CN113582326A - Control device and method suitable for river and lake jet aerator - Google Patents
Control device and method suitable for river and lake jet aerator Download PDFInfo
- Publication number
- CN113582326A CN113582326A CN202111022761.3A CN202111022761A CN113582326A CN 113582326 A CN113582326 A CN 113582326A CN 202111022761 A CN202111022761 A CN 202111022761A CN 113582326 A CN113582326 A CN 113582326A
- Authority
- CN
- China
- Prior art keywords
- water
- jet aerator
- detector
- detection data
- preset
- 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
Links
- 238000005276 aerator Methods 0.000 title claims abstract description 62
- 238000000034 method Methods 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 144
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 238000001514 detection method Methods 0.000 claims description 50
- 238000004458 analytical method Methods 0.000 claims description 16
- 238000003066 decision tree Methods 0.000 claims description 4
- 238000005086 pumping Methods 0.000 claims description 4
- 238000013528 artificial neural network Methods 0.000 claims description 3
- 238000013135 deep learning Methods 0.000 claims description 3
- 238000013278 delphi method Methods 0.000 claims description 3
- 238000012544 monitoring process Methods 0.000 claims description 2
- 238000009434 installation Methods 0.000 abstract 1
- 230000015654 memory Effects 0.000 description 8
- 238000005273 aeration Methods 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000010865 sewage Substances 0.000 description 5
- 230000000630 rising effect Effects 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Images
Classifications
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- 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
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The invention discloses a control device and a control method suitable for a river and lake jet aerator, which comprise the jet aerator and a submersible pump, and further comprise a programmable controller, an acquisition module and an execution module; the programmable controller is connected with the jet aerator through the submersible pump and the execution module; the acquisition module comprises a water level detector, a water body DO detector, a water temperature detector and a pressure detector, the water level detector, the water body DO detector and the water temperature detector are all electrically connected with the programmable controller, and the water level detector, the water body DO detector and the water temperature detector are all arranged in corresponding installation positions of the water body; the pressure detector is arranged between the execution module and the jet aerator, the size of formed bubbles can be changed by adjusting the flow of input liquid, the air suction amount, the volume of the mixing pipe, increasing turbulence-forming components and the like.
Description
Technical Field
The invention belongs to the field of sewage treatment, relates to an aeration technology, and particularly relates to a control device and a control method suitable for a river and lake jet aerator.
Background
Jet aerator as an aeration and oxygenation method is applied to wastewater treatment from the 40 th age of 20 th century, and has a history of more than 60 years. When the jet aerator works, water is discharged from the water pump and flows into a nozzle of the jet aerator, the liquid is sprayed out from the nozzle at a very high speed along with the reduction of the diameter of the nozzle, the liquid flowing at a high speed passes through the air suction chamber and enters the mixing pipe (throat pipe), local vacuum is formed in the mixing pipe (throat pipe) and the air suction chamber, and a large amount of small bubbles and water are divided into a mixture under the action of water pressure after a large amount of air sucked through the air inlet enters the mixing pipe (throat pipe). The gas-liquid mixture is discharged outwards through the diffusion pipe, the speed of the gas-liquid mixture is reduced, the pressure is enhanced to form a powerful jet flow, and the wastewater is stirred and oxygenated. After being disturbed by cutting and jetting for many times, the bubbles are changed into countless fine bubbles, the surface area of the fine bubbles is very large, and oxygen in the air is more easily and quickly dissolved in water. Because the bubbles have small diameter and slow rising speed, the time that oxygen in the atmosphere is dissolved in water is prolonged, the wastewater and the oxygen are promoted to be fully mixed and contacted, reducing substances in the wastewater are oxidized, most of reducing bacteria and other anaerobic bacteria are killed, and the aim of treating the wastewater is fulfilled.
However, the structural parameters of the conventional jet aerator in the current market are generally designed according to the application of large-scale sewage treatment facilities, and have larger air inlets and larger air suction amount, while the general large-scale sewage aeration tank has higher submerged water depth, generally more than 5m to 7m, and the main reason is that the water depth of the aeration tank is increased, and when the effective power is similar, the mixed liquid bubbles sprayed by the jet aerator can obtain larger space utilization rate. The oxygen transfer rate can be improved, and the oxygen absorption is in a certain proportion to the submerged depth. Meanwhile, under the same air suction structure parameters, the jet aerator has large air suction amount under the working condition of small submerged water depth, and the air suction amount becomes small along with deepening of the working condition water depth, so that a larger air suction amount structure is generally designed. Therefore, the conventional jet aerator in the market is directly applied to urban river and lake water body treatment, and ideal working conditions are difficult to obtain. The water depth of the urban river and lake water is generally shallow, and the water depth is greatly influenced by the rising tide and the falling tide, and the water quality of the urban river and lake water also greatly changes.
Disclosure of Invention
The invention aims to provide a control device and a control method suitable for a river and lake jet aerator, which are used for solving the problem that bubbles formed by the jet aerator are not suitable for a dynamic hydrological environment due to the influence of rising tide and falling tide on the jet aerator under the urban river and lake water environment.
The purpose of the invention can be realized by the following technical scheme:
a control device suitable for a river and lake jet aerator comprises the jet aerator, a submersible pump, a programmable controller, an acquisition module and an execution module;
the programmable controller is connected with the jet aerator through the submersible pump and the execution module;
the acquisition module comprises a water level detector, a water body DO detector, a water temperature detector and a pressure detector;
the water level detector, the water body DO detector and the water temperature detector are electrically connected with the programmable controller, and are arranged in corresponding mounting positions of the water body;
the pressure detector is arranged between the execution module and the jet aerator.
Furthermore, the submersible pump also comprises a frequency converter used for adjusting the pumping quantity or/and the water delivery quantity of the submersible pump, the frequency converter is arranged between the programmable controller and the submersible pump, and the programmable controller is electrically connected with the submersible pump through the frequency converter.
Furthermore, the execution module comprises an electric adjustable air valve, and the electric adjustable air valve is connected with the jet aerator through a pressure detector.
Furthermore, the device also comprises a float flowmeter for monitoring the flow of the inlet air, and the float flowmeter is connected with the electric adjustable air valve.
A control method of a river and lake jet aerator is suitable for the control device of the river and lake jet aerator, and comprises the following steps:
acquiring detection data of a DO detector, detection data of a water temperature detector and detection data of a water level detector, wherein the detection data are real-time data;
inputting the detection data into a water working condition detection model in the programmable controller to obtain the water working condition, and determining the viscosity coefficients and the optimal mixing ratio of the liquid and the gas based on the water working condition;
and the electric adjustable gas valve in the execution module controls the gas inflow based on the optimal mixing ratio.
Further, before inputting the detection data into the water working condition detection model in the programmable controller to obtain the water working condition, and determining the viscosity coefficients of the liquid and the gas and the optimal mixing ratio based on the water working condition, the method further comprises:
the method comprises the steps of collecting detection data of a plurality of water body DO detectors, detection data of water temperature detectors and detection data of water level detectors in advance, analyzing the detection data of the water body DO detectors, the detection data of the water temperature detectors and the detection data of the water level detectors in a preset analysis mode to obtain a plurality of water body working conditions, enabling the detection data to correspond to the water body working conditions one by one to obtain an analysis data set, inputting the analysis data set into a deep neural network algorithm to conduct deep learning, and obtaining a water body working condition detection model.
Further, the preset analysis mode comprises a decision tree analysis method and a delphire method.
Further, the viscosity coefficients and the optimal mixing ratio of the liquid and the gas are determined based on the working conditions of the water body, specifically,
and matching the water working condition with a preset viscosity coefficient and a mixing ratio table, wherein the viscosity coefficient and the mixing ratio table comprise the preset water working condition, the preset viscosity coefficient and the preset mixing ratio, the preset water working condition, the preset viscosity coefficient and the preset mixing ratio are in one-to-one correspondence, and when the water working condition is completely coincided with the preset water working condition, the preset viscosity coefficient and the preset mixing ratio corresponding to the preset water working condition are selected to be the viscosity coefficient and the optimal mixing ratio of liquid and gas.
Compared with the prior art, the invention has the beneficial effects that:
the jet aerator mainly forms an energy exchange effect by turbulent fluctuation, collision and shearing of gas-liquid two-phase flow in the mixing pipe, converts the kinetic energy of fluid into energy contained by bubbles, and the kinetic energy of the fluid is brought by input fluid and converted into the energy contained by the bubbles. The device changes the size of formed bubbles by adjusting the liquid flow input by the jet aerator and the air suction amount so as to adapt to the requirement of river and lake water body treatment.
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 block diagram of the control scheme of the present invention;
fig. 2 is a schematic block diagram of the control method of the present invention.
Detailed Description
The embodiments of the present invention will be described below with reference to the drawings.
The terms "first," "second," and the like in the description and claims of the present application and in the above-described drawings are used for distinguishing between different objects and not for describing a particular order. Furthermore, the terms "include" and "have," as well as any variations thereof, are intended to cover non-exclusive inclusions. For example, a process, method, system, article, or apparatus that comprises a list of steps or elements is not limited to only those steps or elements listed, but may alternatively include other steps or elements not listed, or inherent to such process, method, article, or apparatus.
Reference herein to "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment can be included in at least one embodiment of the application. The appearances of the phrase in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments. It is explicitly and implicitly understood by one skilled in the art that the embodiments described herein can be combined with other embodiments.
Traditionally, the structural parameters of the conventional jet aerator in the market are generally designed according to the application of large-scale sewage treatment facilities, and the conventional jet aerator has a large air inlet and a large air suction amount, and the general large-scale sewage aeration tank has an effective high submerged water depth which is generally more than 5m to 7m, and the main reason is that the water depth of the aeration tank is increased, and when the effective power is close, the mixed liquid bubbles sprayed by the jet aerator can obtain a large space utilization rate. The oxygen transfer rate can be improved, and the oxygen absorption is in a certain proportion to the submerged depth. Meanwhile, under the same air suction structure parameters, the jet aerator has large air suction amount under the working condition of small submerged water depth, and the air suction amount becomes small along with deepening of the working condition water depth, so that a larger air suction amount structure is generally designed. Therefore, the conventional jet aerator in the market is directly applied to urban river and lake water body treatment, and ideal working conditions are difficult to obtain.
Aiming at the technical problem, the application provides a control device and a control method suitable for a river and lake jet aerator, wherein the control device comprises the jet aerator, a submersible pump, a programmable controller, an acquisition module and an execution module;
the programmable controller is connected with the jet aerator through the submersible pump and the execution module;
the acquisition module comprises a water level detector, a water body DO detector, a water temperature detector and a pressure detector;
the water level detector, the water body DO detector and the water temperature detector are electrically connected with the programmable controller, and are arranged in corresponding mounting positions of the water body;
the pressure detector is arranged between the execution module and the jet aerator.
The embodiment of the application can be applied to electronic equipment such as a personal computer, a smart phone (such as an Android mobile phone, an iOS mobile phone and the like), a tablet personal computer, a palm computer or wearable equipment, and can also be applied to multimedia playing application (such as a QQ music player) or multimedia editing application (such as Au) operated by the electronic equipment.
Based on the above description, the embodiment of the present invention provides a control apparatus and method suitable for a river and lake jet aerator, as shown in fig. 1;
the water inlet of the jet aerator is connected with the submersible pump, the submersible pump is used for pumping water for the river and lake treatment water body to supply the jet aerator, mixed liquid sprayed by the water jet aerator is added to the river and lake treatment water body, and the water body is oxygenated through the circulating aeration of the river and lake treatment water body.
The submersible pump is powered by a frequency converter, a control line of the frequency converter is connected to a programmable controller, and the programmable controller controls and adjusts the water pumping and water feeding amount of the submersible pump by controlling the power supply frequency of the frequency converter, and regulates and controls the water inlet pressure and the water inlet and outlet amount of the jet aerator.
The air inlet of the jet aerator is sequentially connected with a pressure detector, an electric adjustable air valve and a float flowmeter. The detection signal line of the pressure detector is connected to the programmable controller, the pressure information is transmitted to the programmable controller, the control line of the programmable controller is connected to the electric adjustable air valve, and the programmable controller controls and adjusts the air inflow amount of the jet aerator by controlling the opening angle of the electric adjustable air valve.
And the programmable controller is used for recording the water level, the water temperature, the water body DO, the corresponding optimal water inflow and the optimal air inflow which are obtained through the jet aerator test in advance.
Specifically, detection data of a plurality of water body DO detectors, detection data of water temperature detectors and detection data of water level detectors are collected in advance, the detection data of the water body DO detectors, the detection data of the water temperature detectors and the detection data of the water level detectors are analyzed through a preset analysis mode, wherein the preset analysis mode comprises a decision tree analysis method and a Delphi method, more specifically, the detection data are analyzed through a plurality of related scientific researchers and a front-line real operator, a plurality of water body working conditions are obtained through the decision tree analysis method and the Delphi method, a plurality of detection data are in one-to-one correspondence with the plurality of water body working conditions to obtain an analysis data set, and the analysis data set is input into a deep neural network algorithm for deep learning to obtain a water body working condition detection model.
Acquiring detection data of a DO detector, detection data of a water temperature detector and detection data of a water level detector, wherein the detection data are real-time data;
inputting detection data into a water working condition detection model in a programmable controller to obtain water working conditions, matching the water working conditions with preset viscosity coefficients and a mixing ratio table, wherein the viscosity coefficients and the mixing ratio table comprise preset water working conditions, preset viscosity coefficients and preset mixing ratios, the preset water working conditions, the preset viscosity coefficients and the preset mixing ratios correspond to one another, when the water working conditions are completely coincided with the preset water working conditions, the preset viscosity coefficients and the preset mixing ratios corresponding to the preset water working conditions are selected as viscosity coefficients of liquid and gas and optimal mixing ratios, the viscosity coefficients and the mixing ratio table is formed by installing a jet aerator device in the urban river and lake treatment water to be treated for a plurality of times, installing a water DO detection device 400 meters away from the jet aerator device, starting the jet aerator device, and respectively carrying out tide rising, tide falling and different time periods of the urban river and lake to be treated, the method comprises the steps of manually adjusting the frequency of a frequency converter of an input water pump of the jet aerator and the angle of an air inlet adjusting valve, recording the frequency of the water pump, the values of a pressure detector, the flow rate of an air inlet flowmeter and a DO detection device, calculating the optimal value, simultaneously obtaining the corresponding condition and proportion of the value of the pressure detector and the air inlet flow, and obtaining a viscosity coefficient and a mixing ratio table through a plurality of times of experimental treatment.
The electric adjustable air valve in the execution module controls the air inflow of the air based on the optimal mixing ratio, and adjusts the water inflow and the air inflow of the jet aerator to ensure that the jet aerator works under the optimal working condition.
In summary, the programmable controller, the acquisition module and the execution module provided by the application can realize that the sizes of formed bubbles can be changed by adjusting the flow rate of input liquid, adjusting the air suction amount, adjusting the (length) volume of the mixing tube, increasing turbulence-forming components and the like. The device changes the size of formed bubbles by adjusting the liquid flow input by the jet aerator and the air suction amount so as to adapt to the requirement of river and lake water body treatment.
It should be noted that, for simplicity of description, the above-mentioned method embodiments are described as a series of acts or combination of acts, but those skilled in the art will recognize that the present application is not limited by the order of acts described, as some steps may occur in other orders or concurrently depending on the application. Further, those skilled in the art should also appreciate that the embodiments described in the specification are preferred embodiments and that the acts and modules referred to are not necessarily required in this application.
In the foregoing embodiments, the descriptions of the respective embodiments have respective emphasis, and for parts that are not described in detail in a certain embodiment, reference may be made to related descriptions of other embodiments.
In the embodiments provided in the present application, it should be understood that the disclosed apparatus may be implemented in other manners. For example, the above-described embodiments of the apparatus are merely illustrative, and for example, the above-described division of the units is only one type of division of logical functions, and other divisions may be realized in practice, for example, a plurality of units or components may be combined or integrated into another system, or some features may be omitted, or not executed. In addition, the shown or discussed mutual coupling or direct coupling or communication connection may be an indirect coupling or communication connection of some interfaces, devices or units, and may be an electric or other form.
The units described as separate parts may or may not be physically separate, and parts displayed as units may or may not be physical units, may be located in one place, or may be distributed on a plurality of network units. Some or all of the units can be selected according to actual needs to achieve the purpose of the solution of the embodiment.
In addition, functional units in the embodiments of the present application may be integrated into one processing unit, or each unit may exist alone physically, or two or more units are integrated into one unit. The integrated unit can be realized in a form of hardware, and can also be realized in a form of a software functional unit.
The integrated unit may be stored in a computer readable memory if it is implemented in the form of a software functional unit and sold or used as a stand-alone product. Based on such understanding, the technical solution of the present application may be substantially implemented or a part of or all or part of the technical solution contributing to the prior art may be embodied in the form of a software product stored in a memory, and including several instructions for causing a computer device (which may be a personal computer, a server, or a network device) to execute all or part of the steps of the above-mentioned method of the embodiments of the present application. And the aforementioned memory comprises: a U-disk, a Read-Only Memory (ROM), a Random Access Memory (RAM), a removable hard disk, a magnetic or optical disk, and other various media capable of storing program codes.
Those skilled in the art will appreciate that all or part of the steps in the methods of the above embodiments may be implemented by associated hardware instructed by a program, which may be stored in a computer-readable memory, which may include: flash Memory disks, Read-Only memories (ROMs), Random Access Memories (RAMs), magnetic or optical disks, and the like.
The foregoing detailed description of the embodiments of the present application has been presented to illustrate the principles and implementations of the present application, and the above description of the embodiments is only provided to help understand the method and the core concept of the present application; meanwhile, for a person skilled in the art, according to the idea of the present application, there may be variations in the specific embodiments and the application scope, and in summary, the content of the present specification should not be construed as a limitation to the present application.
Claims (8)
1. A control device suitable for a river and lake jet aerator comprises the jet aerator and a submersible pump, and is characterized by also comprising a programmable controller, an acquisition module and an execution module;
the programmable controller is connected with the jet aerator through the submersible pump and the execution module;
the acquisition module comprises a water level detector, a water body DO detector, a water temperature detector and a pressure detector;
the water level detector, the water body DO detector and the water temperature detector are electrically connected with the programmable controller, and are arranged in corresponding mounting positions of the water body;
the pressure detector is arranged between the execution module and the jet aerator.
2. The control device suitable for the river and lake jet aerator according to claim 1, further comprising a frequency converter for adjusting the pumping amount or/and the water delivery amount of the submersible pump, wherein the frequency converter is arranged between the programmable controller and the submersible pump, and the programmable controller is electrically connected with the submersible pump through the frequency converter.
3. The control device for the river and lake jet aerator as claimed in claim 1, wherein the execution module comprises an electric adjustable gas valve, and the electric adjustable gas valve is connected with the jet aerator through a pressure detector.
4. The control device for the river and lake jet aerator as claimed in claim 3, further comprising a float flow meter for monitoring the flow rate of the inlet air, wherein the float flow meter is connected with the electric adjustable air valve.
5. A control method of a river and lake jet aerator, which is suitable for the control device of the river and lake jet aerator as claimed in any claim 1-4, and is characterized by comprising the following steps:
acquiring detection data of a DO detector, detection data of a water temperature detector and detection data of a water level detector, wherein the detection data are real-time data;
inputting the detection data into a water working condition detection model in the programmable controller to obtain the water working condition, and determining the viscosity coefficients and the optimal mixing ratio of the liquid and the gas based on the water working condition;
and the electric adjustable gas valve in the execution module controls the gas inflow based on the optimal mixing ratio.
6. The method for controlling the river and lake jet aerator according to claim 5, wherein the step of inputting the detection data into the water working condition detection model in the programmable controller to obtain the water working conditions further comprises the steps of, before determining viscosity coefficients and an optimal mixing ratio of the liquid and the gas based on the water working conditions:
the method comprises the steps of collecting detection data of a plurality of water body DO detectors, detection data of water temperature detectors and detection data of water level detectors in advance, analyzing the detection data of the water body DO detectors, the detection data of the water temperature detectors and the detection data of the water level detectors in a preset analysis mode to obtain a plurality of water body working conditions, enabling the detection data to correspond to the water body working conditions one by one to obtain an analysis data set, inputting the analysis data set into a deep neural network algorithm to conduct deep learning, and obtaining a water body working condition detection model.
7. The method as claimed in claim 6, wherein the predetermined analysis method includes decision tree analysis and Delphi method.
8. The method for controlling the river and lake jet aerator according to claim 5, wherein the viscosity coefficients and the optimal mixing ratio of the liquid and the gas are determined based on the working conditions of the water body, specifically,
and matching the water working condition with a preset viscosity coefficient and a mixing ratio table, wherein the viscosity coefficient and the mixing ratio table comprise the preset water working condition, the preset viscosity coefficient and the preset mixing ratio, the preset water working condition, the preset viscosity coefficient and the preset mixing ratio are in one-to-one correspondence, and when the water working condition is completely coincided with the preset water working condition, the preset viscosity coefficient and the preset mixing ratio corresponding to the preset water working condition are selected to be the viscosity coefficient and the optimal mixing ratio of liquid and gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111022761.3A CN113582326B (en) | 2021-09-01 | 2021-09-01 | Control device and method suitable for river and lake jet aerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111022761.3A CN113582326B (en) | 2021-09-01 | 2021-09-01 | Control device and method suitable for river and lake jet aerator |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113582326A true CN113582326A (en) | 2021-11-02 |
CN113582326B CN113582326B (en) | 2024-01-30 |
Family
ID=78240821
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202111022761.3A Active CN113582326B (en) | 2021-09-01 | 2021-09-01 | Control device and method suitable for river and lake jet aerator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113582326B (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103663674A (en) * | 2013-12-18 | 2014-03-26 | 清华大学 | Real-time control device and control method for blast aeration process of sewage treatment plant |
CN105929767A (en) * | 2016-07-05 | 2016-09-07 | 广州资源环保科技股份有限公司 | River automatic control system capable of carrying out automatic monitoring and automatic aeration remotely |
CN205721251U (en) * | 2016-06-16 | 2016-11-23 | 河南和方科技有限公司 | Surface aeration equipment Digitizing And Control Unit |
CN110683664A (en) * | 2019-09-26 | 2020-01-14 | 河海大学 | Aeration system for river restoration |
-
2021
- 2021-09-01 CN CN202111022761.3A patent/CN113582326B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103663674A (en) * | 2013-12-18 | 2014-03-26 | 清华大学 | Real-time control device and control method for blast aeration process of sewage treatment plant |
CN205721251U (en) * | 2016-06-16 | 2016-11-23 | 河南和方科技有限公司 | Surface aeration equipment Digitizing And Control Unit |
CN105929767A (en) * | 2016-07-05 | 2016-09-07 | 广州资源环保科技股份有限公司 | River automatic control system capable of carrying out automatic monitoring and automatic aeration remotely |
CN110683664A (en) * | 2019-09-26 | 2020-01-14 | 河海大学 | Aeration system for river restoration |
Also Published As
Publication number | Publication date |
---|---|
CN113582326B (en) | 2024-01-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103041723B (en) | Micro-bubble generation device | |
CN205461848U (en) | Bubble generating device | |
CN212819194U (en) | Micro-nano bubble generating device | |
CN109607837A (en) | A kind of sanitary sewage aeration treatment apparatus being equipped with settling tank | |
CN204173971U (en) | In sulfate process titanium dioxide production acid waste water and aerator tank | |
CN113582326A (en) | Control device and method suitable for river and lake jet aerator | |
CN206486351U (en) | A kind of sewage disposal system with accurate jet-flow aeration system | |
CN203461870U (en) | Ozone oxidation device for processing secondary biological treatment effluent of urban sewage plant | |
CN204873999U (en) | Micropore aeration pipe | |
Yadav et al. | Design characteristics of venturi aeration system | |
CN213012226U (en) | High-efficiency double-suction gas-dissolved oxygen mixer | |
CN105036339A (en) | Integrated anaerobic ammonia oxidation reactor | |
CN208327539U (en) | A kind of air conducting water treatment facilities | |
CN211035380U (en) | Pressurized dissolved air injection mixing ozone oxidation device | |
CN204848421U (en) | Rotatory jet aeration equipment of frequency conversion | |
CN208791281U (en) | Opel oxidation ditch | |
CN108328756A (en) | A kind of air conducting water treatment facilities, system and method | |
CN217947720U (en) | Air stripping device | |
CN111453935A (en) | Molecular-level dense-phase rectification magnetic coupling dissolved oxygen device and ecological activity restoration system | |
CN205773660U (en) | There is the aerating system of defecator | |
CN219907216U (en) | Adjustable efficient gas stripping reflux device | |
CN111018108A (en) | Integrated AAO oxidation ditch device | |
CN218146027U (en) | Intelligent aeration control system for water treatment | |
CN221141449U (en) | Automatic aeration equipment of waste water | |
CN201424389Y (en) | Reverse osmosis vacuum degassing device |
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 |