressure sensor 4, and P1 and P are respectively compared with P2 and P.
In the specific embodiment, when P is 0.3MPa, P1 is 0.4MPa, and P2 is 0.5MPa, both P1 and P2 are greater than P, so the roadbed control module 8 gives an alarm and sends the alarm to the data management platform 14 and the mobile management terminal 15 through the data transmission module 13.
In the specific embodiment, when P is 0.3MPa, P1 is 0.2MPa, and P2 is 0.5MPa, P2 is greater than P, so the logic control module 8 alarms and sends an alarm signal to the data management platform 14 and the mobile management terminal 15 through the data transmission module 13.
In the specific embodiment, when P is 0.3MPa, when P1 is 0.4MPa, and P2 is 0.2MPa, P1 is greater than P, so the logic control module 8 alarms and sends an alarm signal to the data management platform 14 and the mobile management terminal 15 through the data transmission module 13.
In a specific embodiment, when P is 0.3MPa, P1 is 0.2MPa, and P2 is 0.3MPa, neither P1 nor P2 is greater than P, at this time, the sizes of P1 and P2 are compared, and P1 is less than P2+0.05MPa, at this time, the logic control module 8 sends a control signal to the proportional control valve 2 through the a/D converter 7, or the mobile management terminal 15 sends a control signal to the proportional control valve 2 through the data transmission module 13 and the a/D converter 7, wherein the signal priority of the data transmission module 13 is greater than the signal priority of the logic control module 8, the opening of the proportional control valve 2 is increased, so as to increase the gas flow and pressure, and then the detection comparison between P1 and P2 is performed in real time. If the opening degree of the proportional control valve 2 reaches the maximum p1 and is still not greater than p2+0.05MPa in the subsequent adjustment process, the logic control module 8 gives an alarm, if the p1 is greater than p2+0.05MPa in the subsequent adjustment process, timing aeration is started, and when the aeration time reaches T, the logic control module 8 or the mobile management terminal 15 sends a control signal to close the proportional control valve 2.
In the specific embodiment, when P is 0.3MPa, P1 is 0.3MPa, and P2 is 0.2MPa, neither P1 nor P2 is greater than P, and P1 is greater than P2+0.05MPa, at this time, the timing of aeration is started, and when the aeration time reaches T, the logic control module 8 or the mobile management terminal 15 sends out a control signal, and the proportional control regulating valve 2 is closed.
In a specific embodiment, when the flow sensor 9 collects a flow signal L1 in the intake pipe 12, the logic control module 8 compares L with L1, when L1 is smaller than L, the logic control module 8 sends a control signal to the proportional control valve 2 through the a/D converter 7 or the mobile management terminal 15 sends a control signal to the proportional control valve 2 through the data transmission module 13 and the a/D converter 7, the proportional control valve 2 is controlled to be opened, and when L1 is larger than L, the logic control module 8 gives an alarm.
In the specific embodiment, the pressure values p1 and p2 and the flow value l1 converted by the a/D converter 7 are all sent to the data management platform 14 and the mobile management terminal 15 through the data transmission module 13.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.

Claims (10)

1. An automatic aeration control system for ultrafiltration air-water mixed membrane equipment comprises ultrafiltration air-water mixed membrane equipment (1), wherein an inlet pipe (11) and an inlet pipe (12) are communicated with the ultrafiltration air-water mixed membrane equipment, a proportional control valve (2) is installed on the inlet pipe (11), the automatic aeration control system is characterized by further comprising an air pressure sensor (3), a water pressure sensor (4), an air pressure transmitter (5), a water pressure transmitter (6), an A/D converter (7) and a logic control module (8), the air pressure sensor (3) is installed in the inlet pipe (12), the water pressure sensor (4) is installed in the ultrafiltration air-water mixed membrane equipment (1), the air pressure sensor (3) is in signal connection with the A/D converter (7) through the air pressure transmitter (5), and the water pressure sensor (4) is in signal connection with the A/D converter (7) through the water pressure transmitter (6), the A/D converter (7) is in signal connection with the logic control module (8), and the proportional control valve (2) is in signal connection with the A/D converter (7).
2. The automatic aeration control system for the ultrafiltration gas-water mixed membrane device according to claim 1, further comprising a flow sensor (9) and a flow transmitter (10), wherein the flow sensor (9) is installed in the air inlet pipe (12), and the flow sensor (9) is in signal connection with the A/D converter (7) through the flow transmitter (10).
3. The automatic aeration control system for the ultrafiltration gas-water mixed membrane device according to claim 1, further comprising a data transmission module (13) and a data management platform (14), wherein the A/D converter (7) is in signal connection with the data transmission module (13), and the data transmission module (13) is in signal connection with the data management platform (14).
4. The automatic aeration control system for the ultrafiltration gas-water mixed membrane device according to claim 3, further comprising a mobile management terminal (15), wherein the data transmission module (13) is in signal connection with the mobile management terminal (15).
5. The control method of the automatic aeration control system for the ultra-filtration gas-water mixed membrane device as set forth in any one of claims 1 to 4, characterized by comprising the steps of:
firstly, when aeration operation is started, a pressure threshold value P is preset by a logic control module (8), a gas pressure sensor (3) collects the gas pressure of an air inlet pipe (12), a water pressure sensor (4) collects the pressure of water in ultrafiltration gas-water mixed membrane equipment (1), the gas pressure and the water pressure are converted into electric signals respectively, the two pressure electric signals are transmitted to an A/D converter (7) through a gas pressure transmitter (5) and a water pressure transmitter (6) and are converted into analog-to-digital signals respectively, and therefore an analog-to-digital signal value P1 of measured gas pressure and an analog-to-digital signal value P2 of measured water pressure are obtained;
step two, presetting an intake flow target value L by a logic control module (8), simultaneously collecting the flow of gas in an air inlet pipe (12) by a flow sensor (9) and obtaining a flow signal, converting the flow signal into an analog-digital signal value L1 of the gas flow by an A/D converter (7), and adjusting the opening degree of a control valve (2) by the logic control module (8) according to the preset intake flow target value L;
step three, the A/D converter (7) transmits the converted analog-digital signal values P1 and P2 to the logic control module (8) respectively, the logic control module (8) compares P with P1 and P2, and when at least one of P1 and P2 is larger than P, the logic control module (8) gives an alarm;
step four, when the P1 and the P2 are not more than P, the logic control module (8) continuously compares the P1 and the P2, when the P1 is more than P2+ n, the logic control module (8) carries out aeration control according to the preset aeration time T, when the aeration time is over, the proportional control valve (2) is controlled to be closed, and when the P1 is not more than P2+ n, the step five is carried out;
and step five, the logic control module (8) controls the opening of the proportional control valve (2) to increase, then the step four is repeated, and when the opening of the proportional control valve (2) reaches the maximum and p1 is not greater than p2+ n, the logic control module (8) gives an alarm.
6. The control method of the automatic aeration control system for an ultra-filtration gas-water mixed membrane facility according to claim 5, wherein the first step further comprises the step of transmitting the measured gas pressure modulus signal value p1 and the measured water pressure modulus signal value p2 to the data management platform (14) and the mobile management terminal (15) through the data transmission module (13), respectively.
7. The control method of the automatic aeration control system for an ultrafiltration gas-water mixed membrane device according to claim 5, wherein the first step further comprises the step that the mobile management terminal (15) presets a pressure threshold value P to the logic control module (8) through the data transmission module (13).
8. The control method of the automatic aeration control system for the ultra-filtration gas-water mixed membrane device according to claim 5, wherein the second step further comprises the step of transmitting the analog-to-digital signal l1 of the gas flow rate to the data management platform (14) and the mobile management terminal (15) through the data transmission module (13), respectively.
9. The control method of the automatic aeration control system for the ultrafiltration gas-water mixed membrane device according to claim 5, wherein the second step further comprises the step that the mobile management terminal (15) presets the intake air flow target value L to the logic control module (8) through the data transmission module (13).
10. The method of claim 5, wherein n is 0.05MPa in the fourth step.
CN202011509259.0A 2020-12-18 2020-12-18 Control method of aeration automatic control system for ultrafiltration gas-water mixed membrane equipment Active CN112774453B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011509259.0A CN112774453B (en) 2020-12-18 2020-12-18 Control method of aeration automatic control system for ultrafiltration gas-water mixed membrane equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011509259.0A CN112774453B (en) 2020-12-18 2020-12-18 Control method of aeration automatic control system for ultrafiltration gas-water mixed membrane equipment

Publications (2)

Publication Number Publication Date
CN112774453A true CN112774453A (en) 2021-05-11
CN112774453B CN112774453B (en) 2023-08-01

Family

ID=75751310

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011509259.0A Active CN112774453B (en) 2020-12-18 2020-12-18 Control method of aeration automatic control system for ultrafiltration gas-water mixed membrane equipment

Country Status (1)

Country Link
CN (1) CN112774453B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113607237A (en) * 2021-10-08 2021-11-05 南通市大安消防技术服务有限公司 Wireless water pressure transmission device
CN116688759A (en) * 2023-08-07 2023-09-05 泰州禾益新材料科技有限公司 Ultrafiltration membrane with air pressure adjusting function

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202936241U (en) * 2012-12-04 2013-05-15 北京碧水源环境科技有限公司 Device capable of circularly cleaning MBR (Membrane Biological Reactor) membrane unit in offline way
CN110461446A (en) * 2017-01-06 2019-11-15 苏伊士集团 For making the improvement system of submerged film aeration
CN211411648U (en) * 2019-10-31 2020-09-04 苏州热工研究院有限公司 Flat ceramic membrane filtering performance test equipment

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202936241U (en) * 2012-12-04 2013-05-15 北京碧水源环境科技有限公司 Device capable of circularly cleaning MBR (Membrane Biological Reactor) membrane unit in offline way
CN110461446A (en) * 2017-01-06 2019-11-15 苏伊士集团 For making the improvement system of submerged film aeration
CN211411648U (en) * 2019-10-31 2020-09-04 苏州热工研究院有限公司 Flat ceramic membrane filtering performance test equipment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113607237A (en) * 2021-10-08 2021-11-05 南通市大安消防技术服务有限公司 Wireless water pressure transmission device
CN113607237B (en) * 2021-10-08 2021-12-07 南通市大安消防技术服务有限公司 Wireless water pressure transmission device
CN116688759A (en) * 2023-08-07 2023-09-05 泰州禾益新材料科技有限公司 Ultrafiltration membrane with air pressure adjusting function
CN116688759B (en) * 2023-08-07 2023-11-07 泰州禾益新材料科技有限公司 Ultrafiltration membrane with air pressure adjusting function

Also Published As

Publication number Publication date
CN112774453B (en) 2023-08-01

Similar Documents

Publication Publication Date Title
CN112774453B (en) Control method of aeration automatic control system for ultrafiltration gas-water mixed membrane equipment
CN207650621U (en) A kind of remote auto is for ash handing system
CN103425108B (en) Water pollution prevention and control system and method based on quality-divided discharge and quality-divided treatment
CN105641986B (en) Flap valve filter back washing Intelligentized control method and equipment
CN113324182B (en) Control system and method for monitoring leakage of water system
CN107120263B (en) Vacuum drainage water pump test system and test method
CN206925101U (en) A kind of pressure flow adjustable gas-liquid pulse-control system
CN203668102U (en) Aeration tank dissolved oxygen concentration control system and sewage treatment system
CN113341842B (en) Storage yard spray dedusting intelligent control system
CN115126041A (en) Intelligent water supply system and method
CN211170043U (en) Ozone on-line automatic control device in purified water production
CN208872663U (en) A kind of power plant stack gas on-line monitoring system
CN110543135A (en) direct drinking water hardness automatic adjusting control system and method based on central water treatment equipment
CN207541480U (en) A kind of vacuum ply rolling composite metal plate slab vacuum prepares automatic detection and control device
CN112823873A (en) Method and device for accurately controlling feeding of reaction kettle
CN207924478U (en) A kind of Sewage Disposal long-distance monitorng device
CN210924306U (en) Electromagnetic control system for industrial water pipeline
CN220703485U (en) Remote control system for anaerobic sludge digestion
CN107884476B (en) Column type membrane module aeration intensity monitoring system based on Arduino controller
CN220976738U (en) Automatic sewage treatment system
CN219636895U (en) Closed loop system capable of automatically controlling oil gas treatment capacity
CN210944893U (en) Balanced discharging equipment of waste water that contains organic matter
CN207764170U (en) Column-type film components aeration intensity based on Arduino controllers monitors system
CN117902756A (en) Automatic rectifying wastewater treatment system and method
CN210786833U (en) SNCR denitration automatic control system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant