CN110615489A - Configuration monitoring output system for BDP process industrial sewage treatment - Google Patents
Configuration monitoring output system for BDP process industrial sewage treatment Download PDFInfo
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- CN110615489A CN110615489A CN201910924462.5A CN201910924462A CN110615489A CN 110615489 A CN110615489 A CN 110615489A CN 201910924462 A CN201910924462 A CN 201910924462A CN 110615489 A CN110615489 A CN 110615489A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
- C02F2103/38—Polymers
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- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Testing And Monitoring For Control Systems (AREA)
Abstract
The invention belongs to the technical field of BDP process industrial sewage treatment systems, and particularly relates to a configuration monitoring output system for BDP process industrial sewage treatment. The system comprises an interface of a sewage treatment plant in the process industry, an equipment graphic control interface picture, a control interface with liquid level control equipment, a control interface of gate valve equipment, a control interface of time control equipment, a control interface of a mud scraper system, a control interface of an aeration fan system, a configuration monitoring output system for a BDP process industrial sewage treatment operation system and a configuration monitoring output system for finishing system operation and data output control.
Description
Technical Field
The invention belongs to the technical field of BDP process industrial sewage treatment systems, and particularly relates to a configuration monitoring output system for BDP process industrial sewage treatment.
Background
The bisphenol A phosphate oligomer of the configuration monitoring output system for BDP process industrial sewage treatment is BDP for short, and is a novel phosphorus flame retardant. BDP is usually synthesized by a two-step method, firstly, phosphorus oxychloride and bisphenol A are condensed into an intermediate product bisphenol A tetrachlorodiphosphonate under the action of a catalyst magnesium chloride, then the intermediate product bisphenol A tetrachlorodiphosphonate and phenol are subjected to esterification reaction to obtain a crude product of bisphenol A type phosphate oligomer, finally, solvents of toluene and methyl cyclohexane with equal mass are added into the crude product, and the final high-purity product is obtained through multiple acid washing, alkali washing and water washing processes. The waste water with high salt (main salt is NaOH and NaCl) and high toxicity (main components are phenol and bisphenol A) is generated in the production process, and simultaneously contains a large amount of macromolecular substances which are difficult to degrade (mainly polycondensation byproducts such as dimers, trimers, polymers and the like), and the waste water has the characteristics of large water discharge amount, difficult degradation and the like, is difficult to degrade under natural environmental conditions, is easy to enrich in organisms through food chains, and is recognized high-toxicity waste water.
At present, the BDP process industrial sewage treatment configuration monitoring output system has fewer treatment methods aiming at the wastewater at home and abroad, and the treatment mainly adopts the combination of physical chemistry and biochemistry. Physicochemical methods including incineration, wet oxidation, membrane methods, and the like; biochemical methods, mainly including activated sludge method and biofilm method; but the physical and chemical method has the disadvantages of high treatment cost, large investment and short membrane life. The biochemical method is convenient to operate and manage, but because organic matters in the wastewater have high toxicity, are difficult to degrade and have poor biodegradability, the organic matters directly enter a biochemical system to cause great impact on microorganisms, and the growth of the microorganisms is seriously inhibited. Moreover, the biochemical method has good treatment effect on aliphatic hydrocarbon and poor treatment effect on high-toxicity aromatic compounds, and particularly, a large amount of polycyclic substances exist in wastewater.
The BDP process industrial sewage treatment configuration monitoring output system generally adopts physicochemical pretreatment and biochemical treatment combined treatment with the lowest cost, but in physical pretreatment, micro-electrolysis and Fenton need to adjust acid of the wastewater, and a large amount of acid and alkali can be consumed by the strong alkali wastewater to generate a large amount of iron mud; advanced oxidation processes, such as catalytic oxidation, electrochemical processes, require catalysts with high costs, high investment and high operating costs, and the latter have high requirements on equipment and complex technology. The ozone oxidation method has strong oxidizability, and particularly has good treatment effect on benzene ring substances. The half-life of ozone is only half an hour, the reaction is thorough, no sludge and secondary pollution exist, the reaction is less influenced by the environment, the wastewater is directly treated without adjusting the pH value, and the ozone is prepared on site, so that the problems of storage and transportation of raw materials do not exist, and the operation and management are convenient.
Disclosure of Invention
The invention aims to provide a configuration monitoring output system for BDP process industrial sewage treatment operation system to complete system operation and data output control.
The invention discloses a configuration monitoring output system for BDP process industrial sewage treatment, which comprises
The interface of the industrial sewage treatment plant is used for displaying the arrangement of the plant area, instrument data and equipment operation conditions, the equipment flickers when running, the equipment operation class of the rotating class rotates, and the equipment of the moving class moves when running;
the method comprises the steps that an equipment graphic control interface picture is displayed, equipment graphics in the picture can pop up a control interface of the equipment when a left key is clicked, when the equipment control mode is remote, a 'start' button can be clicked through the left key to start the current equipment, after the equipment is successfully started, the running state of the equipment can be displayed, a 'stop' button is clicked, and the current equipment is stopped;
when the equipment control mode is remote, the equipment control is selected to be liquid level, the start and stop of the equipment are controlled through operating a start button and a stop button, and when the equipment control mode is remote, the start and stop of the equipment are controlled through a liquid level index; the liquid level index is set in the alarm picture, the upper limit value starts the equipment, the lower limit value stops the equipment, and the alarm picture is popped up by clicking the alarm picture button in the main picture, so that the picture not only can set the upper limit and the lower limit alarm values of the liquid level control, but also can set the upper limit and the lower limit of all instruments needing the alarm index in a plant area. If the current actual value is not in the upper and lower limit intervals, an alarm state exists, the alarm state is lower than the lower limit display lower limit alarm and higher than the upper limit display upper limit alarm;
the control interface of the gate valve type equipment is characterized in that when the equipment control mode is long-distance, an 'opening' button is clicked, the gate valve can be opened, the running state of the equipment displays 'running', the 'full-opening' is displayed until the equipment is fully opened, the 'closing' is clicked, the gate valve can be closed, the running state of the equipment displays 'running', the 'full-closing' is displayed until the equipment is fully closed, if the 'stopping' is clicked in the running process of the gate valve, the gate valve stops to the current opening, and the running state of the equipment displays 'half-opening';
control interface of the time control device: when the equipment control mode is remote and the equipment control selection is remote, the start and stop of the equipment can be controlled by operating a start button and a stop button, and when the equipment control mode is remote and the equipment control selection is time, the start and stop of the equipment are automatically controlled by setting the running time length and the stop time length;
control interface of the mud scraper system: when the equipment control mode is remote, clicking a starting button of the traveling system to start the 1# and 2# sludge pumps, starting the traveling after 15 seconds to advance, stopping the 1# and 2# sludge pumps when the traveling reaches an advancing limit, starting the 3# and 4# sludge pumps, starting the traveling after 15 seconds to return, repeating the steps, and clicking a stopping button of the traveling system to stop the sludge pumps and the traveling; clicking a fan starting button to start the fan, and clicking a fan stopping button to stop the fan;
the control interface of the aeration fan system displays the seed running state of the aeration fan, the motor parameters, the dissolved oxygen value of the BDP pool and the water temperature. When the 'press speed-up' button is pressed, the frequency of the motor will be slowly increased, and when the 'press speed-up' button is released, the frequency of the motor will stop changing; when the 'press down' button is pressed, the motor frequency will be slowly reduced, and when the 'press down' button is released, the motor frequency will stop changing. The measuring range of the dissolved oxygen value can be modified in the picture, the value behind the upper limit of the dissolved oxygen value of the motor is set, and the value is input.
Detailed Description
The invention is described in detail below with reference to specific embodiments.
The invention aims to provide a configuration monitoring output system for BDP process industrial sewage treatment operation system to complete system operation and data output control.
The invention discloses a configuration monitoring output system for BDP process industrial sewage treatment, which comprises
The interface of the industrial sewage treatment plant is used for displaying the arrangement of the plant area, instrument data and equipment operation conditions, the equipment flickers when running, the equipment operation class of the rotating class rotates, and the equipment of the moving class moves when running;
the method comprises the steps that an equipment graphic control interface picture is displayed, equipment graphics in the picture can pop up a control interface of the equipment when a left key is clicked, when the equipment control mode is remote, a 'start' button can be clicked through the left key to start the current equipment, after the equipment is successfully started, the running state of the equipment can be displayed, a 'stop' button is clicked, and the current equipment is stopped;
when the equipment control mode is remote, the equipment control is selected to be liquid level, the start and stop of the equipment are controlled through operating a start button and a stop button, and when the equipment control mode is remote, the start and stop of the equipment are controlled through a liquid level index; the liquid level index is set in the alarm picture, the upper limit value starts the equipment, the lower limit value stops the equipment, and the alarm picture is popped up by clicking the alarm picture button in the main picture, so that the picture not only can set the upper limit and the lower limit alarm values of the liquid level control, but also can set the upper limit and the lower limit of all instruments needing the alarm index in a plant area. If the current actual value is not in the upper and lower limit intervals, an alarm state exists, the alarm state is lower than the lower limit display lower limit alarm and higher than the upper limit display upper limit alarm;
the control interface of the gate valve type equipment is characterized in that when the equipment control mode is long-distance, an 'opening' button is clicked, the gate valve can be opened, the running state of the equipment displays 'running', the 'full-opening' is displayed until the equipment is fully opened, the 'closing' is clicked, the gate valve can be closed, the running state of the equipment displays 'running', the 'full-closing' is displayed until the equipment is fully closed, if the 'stopping' is clicked in the running process of the gate valve, the gate valve stops to the current opening, and the running state of the equipment displays 'half-opening';
control interface of the time control device: when the equipment control mode is remote and the equipment control selection is remote, the start and stop of the equipment can be controlled by operating a start button and a stop button, and when the equipment control mode is remote and the equipment control selection is time, the start and stop of the equipment are automatically controlled by setting the running time length and the stop time length;
control interface of the mud scraper system: when the equipment control mode is remote, clicking a starting button of the traveling system to start the 1# and 2# sludge pumps, starting the traveling after 15 seconds to advance, stopping the 1# and 2# sludge pumps when the traveling reaches an advancing limit, starting the 3# and 4# sludge pumps, starting the traveling after 15 seconds to return, repeating the steps, and clicking a stopping button of the traveling system to stop the sludge pumps and the traveling; clicking a fan starting button to start the fan, and clicking a fan stopping button to stop the fan;
the control interface of the aeration fan system displays the seed running state of the aeration fan, the motor parameters, the dissolved oxygen value of the BDP pool and the water temperature. When the 'press speed-up' button is pressed, the frequency of the motor will be slowly increased, and when the 'press speed-up' button is released, the frequency of the motor will stop changing; when the 'press down' button is pressed, the motor frequency will be slowly reduced, and when the 'press down' button is released, the motor frequency will stop changing. The measuring range of the dissolved oxygen value can be modified in the picture, the value behind the upper limit of the dissolved oxygen value of the motor is set, and the value is input;
finally, it should be noted that the above embodiments are only used for illustrating the technical solutions of the present invention, and not for limiting the protection scope of the present invention, although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications or equivalent substitutions can be made on the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention.
Claims (6)
1. A configuration monitoring output system for BDP process industrial sewage treatment is characterized by comprising a process industrial sewage treatment plant interface, a data acquisition unit and a data acquisition unit, wherein the process industrial sewage treatment plant interface is used for displaying the arrangement of a plant area, instrument data and equipment operation conditions, equipment flickers when running, equipment operation of a rotating type rotates, and equipment of a moving type moves when running;
the method comprises the steps that an equipment graphic controls an interface picture, a control interface of the equipment can be popped up when a left key is used for clicking an equipment graphic in the picture, when the equipment control mode is remote, a 'start' button can be clicked through the left key to start the current equipment, after the equipment is successfully started, the running state of the equipment can be displayed, a 'stop' button is clicked, and the current equipment is stopped.
2. The BDP process industrial sewage treatment configuration monitoring output system of claim 1, comprising a control interface with liquid level control equipment, wherein when the equipment control mode is remote and the equipment control is selected to be remote, the start and stop of the equipment can be controlled by operating start and stop buttons, and when the equipment control mode is remote and the equipment control is selected to be liquid level, the start and stop of the equipment are controlled by a liquid level index; the liquid level index is set in the alarm picture, the upper limit value starts the equipment, the lower limit value stops the equipment, and the alarm picture is popped up by clicking the alarm picture button in the main picture, so that the picture not only can set the upper limit and the lower limit alarm values of the liquid level control, but also can set the upper limit and the lower limit of all instruments needing the alarm index in a plant area. If the current actual value is not in the upper and lower limit interval, an alarm state is generated, the alarm state is lower than the lower limit display lower limit alarm and higher than the upper limit display upper limit alarm.
3. The BDP process industrial sewage treatment configuration monitoring output system of claim 1, comprising a control interface of gate valve type equipment, wherein when the equipment control mode is remote, clicking an 'open' button can open the gate valve, and the equipment operation state shows 'operation' until full opening, displaying 'full opening', clicking 'close', can close the gate valve, and the equipment operation state shows 'operation' until full closing, displaying 'full closing', and if clicking 'stop' in the process of gate valve operation, the gate valve stops to the current opening, and the equipment operation state shows 'half opening'.
4. The BDP process industrial sewage treatment configuration monitoring output system of claim 1, comprising a control interface of a time control device: when the equipment control mode is remote and the equipment control selection is remote, the start and stop of the equipment can be controlled by operating the start button and the stop button, and when the equipment control mode is remote and the equipment control selection is time, the start and stop of the equipment are automatically controlled by setting the running time length and the stop time length.
5. The BDP process industrial sewage treatment configuration monitoring output system of claim 1, comprising a control interface of a mud scraper system: when the equipment control mode is remote, clicking a starting button of the traveling system to start the 1# and 2# sludge pumps, starting the traveling after 15 seconds to advance, stopping the 1# and 2# sludge pumps when the traveling reaches an advancing limit, starting the 3# and 4# sludge pumps, starting the traveling after 15 seconds to return, repeating the steps, and clicking a stopping button of the traveling system to stop the sludge pumps and the traveling; clicking the fan starting button can start the fan, and clicking the fan stopping button can stop the fan.
6. The BDP process industrial sewage treatment configuration monitoring output system of claim 1, wherein the control interface of the aeration fan system displays the operation state of the aeration fan, the motor parameters, the dissolved oxygen value of the BDP pool and the water temperature. When the 'press speed-up' button is pressed, the frequency of the motor will be slowly increased, and when the 'press speed-up' button is released, the frequency of the motor will stop changing; when the 'press down' button is pressed, the motor frequency will be slowly reduced, and when the 'press down' button is released, the motor frequency will stop changing. The measuring range of the dissolved oxygen value can be modified in the picture, the value behind the upper limit of the dissolved oxygen value of the motor is set, and the value is input.
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| CN201910924462.5A CN110615489A (en) | 2019-09-27 | 2019-09-27 | Configuration monitoring output system for BDP process industrial sewage treatment |
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| CN201910924462.5A CN110615489A (en) | 2019-09-27 | 2019-09-27 | Configuration monitoring output system for BDP process industrial sewage treatment |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110258837A1 (en) * | 2008-12-23 | 2011-10-27 | Xoma Technology Ltd. | Flexible manufacturing system |
| CN103034211A (en) * | 2012-12-19 | 2013-04-10 | 江南大学 | Wastewater treatment process monitoring system based on wireless network |
| CN105800755A (en) * | 2016-05-12 | 2016-07-27 | 上海应用技术学院 | Water quality online monitoring system and method of wastewater coagulation treatment unit |
| CN205676212U (en) * | 2016-06-07 | 2016-11-09 | 河南和方科技有限公司 | Intelligent sewage processing system |
| CN107585948A (en) * | 2016-07-10 | 2018-01-16 | 李忠久 | A kind of oxidation ditch activated sludge process sewage treatment control system |
| CN108946840A (en) * | 2018-08-03 | 2018-12-07 | 东莞市达成机械设备制造有限公司 | A kind of sewage disposal device touch screen mainly controls the control method of picture |
-
2019
- 2019-09-27 CN CN201910924462.5A patent/CN110615489A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110258837A1 (en) * | 2008-12-23 | 2011-10-27 | Xoma Technology Ltd. | Flexible manufacturing system |
| CN103034211A (en) * | 2012-12-19 | 2013-04-10 | 江南大学 | Wastewater treatment process monitoring system based on wireless network |
| CN105800755A (en) * | 2016-05-12 | 2016-07-27 | 上海应用技术学院 | Water quality online monitoring system and method of wastewater coagulation treatment unit |
| CN205676212U (en) * | 2016-06-07 | 2016-11-09 | 河南和方科技有限公司 | Intelligent sewage processing system |
| CN107585948A (en) * | 2016-07-10 | 2018-01-16 | 李忠久 | A kind of oxidation ditch activated sludge process sewage treatment control system |
| CN108946840A (en) * | 2018-08-03 | 2018-12-07 | 东莞市达成机械设备制造有限公司 | A kind of sewage disposal device touch screen mainly controls the control method of picture |
Non-Patent Citations (2)
| Title |
|---|
| 温淑玲: "《电气自动化技术专业技能训练教程（下）》", 31 August 2013, 合肥工业大学出版社 * |
| 盛力: "《水处理装备装置实验技术》", 30 June 2016, 同济大学出版社 * |
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Application publication date: 20191227 |
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