CN214693467U - Intelligent control system for kitchen biogas slurry MBR (membrane bioreactor) membrane system - Google Patents
Intelligent control system for kitchen biogas slurry MBR (membrane bioreactor) membrane system Download PDFInfo
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- CN214693467U CN214693467U CN202023102506.3U CN202023102506U CN214693467U CN 214693467 U CN214693467 U CN 214693467U CN 202023102506 U CN202023102506 U CN 202023102506U CN 214693467 U CN214693467 U CN 214693467U
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Abstract
The utility model relates to an intelligent control system for meal kitchen natural pond liquid MBR membrane system, it includes filtration system, cleaning system and control system. The filtration system comprises a membrane pool, a water production pump, a water production tank and a plurality of MBR membrane modules, and the cleaning system comprises a backwashing water tank, a backwashing pump, a pipeline mixer and a plurality of medicine storage tanks. The kitchen biogas slurry is filtered by the filtering system through the MBR membrane assembly, the MBR membrane assembly is effectively cleaned by the cleaning system to ensure that the MBR membrane assembly can normally operate, and the control system controls each component in the filtering system and the cleaning system in real time to realize automatic switching between the filtering function and the cleaning function. The MBR membrane system realizes automatic operation to the maximum extent, reduces manual operation, is convenient to maintain, and greatly reduces the management difficulty and the labor input. The cleaning system realizes the on-line cleaning of the MBR membrane component, avoids the MBR membrane component from being lifted out and off-line cleaned, reduces the occurrence of broken filaments, increases the running stability of the membrane system, and reduces the occupied area.
Description
Technical Field
The utility model relates to a water treatment technical field especially relates to an intelligent control system that is used for meal kitchen natural pond liquid MBR membrane system.
Background
In recent years, along with the vigorous promotion of garbage classification in China, a large number of kitchen treatment projects are put on the market, the kitchen biogas slurry has high treatment difficulty due to the characteristics of oil content, high salt content, unbalanced carbon-nitrogen ratio and the like, the engineering application in the field of kitchen biogas slurry treatment is more at present, good effects are obtained mainly by adopting an MBR technology, and compared with the traditional method, the method has the advantages of high efficiency, low energy consumption, simple process, small floor area, no secondary pollution and the like, and is widely applied to the aspects of petrochemical industry, seawater desalination, food processing, municipal sewage treatment and the like.
However, the MBR technology has a great challenge of membrane pollution, in the separation process, macromolecules or suspended particles dissolved in the solution to be treated can deposit on the wall of a membrane pore and the surface of the membrane, block the membrane pore, reduce the membrane flux, shorten the service life of the membrane, increase the energy consumption and the operation cost, and simultaneously, because the MBR membrane system has high acquisition cost, high requirements on operation, maintenance and cleaning, improper operation, maintenance and cleaning and short service life of the MBR membrane module.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In view of the above shortcoming, the not enough of prior art, the utility model provides an intelligent control system for meal kitchen natural pond liquid MBR membrane system, it has solved the big technical problem of MBR membrane system operation maintenance and washing degree of difficulty.
(II) technical scheme
In order to achieve the above object, the utility model discloses an intelligent control system for meal kitchen natural pond liquid MBR membrane system includes:
a filtration system, a cleaning system and a control system;
the filtering system comprises a membrane pool, a water production pump, a water production tank and a plurality of MBR membrane modules;
the MBR membrane modules are arranged in the membrane pool, the outlets of the MBR membrane modules are connected with the inlet of the water production tank through a water production pipeline, the water production pump is arranged on the water production pipeline, and a water production valve is arranged between the inlet of the water production pipeline and the outlet of each MBR membrane module;
the cleaning system comprises a backwashing water tank, a backwashing pump, a pipeline mixer and a plurality of medicine storage boxes;
the outlet of the backwashing water tank is connected with a plurality of backwashing branch pipes through a backwashing pipeline, the backwashing branch pipes are connected with the outlets of the MBR membrane assemblies in a one-to-one correspondence manner, backwashing valves are arranged on the backwashing branch pipes, the inlet of the backwashing water tank is connected with the inlet of the water production tank, the pipeline mixer and the backwashing pump are arranged on the backwashing pipeline, the first outlet of the medicine storage tank is connected with the pipeline mixer through a first feeding pump, and the second outlet of the medicine storage tank is connected with the inlet of the backwashing water tank through a second feeding pump;
the water producing pump, the backwashing pump, the water producing valve, the backwashing valve, the first adding pump and the second adding pump are in signal connection with the control system.
Optionally, an outlet of each water production valve is connected to an inlet of the water production pump through a water production branch pipe, and a water production pressure sensor is arranged on each water production branch pipe;
a water production turbidity meter, a water production flow meter and a water production outlet valve are sequentially arranged on the water production pipeline from the outlet of the water production pump to the inlet of the water production tank;
the water production pressure sensor, the water production turbidity meter, the water production flow meter and the water production water outlet valve are in signal connection with the control system.
Optionally, a backwashing water inlet pipeline and a backwashing water replenishing pipeline are arranged between the inlet of the water production tank and the inlet of the backwashing water tank;
an inlet of the backwashing water inlet pipeline is connected with an outlet of the water production tank, an outlet of the backwashing water inlet pipeline is connected with an inlet of the backwashing water tank, and a backwashing water inlet valve is arranged on the backwashing water inlet pipeline;
the inlet of the backwashing water supply pipeline is connected with the water production pipeline, the connection point of the backwashing water supply pipeline and the water production pipeline is positioned on the pipeline between the water production flowmeter and the water production outlet valve, the outlet of the backwashing water supply pipeline is connected with the inlet of the backwashing water tank, and the backwashing water supply pipeline is provided with a backwashing water supply valve;
and the backwashing water replenishing valve and the backwashing water inlet valve are in signal connection with the control system.
Optionally, a first liquid level meter is arranged in the medicine storage box and used for detecting the liquid level in the medicine storage box;
the medicine storage boxes comprise a sodium hypochlorite medicine storage box, a sodium hydroxide medicine storage box and a hydrochloric acid medicine storage box;
the first liquid level meter is in signal connection with the control system.
Optionally, a backwashing filter is further arranged on the backwashing pipeline, the backwashing water tank, the backwashing pump, the pipeline mixer and the backwashing filter are sequentially connected through the backwashing pipeline, and inlets of the backwashing valves are all connected with an outlet of the backwashing filter.
Optionally, a second liquid level meter and a PH meter are arranged in the backwash water tank, the second liquid level meter is used for detecting the liquid level in the backwash water tank, and the PH meter is used for detecting the PH value of the liquid in the backwash water tank;
a third liquid level meter is arranged in the water production tank, and a fourth liquid level meter is arranged in the membrane pool;
the second liquid level meter, the PH meter, the third liquid level meter and the fourth liquid level meter are all in signal connection with the control system.
Optionally, the backwashing water tank is connected with a cleaning water replenishing pipeline and a cleaning emptying pipeline;
an inlet of the cleaning water replenishing pipeline is connected with a tap water pipe network, an outlet of the cleaning water replenishing pipeline is connected with an inlet of the backwashing water tank, and a cleaning water replenishing valve is arranged on the cleaning water replenishing pipeline;
a water outlet is formed in the bottom of the backwashing water tank, an inlet of the cleaning emptying pipeline is connected with the water outlet, and a cleaning emptying valve is arranged on the cleaning emptying pipeline;
and the cleaning water supplementing valve and the cleaning emptying valve are in signal connection with the control system.
Optionally, the filtration system further comprises a fan, the fan is connected with the MBR membrane module through an aeration pipeline, and an air pressure sensor, an air valve and an air flow meter are arranged on the aeration pipeline;
the fan, the air pressure sensor, the air valve and the air flow meter are in signal connection with the control system.
Optionally, the filtering system further comprises a sewage discharge pipeline, a sludge return pipeline, a sludge discharge pipe, a sludge return tank and a sludge concentration tank;
a sewage discharge port is formed in the bottom of the membrane tank, the inlet of the sewage discharge pipeline is connected with the sewage discharge port, the inlets of the sludge return pipeline and the sludge discharge pipe are both connected with the outlet of the sewage discharge pipeline, the outlet of the sludge return pipeline is connected with the sludge return tank, and the outlet of the sludge discharge pipeline is connected with the sludge concentration tank;
a sludge pump is arranged on the sewage discharge pipeline, a sludge return valve is arranged on the sludge return pipeline, and a sludge discharge valve is arranged on the sludge discharge pipeline;
the sludge pump, the sludge return valve and the sludge discharge valve are in signal connection with the control system.
Optionally, the control system comprises a computer and a process controller, wherein an input end of the computer is in signal connection with the process controller;
the water production pump, the backwashing pump, the water production valve, the backwashing valve, the first feeding pump and the second feeding pump are all in signal connection with the process controller.
(III) advantageous effects
The MBR membrane system of the utility model realizes the automatic operation to the maximum extent, reduces the manual operation, is convenient to maintain, and greatly reduces the management difficulty and the labor input;
the system keeps high water production flux for a long time by controlling the real-time monitoring of the system and controlling the alternate operation of a plurality of cleaning modes, thereby reducing the energy consumption to a certain extent and lowering the operation cost;
the cleaning system realizes the on-line cleaning of the MBR membrane component, avoids the MBR membrane component from being lifted out and off-line cleaned, reduces the occurrence of broken filaments, increases the running stability of the membrane system and reduces the occupied area;
the control system controls operation control parameters such as operation time, interval period and the like of a backwashing mode, a chemical cleaning mode and a shutdown cleaning mode, and the membrane treatment system is cleaned in time, so that the membrane flux is effectively recovered, the service life of the membrane system is prolonged, and manual operation errors and irreversible damage to the membrane module are effectively avoided.
Drawings
Fig. 1 is a process flow diagram of the intelligent control system for the kitchen biogas slurry MBR membrane system of the utility model;
fig. 2 is the utility model discloses a process schematic diagram of an intelligent control system for meal kitchen natural pond liquid MBR membrane system.
[ description of reference ]
11: a membrane tank; 12: a water production pump; 13: a water production tank; 14: an MBR membrane module; 15: a water production valve; 16: a water production pressure sensor; 17: a produced water turbidity meter; 18: a produced water flow meter; 19: a water outlet valve for producing water; 20: backwashing a water replenishing valve; 21: backwashing the water inlet valve; 22: backwashing the filter; 23: a third liquid level meter;
41: a backwash water tank; 42: a backwash pump; 43: a pipeline mixer; 45: a sodium hypochlorite medicine storage box; 46: a sodium hydroxide storage tank; 47: a hydrochloric acid storage box; 48: a backwash valve; 49: sodium hypochlorite pump; 50: sodium hypochlorite secondary pump; 51: a pump of sodium hydroxide; 52: a sodium hydroxide secondary pump; 53: a pump for hydrochloric acid; 54: a second pump for hydrochloric acid; 55: a pH meter; 56: a second level gauge; 57: a fourth liquid level meter; 58: cleaning a water replenishing valve; 59: cleaning the emptying valve;
70: a vacuum pumping system;
81: a fan; 82: an air pressure sensor; 83: an air valve; 84: an air flow meter;
91: a sludge pump; 92: a sludge reflux valve; 93: a sludge return tank; 94: a sludge discharge valve; 95: a sludge concentration tank;
100: a computer; 101: a process controller.
Detailed Description
For a better understanding of the present invention, reference will now be made in detail to the present invention, examples of which are illustrated in the accompanying drawings.
In order to better understand the above technical solutions, exemplary embodiments of the present invention will be described in more detail below with reference to the accompanying drawings. While exemplary embodiments of the invention are shown in the drawings, it should be understood that the invention can be embodied in various forms and should not be limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art.
The utility model provides an intelligent control system for meal kitchen natural pond liquid MBR membrane system, as shown in figure 1, it includes filtration system, cleaning system and control system. The filtering system utilizes the MBR membrane module 14 to filter the kitchen biogas slurry, the cleaning system effectively cleans the filtering system to ensure that the filtering system can normally operate, and the control system controls each component in the filtering system and the cleaning system in real time to realize automatic switching between the filtering function and the cleaning function. The MBR membrane system realizes automatic operation to the maximum extent, reduces manual operation, is convenient to maintain, and greatly reduces the management difficulty and the labor input. The cleaning system realizes the online cleaning of the filtering system, avoids the MBR membrane module 14 in the filtering system from being lifted out for offline cleaning, reduces the occurrence of broken filaments, increases the running stability of the MBR membrane system, and simultaneously reduces the occupied area of the whole system. The filtering system comprises a membrane pool 11, a water production pump 12, a water production tank 13 and a plurality of groups of MBR membrane modules 14. A plurality of groups of MBR membrane modules 14 are arranged in the membrane tank 11 and used for filtering the sewage in the membrane tank 11. The outlet of each group of MBR membrane modules 14 is connected with the inlet of a water production tank 13 through a water production pipeline, a water production pump 12 is arranged on the water production pipeline, and the outlet of each MBR membrane module 14 is provided with an independent water production valve 15 for independently turning off or turning on the group of MBR membrane modules 14. When the filtering system is in operation, the MBR membrane module 14 filters the sewage in the membrane tank 11, the clear water filtered by the MBR membrane module 14 is extracted by the water production pump 12, and the clear water is conveyed to the water production tank 13 for storage and standby.
As shown in fig. 1, the washing system includes a backwash water tank 41, a backwash pump 42, a line mixer 43, and a plurality of medicine tanks. The outlet of the backwashing water tank 41 is connected with a plurality of backwashing branch pipes through backwashing pipelines, the backwashing branch pipes are connected with the outlets of the plurality of groups of MBR membrane modules 14 in a one-to-one correspondence manner, and each backwashing branch pipe is provided with a backwashing valve 48. The cleaning liquid in the backwash water tank 41 is flushed into the MBR membrane modules 14 from the outlets of the MBR membrane modules 14, so as to perform a backwash function on each group of MBR membrane modules 14, and remove macromolecular impurities or particles deposited on the membrane pore walls and the membrane surfaces of the MBR membrane modules 14, thereby improving the membrane flux of the MBR membrane modules 14 and prolonging the service life of the MBR membrane modules 14. The inlet of the backwashing water tank 41 is connected with the production water tank 13, and the backwashing water tank 41 directly obtains water required for cleaning from the production water tank 13 to recycle the filtered water. The pipeline mixer 43 and the backwashing pump 42 are both arranged on a backwashing pipeline, a first outlet of the medicine storage box is connected with the pipeline mixer 43 through a first feeding pump, and a second outlet of the medicine storage box is connected with an inlet of the backwashing water tank 41 through a second feeding pump. Each medicine storage box stores one cleaning agent correspondingly so as to deal with the condition that the MBR membrane module 14 is blocked due to different dirt. The water production pump 12, the backwashing pump 42, the water production valve 15, the backwashing valve 48, the first feeding pump and the second feeding pump are in signal connection with the control system. When the MBR membrane module 14 needs to be cleaned, the control system controls the operation states of the water production pump 12, the backwashing pump 42, the water production valve 15, the backwashing valve 48, the first adding pump and the second adding pump in real time, so that cleaning in different modes is realized. And during cleaning, the control system controls the filtering system to stop working and starts the cleaning system. The first mode is a backwashing mode, only a backwashing pump 42 in the cleaning system is started, the water production pump 12 and the water production valve 15 are closed, a backwashing valve 48 is opened, clean water in a backwashing water tank 41 is conveyed to each group of MBR membrane modules 14 through the backwashing pump 42, the MBR membrane modules 14 are backwashed, the cleaning process is short, and no medicament is needed; the second mode is a chemical cleaning mode, only a first feeding pump and a backwashing pump 42 in the cleaning system are started, the water production pump 12 and the water production valve 15 are closed, the backwashing valve 48 is opened, the first feeding pump conveys the medicament in the medicament storage tank to the pipeline mixer 43, the medicament is mixed with clean water and then conveyed to each group of MBR membrane modules 14 through the backwashing pump 42 for backwashing, the cleaning process is short, and the normal operation of the filtering system is not influenced; the third mode is a shutdown cleaning mode, only the second feeding pump and the backwashing pump 42 in the cleaning system are started, the water production pump 12 and the water production valve 15 are closed, the backwashing valve 48 is opened, the second feeding pump conveys the chemical in the chemical storage tank to the backwashing water tank 41, the chemical is mixed with the clean water in the backwashing water tank 41 and then conveyed to each group of MBR membrane modules 14 through the backwashing pump 42 for backwashing, the cleaning process is long, and the cleaning is more thorough. The control system controls operation control parameters such as operation time, interval period and the like of a backwashing mode, a chemical cleaning mode and a shutdown cleaning mode, and the membrane treatment system is cleaned in time, so that the membrane flux is effectively recovered, the service life of the membrane system is prolonged, and manual operation errors and irreversible damage to the membrane module are effectively avoided. By controlling the real-time monitoring of the system and controlling the alternate operation of various cleaning modes, the membrane system keeps higher water production flux for a long time, the energy consumption is reduced to a certain extent, and the operation cost is reduced.
As shown in fig. 1, the outlet of each water producing valve 15 is connected to the inlet of the water producing pump 12 through a water producing branch pipe, and a water producing pressure sensor 16 is arranged on each water producing branch pipe. A produced water turbidity meter 17, a produced water flow meter 18 and a produced water outlet valve 19 are sequentially arranged on the produced water pipeline from the outlet of the produced water pump 12 to the inlet of the produced water tank 13. The produced water pressure sensor 16, the produced water turbidity meter 17, the produced water flow meter 18 and the produced water outlet valve 19 are in signal connection with the control system. The water production outlet valve 19 is used for preventing water in the water production tank 13 from flowing backwards, the water production pressure sensor 16 is used for monitoring the water pressure in the water production branch pipe, the control system judges the water production efficiency of each group of MBR membrane modules 14 according to the value of the water production pressure sensor 16, and when the water production pressure is lower than a set value, the blockage situation of the group of MBR membrane modules 14 is serious, and the MBR membrane modules need to be cleaned. The produced water flowmeter 18 is used for detecting the flow of the water produced by all the MBR membrane modules 14 together, the produced water turbidimeter 17 is used for monitoring the cleaning degree of the water in the produced water pipeline, the control system acquires the values of the produced water flowmeter 18 and the produced water turbidimeter 17 in real time, so as to judge the volume and the cleaning degree of the produced water in the produced water pipeline, thereby judging the operation condition of the MBR membrane modules 14, and the control system monitors the turbidity of the produced water in real time, effectively ensures the quality of the produced water in the system operation, and simultaneously provides a powerful guarantee for the operation of the rear-end deep treatment system. Preferably, a vacuum pumping system 70 is further disposed downstream of the water production pump 12, after the MBR membrane module 14 is cleaned, the water production pipeline is vacuumized by the vacuum pumping system 70, so as to prevent waste gas in the water production pipeline from polluting produced water, and negative pressure is provided for the secondary operation of the filtering system, so that the water production pipeline is automatically and quickly filled with water, and the degree of automation and the operation efficiency are improved.
As shown in fig. 1, a backwash water inlet line and a backwash water replenishing line are provided between the inlet of the water production tank 13 and the inlet of the backwash water tank 41. Wherein, the inlet of the backwashing water inlet pipeline is connected with the outlet of the water production tank 13, the outlet of the backwashing water inlet pipeline is connected with the inlet of the backwashing water tank 41, and the backwashing water inlet pipeline is provided with a backwashing water inlet valve 21; the inlet of the backwashing water supplementing pipeline is connected with the water production pipeline, the connection point of the backwashing water supplementing pipeline and the water production pipeline is positioned on the pipeline between the water production flowmeter 18 and the water production outlet valve 19, the outlet of the backwashing water supplementing pipeline is connected with the inlet of the backwashing water tank 41, and the backwashing water supplementing pipeline is provided with a backwashing water supplementing valve 20. The backwashing water replenishing valve 20 and the backwashing water inlet valve 21 are in signal connection with a control system. Preferably, the product tank 13 is located above the backwash tank 41 and water in the product tank 13 is able to flow into the backwash tank 41 by gravity. The backwash water inlet line is used to reverse flow water in the product water tank 13 into the backwash water tank 41 to provide clean water for the cleaning system. When the backwashing water tank 41 is filled with water by utilizing the backwashing water inlet pipeline, the backwashing water supplementing valve 20 and the water producing and discharging valve 19 are controlled to be closed by the control system, and the backwashing water inlet valve 21 is opened. The backwashing water supply pipeline directly utilizes water produced by the MBR membrane module 14, and the water produced by the MBR membrane module 14 is conveyed to the backwashing water tank 41 through the water producing pump 12 to provide clear water for the cleaning system. When the backwashing water tank 41 is filled with water by using the backwashing water supply pipeline, the control system closes the water production outlet valve 19 and the backwashing water inlet valve 21, and opens the backwashing water supply valve 20.
As shown in fig. 1, each of the medicine boxes is provided with a first liquid level meter, the first liquid level meter is in signal connection with the control system and is used for detecting the liquid level in the medicine box, and the first liquid level meter is preferably an ultrasonic liquid level meter with strong corrosion resistance and high precision. The medicine storage boxes comprise a sodium hypochlorite medicine storage box 45, a sodium hydroxide medicine storage box 46 and a hydrochloric acid medicine storage box 47. When the control system detects that the sodium hydroxide medicine box 46, the hydrochloric acid medicine box 47 or the sodium hypochlorite medicine box 45 is lower than a set value, the control system sends out an alarm signal to prompt the user to add medicine. The sodium hydroxide medicine box 46 stores industrial-grade liquid sodium hydroxide solution with the concentration less than or equal to 30mg/L, the hydrochloric acid medicine box 47 stores industrial-grade hydrochloric acid with the concentration less than or equal to 31%, and the sodium hypochlorite medicine box 45 stores industrial-grade liquid sodium hypochlorite solution with the concentration less than or equal to 10%. When the MBR membrane module 14 is reversely cleaned, hydrochloric acid is used as an acid cleaning agent for acid cleaning, and a mixed solution obtained by mixing sodium hypochlorite and sodium hydroxide in proportion is used as an alkaline cleaning agent for alkaline cleaning. A small amount of sodium hypochlorite is added on the basis of alkaline cleaning to serve as an auxiliary cleaning agent, and compared with sodium hydroxide, the sodium hypochlorite can effectively remove organic dirt attached to the MBR membrane module 14, so that the MBR membrane module 14 can keep high permeability when filtering sewage with high organic matter content such as kitchen biogas slurry, and the filtering effect of the MBR membrane module 14 on the kitchen biogas slurry is improved; for sewage with low organic content, the MBR membrane module 14 is periodically cleaned by the mixture of sodium hypochlorite and sodium hydroxide, so that the condition that the MBR membrane module 14 is blocked by organic pollutants can be effectively prevented, the load of shutdown cleaning is reduced, and the working efficiency of the MBR membrane module 14 is improved.
As shown in fig. 1, the backwash pipeline is further provided with a backwash filter 22, the backwash water tank 41, the backwash pump 42, the line mixer 43 and the backwash filter 22 are connected in sequence by the backwash pipeline, and the inlets of the plurality of backwash valves 48 are connected to the outlet of the backwash filter 22. The filtration precision of the backwashing filter 22 is less than or equal to 5um, preferably a cartridge type cartridge filter, and the filter cartridge of the filter is replaced regularly, so that impurities in backwashing water and medicament can be filtered out, and the phenomenon that the impurities enter the interior of the MBR membrane module 14 to block the membrane holes and damage the MBR membrane module 14 in the cleaning process is avoided.
As shown in fig. 1, a second liquid level meter 56 and a PH meter 55 are disposed in the backwash water tank 41, the second liquid level meter 56 is used for detecting the liquid level in the backwash water tank 41, and the PH meter 55 is used for detecting the PH value of the liquid in the backwash water tank 41. A third liquid level meter 23 is arranged in the water production tank 13, and a fourth liquid level meter 57 is arranged in the membrane tank 11. Second level gauge 56, PH meter 55, third level gauge 23 and fourth level gauge 57 all with control system signal connection, control system obtains the liquid level in backwash water tank 41, product water tank 13 and the membrane pond 11 through second level gauge 56, third level gauge 23 and fourth level gauge 57, for subsequent operation provides data support, for example, when fourth level gauge 57 detects that the liquid level of membrane pond 11 is less than the setting value, control system sends out trouble alarm, indicate artifical futilely to predict and the automatic shutdown system operation. When the machine is stopped and the cleaning mode is performed, the control system obtains the pH value of the liquid in the backwashing water tank 41 through the pH meter 55, so that the medicament in the medicament storage tank and the clean water in the production water tank 13 are mixed into the cleaning liquid with the set pH value of the system.
As shown in fig. 1, a purge refill line and a purge drain line are connected to the backwash water tank 41. The inlet of the cleaning water replenishing pipeline is connected with a tap water pipe network, the outlet of the cleaning water replenishing pipeline is connected with the inlet of the backwashing water tank 41, and a cleaning water replenishing valve 58 is arranged on the cleaning water replenishing pipeline. When the MBR membrane module 14 is cleaned, if the liquid level in the backwash water tank 41 cannot reach the set value, the backwash water tank 41 is timely replenished with water through a tap water pipeline, so that the cleaning system cannot normally operate. The bottom of the backwashing water tank 41 is provided with a water outlet, the inlet of the cleaning emptying pipeline is connected with the water outlet, and the cleaning emptying pipeline is provided with a cleaning emptying valve 59. The cleaning evacuation line is used for evacuating the liquid in the backwash water tank 41, so that the liquid in the backwash water tank 41 can be rapidly evacuated when the two agents are switched to be used, and normal operation of a cleaning mode can be ensured. The cleaning water supplementing valve 58 and the cleaning emptying valve 59 are in signal connection with the control system, and the control system controls the on-off states of the cleaning water supplementing valve 58 and the cleaning emptying valve 59 in real time.
As shown in fig. 1, the filtration system further includes a blower 81, the blower 81 is connected to the MBR membrane modules 14 through an aeration pipeline, and the aeration pipeline is provided with an air valve 83 for adjusting aeration amount, an air flow meter 84 for detecting aeration amount of each group of MBR membrane modules 14, and an air pressure sensor 82 for detecting air pipe pressure. The fan 81, the air pressure sensor 82, the air valve 83 and the air flow meter 84 are all in signal connection with the control system. When the air flow meter 84 on the aeration pipeline of one of the plurality of groups of MBR membrane modules 14 detects that the air quantity is lower than a set value, the control system automatically adjusts the air valve 83 on the aeration pipeline, so as to ensure that the air quantity of each group of MBR membrane modules 14 reaches the set value, sludge accumulation and dirt generation among membrane filaments of the MBR membrane modules 14 is avoided, the fan 81 is electrically connected with the control system through a fan 81 frequency converter, and the control system adjusts the frequency of the fan 81 through comparison between the set air flow value and the air flow value detected by the air flow meter 84, so as to adjust the air quantity of the fan 81. When the control system detects that the pressure value of the air pressure sensor 82 is equal to 0bar, the control system sends out a fault alarm to prompt manual intervention and automatically stop the system to operate so as to protect the MBR membrane module 14, and after the fault is eliminated, the operation is recovered.
As shown in fig. 1, the filtration system further includes a sewage line, a sludge return line, a sludge discharge pipe, a sludge return tank 93, and a sludge concentration tank 95. The drain that is used for discharging the sedimentary silt in membrane pond 11 bottom is seted up to the bottom of membrane pond 11, and the entry and the drain of blowdown pipeline are connected, and the entry of mud return line and mud delivery pipe all is connected with the exit linkage of blowdown pipeline. Wherein, the outlet of the sludge return pipeline is connected with the sludge return tank 93, and the outlet of the sludge discharge pipeline is connected with the sludge concentration tank 95. A sludge pump 91 is arranged on the sewage discharge pipeline, a sludge return valve 92 is arranged on the sludge return pipeline, and a sludge discharge valve 94 is arranged on the sludge discharge pipeline. The sludge pump 91, the sludge return valve 92 and the sludge discharge valve 94 are in signal connection with the control system.
As shown in fig. 2, the control system includes a computer 100 and a process controller 101, and an input of the computer 100 is in signal connection with the process controller 101. The water production pump 12, the backwashing pump 42, the water production valve 15, the backwashing valve 48, the first feeding pump and the second feeding pump are all in signal connection with the process controller 101, all the valves, the sensors, the liquid level meter and the pH meter 55 are all connected with the process controller 101 as described above, a control program is stored in the computer 100, the operating condition of the MBR membrane system is judged by acquiring the on-off states of all the valves and the values of the sensors, the liquid level meter and the pH meter 55, the MBR membrane system is controlled to carry out a filtering operation mode, and the MBR membrane module 14 is cleaned by adopting different cleaning modes. The utility model discloses a MBR membrane system contains four kinds of modes: an operation mode, a backwashing mode, a chemical cleaning mode and a shutdown cleaning mode. The specific control process of the control system is as follows:
when normal filtration kitchen natural pond liquid of MBR membrane system, through the operation of computer 100 software program, automatic control starts the operation mode, and the concrete step of operation mode is as follows:
opening a water inlet valve to replenish water in the membrane tank 11, starting a vacuum pumping system 70 to operate for 30S (specific operation time can be flexibly set according to effects) after the water level of the set starting membrane tank 11 is reached, and opening a water production valve 15 corresponding to each group of MBR membrane modules 14;
secondly, starting the water producing pump 12, and enabling the system to enter an automatic running state;
when the system runs for 9min, the water production pump 12 and the water production valve 15 corresponding to each group of MBR membrane modules 14 are automatically closed, the water production pump 12 and the water production valve 15 corresponding to each group of MBR membrane modules 14 are opened after the system is stopped for 1min, the system automatically enters the next automatic running water production period so as to avoid damage of the MBR membrane modules 14, the service life of the MBR membrane modules 14 is prolonged, and the specific running and stopping time can be flexibly set and adjusted according to the actual running effect;
when the kitchen biogas slurry MBR membrane system is in the operation mode, the operation of the sludge pump 91 and the water production pump 12 are controlled in a linkage manner, namely the sludge pump 91 operates when the water production pump 12 operates in the operation mode state, and the sludge pump 91 is closed when the water production pump 12 is closed; the sludge return valve 92 and the sludge discharge valve 94 are respectively opened and closed according to time, and the respective opening time can be flexibly set according to actual operation conditions;
when the liquid level of the membrane pool 11 is at a set protection low liquid level, the system automatically stops the operation of the water production pump 12 and the sludge reflux pump and closes the corresponding water production pneumatic valve, the sludge reflux valve 92 and the sludge discharge valve 94, and after the liquid level of the membrane pool 11 is restored to a starting liquid level, the corresponding water production pneumatic valve, the sludge reflux valve 92 and the sludge discharge valve 94, the water production pump 12 and the sludge reflux pump are automatically started;
when the air pressure of the aeration air pipe is 0, the system automatically stops running, and the system resumes running after the fault is eliminated;
when the water production pressure of any one group of MBR membrane modules 14 in the MBR membrane modules 141, 142 and 14n is equal to-0.60 Mpa, automatically closing the corresponding water production valves 15 of the MBR membrane modules 14, automatically stopping the operation of the membrane array, popping up a dialog box requiring on-line cleaning or shutdown cleaning, and prompting timely cleaning to ensure that the MBR membrane modules 14 operate normally;
when the water production flow meter 18 displays that the water production flow lasts for 1 hour and is lower than the set water production flow, automatically prompting to request fault check or cleaning;
ninthly, when the Turbidity of the produced water is more than 5NTU (nephelometric turbidimetry unit), automatically stopping the operation of the MBR (membrane bioreactor) system of the kitchen biogas slurry, and sending a fault alarm by the control system to prompt manual inspection;
when the backwashing mode needs to be operated, the software program of the computer 100 is operated to automatically control and start the backwashing mode, and the backwashing mode comprises the following specific steps:
firstly, when a kitchen biogas slurry MBR membrane system is started to continuously operate for 12 periods (120min, one period is 10min, and the system can be flexibly adjusted), the system automatically closes a water production pump 12 and a water production valve 15 corresponding to each group of MBR membrane modules 14 in sequence, and enters a backwashing program;
opening a water production valve 15 corresponding to the first group of MBR membrane modules 14, and starting a backwashing pump 42 and a backwashing valve 48 corresponding to the first group of MBR membrane modules 14;
after 55 seconds, opening the water production valve 15 and the backwashing valve 48 corresponding to the second group of MBR membrane modules 14, and closing the water production valve 15 and the backwashing valve 48 corresponding to the first group of MBR membrane modules 14;
continuing sequentially until the last group of MBR membrane modules 14, setting the last group of MBR membrane modules 14 as the nth group, wherein n is a positive integer greater than 2, opening a water production valve 15 and a backwashing valve 48 corresponding to the nth group of MBR membrane modules 14 after 55 x n seconds, and closing the water production valve 15 and the backwashing valve 48 corresponding to the nth-1 group of MBR membrane modules 14;
after 55 × n +1 s, the backwashing is finished, the backwashing pump 42 is closed, the water production valve 15 and the backwashing valve 48 corresponding to the nth group of MBR membrane modules 14 are closed, the backwashing program is finished, and the operation mode is automatically entered (the opening and closing of each valve must be carried out after the previous operation is finished, and the opening and closing time delay of the pump and the valve is set according to the operation condition);
when the backwashing water tank 41 does not reach the set starting liquid level, the backwashing operation mode cannot be started to protect the backwashing pump 42, and when the backwashing water tank 41 is lower than the set liquid level in the operation mode, the backwashing water replenishing valve 20 is automatically opened to replenish water, and when the set highest liquid level is reached, the backwashing water replenishing valve 20 is automatically closed;
fourthly, flexibly setting the starting time interval and the backwashing time of the backwashing mode according to the actual operation condition of the MBR membrane system for the kitchen biogas slurry;
when the chemical cleaning mode needs to be operated, the chemical cleaning mode is automatically controlled and started through the operation of a software program of the computer 100, and the specific steps of the chemical cleaning mode are as follows:
firstly, when a kitchen biogas slurry MBR membrane system is started to continuously run, and a backwashing mode is executed for 12 times (specifically, flexible setting can be carried out according to actual running conditions), the system automatically closes a water production pump 12 and a water production valve 15 corresponding to each group of MBR membrane modules 14 in sequence, and when the backwashing program is entered for 12 times, acid chemical cleaning is synchronously carried out;
and secondly, opening the water production valve 15 corresponding to the first group of MBR membrane modules 14, and starting a first feeding pump on the backwashing pump 42 and the hydrochloric acid storage tank 47 and a backwashing valve 48 corresponding to the first group of MBR membrane modules 14. It should be noted that: the first feeding pump on the hydrochloric acid medicine storage tank 47 is a hydrochloric acid first pump 53, and the second feeding pump on the hydrochloric acid medicine storage tank 47 is a hydrochloric acid second pump 54.
After 295 seconds, opening the water production valve 15 and the backwashing valve 48 corresponding to the second group of MBR membrane modules 14, and closing the water production valve 15 and the backwashing valve 48 corresponding to the first group of MBR membrane modules 14;
after 295 × n seconds, opening a water production valve 15 and a backwashing valve 48 corresponding to the nth group of MBR membrane modules 14, closing the water production valve 15 and the backwashing valve 48 corresponding to the nth-1 group of MBR membrane modules 14, ending after 295 × 1 s, closing the backwashing pump 42 and the hydrochloric acid first pump 53, closing the water production valve 15 and the backwashing valve 48 corresponding to the nth group of MBR membrane modules 14, ending the backwashing program, and automatically entering an operation mode (the opening and closing of each valve must be carried out after the previous operation is finished, and the opening and closing time delay of the pump and the valves is set according to the operation condition);
and thirdly, when the kitchen biogas slurry MBR membrane system is started up and continuously operates, and the backwashing mode is executed for 24 times (specifically, the backwashing mode can be flexibly set according to actual operation conditions), the system automatically closes the water production pump 12 and the water production valve 15 corresponding to each group of MBR membrane modules 14 in sequence, and when the kitchen biogas slurry MBR membrane system enters the backwashing program for 24 times, alkaline chemical cleaning is synchronously performed.
And fourthly, opening the water production valve 15 and the backwashing valve 48 corresponding to the first group of MBR membrane modules 14, wherein the first feeding pump on the sodium hydroxide medicine storage box 46 is a first sodium hydroxide pump 51, the second feeding pump on the sodium hydroxide medicine storage box 46 is a second sodium hydroxide pump 52, the first feeding pump on the sodium hypochlorite medicine storage box 45 is a first sodium hypochlorite pump 49, and the second feeding pump on the sodium hypochlorite medicine storage box 45 is a second sodium hypochlorite pump 50. Starting a backwashing pump 42, a sodium hydroxide pump 51 and a sodium hypochlorite pump 49, opening a water production valve 15 and a backwashing valve 48 corresponding to a second group of MBR membrane modules 14 after 295 seconds, closing the water production valve 15 and the backwashing valve 48 corresponding to a first group of MBR membrane modules 14, opening the water production valve 15 and the backwashing valve 48 corresponding to an nth group of MBR membrane modules 14 after 295 seconds, closing the water production valve 15 and the backwashing valve 48 corresponding to an n-1 group of MBR membrane modules 14, ending after 295 s, closing the backwashing pump 42, the sodium hypochlorite pump 49 and the sodium hydroxide pump 51, closing the water production valve 15 and the backwashing valve 48 corresponding to an nth group of MBR membrane modules 14, ending a backwashing program, and automatically entering an operation mode (the opening and closing of each valve must be carried out after the previous operation is finished, and the opening and closing time delay of the pump and the valve is set according to the operation condition);
and (6) flexibly setting the starting time interval and the chemical cleaning time of the chemical cleaning mode according to the actual operation condition of the kitchen biogas slurry MBR membrane system, manually adjusting and determining the adding amount of hydrochloric acid, sodium hydroxide and sodium hypochlorite according to the actual chemical cleaning, and alternately performing acidic chemical cleaning and alkaline chemical cleaning to ensure the chemical cleaning effect and maintain the normal operation of the membrane system.
Sixthly, when the backwashing water tank 41 does not reach the set starting liquid level, the chemical cleaning mode cannot be started to protect the backwashing pump 42, and when the backwashing water tank 41 is lower than the set liquid level in the chemical cleaning mode, the cleaning water replenishing valve 58 is automatically opened to replenish tap water, and when the set maximum liquid level is reached, the cleaning water replenishing valve 58 is automatically closed to ensure the chemical cleaning effect.
The backwashing mode is matched with the chemical cleaning mode to provide continuous pre-cleaning, and the addition of the sodium hypochlorite improves the cleaning effect on the MBR membrane module 14, so that the burden of shutdown cleaning is reduced.
When the shutdown cleaning mode needs to be operated, the shutdown cleaning mode is automatically controlled and started through the operation of a software program of the computer 100, and the specific steps of the shutdown cleaning mode are as follows:
when the kitchen biogas slurry MBR membrane system is started to continuously run, and the backwashing mode is executed for 1000 times (when the continuous operation lasts for about 3 months, the backwashing mode can be flexibly set according to actual running conditions), the system automatically closes the water production pump 12 and the water production valve 15 corresponding to each group of MBR membrane modules 14 in sequence, and then the system enters a shutdown cleaning program.
Secondly, opening the cleaning water replenishing valve 58, controlling the opening and closing of the cleaning water replenishing valve 58 by setting the liquid level through the second liquid level meter 56, and automatically closing the cleaning water replenishing valve 58 when the liquid level in the backwashing water tank 41 reaches a set liquid level value;
starting the second hydrochloric acid pump 54, and when the pH value in the backwashing water tank 41 reaches a set pH value of 2, automatically closing the second hydrochloric acid pump 54 to operate, and controlling the pH value in the backwashing water tank 41 to be 2;
opening a water production valve 15 and a backwashing valve 48 corresponding to the first group of MBR membrane modules 14, starting a backwashing pump 42, opening a water production valve 15 and a backwashing valve 48 corresponding to the second group of MBR membrane modules 14 after 295 seconds, closing the water production valve 15 and the backwashing valve 48 corresponding to the first group of MBR membrane modules 14, opening the water production valve 15 and the backwashing valve 48 corresponding to the nth group of MBR membrane modules 14 after 295 seconds, closing the water production valve 15 and the backwashing valve 48 corresponding to the nth-1 group of MBR membrane modules 14, closing 295 (n +1) s, then opening the water production valve 15 and the backwashing valve 48 corresponding to the second group of MBR membrane modules 14, closing the backwashing pump 42, closing the water production valve 15 and the backwashing valve 48 corresponding to the nth group of MBR membrane modules 14 after 1-time cleaning, opening a cleaning emptying valve 59, automatically closing the cleaning emptying valve 59 after the minimum MBR liquid level in the set backwashing water tank 41 is reached, entering an alkaline washing shutdown cleaning program;
the cleaning water replenishing valve 58 is opened, the liquid level is set by the second liquid level meter 56 to control the opening and closing of the cleaning water replenishing valve 58, and the cleaning water replenishing valve 58 is automatically closed when the liquid level in the backwashing water tank 41 reaches the set liquid level value;
sixthly, opening a sodium hydroxide secondary pump 52 and a sodium hypochlorite secondary pump 50, automatically closing the sodium hydroxide secondary pump 52 to operate when the PH value in the backwashing water tank 41 reaches a set PH value of 12, controlling the PH value in the backwashing water tank 41 to be 12.0, and flexibly setting the adding amount and the operating time of the sodium hypochlorite secondary pump 50 according to the actual cleaning effect;
the water production valve 15 and the backwashing valve 48 corresponding to the first group of MBR membrane module 14 are opened, the backwashing pump 42 is started, the water production valve 15 and the backwashing valve 48 corresponding to the second group of MBR membrane module 14 are opened after 295 seconds, the water production valve 15 and the backwashing valve 48 corresponding to the first group of MBR membrane module 14 are closed, the water production valve 15 and the backwashing valve 48 corresponding to the nth group of MBR membrane module 14 are opened after 2955 x n seconds, the water production valve 15 and the backwashing valve 48 corresponding to the nth-1 group of MBR membrane module 14 are opened after closing the water production valve 15 and the backwashing valve 48 corresponding to the nth-1 group of MBR membrane module 14, the water production valve 15 and the backwashing valve 48 corresponding to the nth group of MBR membrane module 14 are cleaned again for 1 time, the backwashing pump 42 is closed, the backwashing valve 48 corresponding to the nth group of MBR membrane module 14 is closed, the cleaning evacuation valve 59 is opened, the cleaning evacuation valve 59 is automatically closed after the minimum liquid level in the backwashing water tank 41 is reached, stopping the cleaning mode, and automatically entering the running mode (the opening and closing of each valve must be carried out after the previous operation is finished, and the opening and closing time delay of the pump and the valve is set according to the running condition);
and (8) flexibly setting the starting time interval and the cleaning time of the shutdown cleaning mode according to the actual operation condition of the kitchen biogas slurry MBR membrane system, and alternately performing acidic chemical cleaning and alkaline chemical cleaning to ensure the chemical cleaning effect and maintain the normal operation of the membrane system.
The control system automatically and intelligently controls the operation of the MBR membrane system through real-time acquisition and analysis of operation data of the MBR membrane system for kitchen biogas slurry, controls operation control parameters such as operation time, interval period and the like of a backwashing mode, a chemical cleaning mode and a shutdown cleaning mode, timely cleans the membrane treatment system, effectively recovers membrane flux, prolongs the service life of the membrane system, and effectively avoids manual operation errors and possible irreversible damage to the membrane module. By controlling the real-time monitoring of the system and controlling the alternate operation of various cleaning modes, the membrane system keeps higher water production flux for a long time, the energy consumption is reduced to a certain extent, and the operation cost is reduced.
In the description of the present invention, it is to be understood that the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implying any number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless specifically limited otherwise.
In the present invention, unless otherwise expressly stated or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally formed; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium; either as communication within the two elements or as an interactive relationship of the two elements. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.
In the present application, unless otherwise expressly stated or limited, a first feature may be "on" or "under" a second feature, and the first and second features may be in direct contact, or the first and second features may be in indirect contact via an intermediate. Also, a first feature "on," "above," and "over" a second feature may be directly or obliquely above the second feature, or simply mean that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the second feature, or may simply mean that the first feature is at a lower level than the second feature.
In the description herein, the description of the terms "one embodiment," "some embodiments," "an embodiment," "an example," "a specific example" or "some examples" or the like, means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.
While embodiments of the present invention have been shown and described, it is to be understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and that modifications, alterations, substitutions and variations may be made to the above embodiments by those of ordinary skill in the art without departing from the scope of the present invention.
Claims (10)
1. The utility model provides an intelligent control system for meal kitchen natural pond liquid MBR membrane system which characterized in that, intelligent control system includes: a filtration system, a cleaning system and a control system;
the filtering system comprises a membrane pool, a water production pump, a water production tank and a plurality of MBR membrane modules;
the MBR membrane modules are arranged in the membrane pool, the outlets of the MBR membrane modules are connected with the inlet of the water production tank through a water production pipeline, the water production pump is arranged on the water production pipeline, and a water production valve is arranged between the inlet of the water production pipeline and the outlet of each MBR membrane module;
the cleaning system comprises a backwashing water tank, a backwashing pump, a pipeline mixer and a plurality of medicine storage boxes;
the outlet of the backwashing water tank is connected with a plurality of backwashing branch pipes through a backwashing pipeline, the backwashing branch pipes are connected with the outlets of the MBR membrane assemblies in a one-to-one correspondence manner, backwashing valves are arranged on the backwashing branch pipes, the inlet of the backwashing water tank is connected with the inlet of the water production tank, the pipeline mixer and the backwashing pump are arranged on the backwashing pipeline, the first outlet of the medicine storage tank is connected with the pipeline mixer through a first feeding pump, and the second outlet of the medicine storage tank is connected with the inlet of the backwashing water tank through a second feeding pump;
the water producing pump, the backwashing pump, the water producing valve, the backwashing valve, the first adding pump and the second adding pump are in signal connection with the control system.
2. The intelligent control system for the kitchen biogas slurry MBR membrane system of claim 1, wherein the outlet of each water production valve is connected to the inlet of the water production pump through a water production branch pipe, and a water production pressure sensor is arranged on each water production branch pipe;
a water production turbidity meter, a water production flow meter and a water production outlet valve are sequentially arranged on the water production pipeline from the outlet of the water production pump to the inlet of the water production tank;
the water production pressure sensor, the water production turbidity meter, the water production flow meter and the water production water outlet valve are in signal connection with the control system.
3. The intelligent control system for the kitchen biogas slurry MBR membrane system of claim 2, wherein a backwashing water inlet pipeline and a backwashing water replenishing pipeline are arranged between the inlet of the water production tank and the inlet of the backwashing water tank;
the inlet of the backwashing water inlet pipeline is connected with the inlet of the water production tank, the outlet of the backwashing water inlet pipeline is connected with the inlet of the backwashing water tank, and a backwashing water inlet valve is arranged on the backwashing water inlet pipeline;
the inlet of the backwashing water supply pipeline is connected with the water production pipeline, the connection point of the backwashing water supply pipeline and the water production pipeline is positioned on the pipeline between the water production flowmeter and the water production outlet valve, the outlet of the backwashing water supply pipeline is connected with the inlet of the backwashing water tank, and the backwashing water supply pipeline is provided with a backwashing water supply valve;
and the backwashing water replenishing valve and the backwashing water inlet valve are in signal connection with the control system.
4. The intelligent control system for the kitchen biogas slurry MBR membrane system according to claim 1, wherein a first liquid level meter is arranged in the medicine storage box and used for detecting the liquid level in the medicine storage box;
the medicine storage boxes comprise a sodium hypochlorite medicine storage box, a sodium hydroxide medicine storage box and a hydrochloric acid medicine storage box;
the first liquid level meter is in signal connection with the control system.
5. The intelligent control system for the kitchen biogas slurry MBR membrane system of claim 1, wherein a backwashing filter is further arranged on the backwashing pipeline, the backwashing water tank, the backwashing pump, the pipeline mixer and the backwashing filter are sequentially connected through the backwashing pipeline, and inlets of the plurality of backwashing valves are connected with an outlet of the backwashing filter.
6. The intelligent control system for the kitchen biogas slurry MBR membrane system of claim 1, wherein a second liquid level meter and a PH meter are arranged in the backwash water tank, the second liquid level meter is used for detecting the liquid level in the backwash water tank, and the PH meter is used for detecting the pH value of the liquid in the backwash water tank;
a third liquid level meter is arranged in the water production tank, and a fourth liquid level meter is arranged in the membrane pool;
the second liquid level meter, the PH meter, the third liquid level meter and the fourth liquid level meter are all in signal connection with the control system.
7. The intelligent control system for the kitchen biogas slurry MBR membrane system of claim 1, wherein a cleaning water supplementing pipeline and a cleaning emptying pipeline are connected to the backwashing water tank;
an inlet of the cleaning water replenishing pipeline is connected with a tap water pipe network, an outlet of the cleaning water replenishing pipeline is connected with an inlet of the backwashing water tank, and a cleaning water replenishing valve is arranged on the cleaning water replenishing pipeline;
a water outlet is formed in the bottom of the backwashing water tank, an inlet of the cleaning emptying pipeline is connected with the water outlet, and a cleaning emptying valve is arranged on the cleaning emptying pipeline;
and the cleaning water supplementing valve and the cleaning emptying valve are in signal connection with the control system.
8. The intelligent control system for the MBR membrane system for the kitchen biogas slurry according to any one of claims 1-7, wherein the filtering system further comprises a fan, the fan is connected with the MBR membrane module through an aeration pipeline, and an air pressure sensor, an air valve and an air flow meter are arranged on the aeration pipeline;
the fan, the air pressure sensor, the air valve and the air flow meter are in signal connection with the control system.
9. The intelligent control system for the MBR membrane system for the kitchen biogas slurry according to any one of claims 1-7, wherein the filtering system further comprises a sewage discharge pipeline, a sludge return pipeline, a sludge discharge pipe, a sludge return tank and a sludge concentration tank;
a sewage discharge port is formed in the bottom of the membrane tank, the inlet of the sewage discharge pipeline is connected with the sewage discharge port, the inlets of the sludge return pipeline and the sludge discharge pipe are both connected with the outlet of the sewage discharge pipeline, the outlet of the sludge return pipeline is connected with the sludge return tank, and the outlet of the sludge discharge pipeline is connected with the sludge concentration tank;
a sludge pump is arranged on the sewage discharge pipeline, a sludge return valve is arranged on the sludge return pipeline, and a sludge discharge valve is arranged on the sludge discharge pipeline;
the sludge pump, the sludge return valve and the sludge discharge valve are in signal connection with the control system.
10. The intelligent control system for the kitchen biogas slurry MBR membrane system according to any one of claims 1-7, wherein the control system comprises a computer and a process controller, and the input end of the computer is in signal connection with the process controller;
the water production pump, the backwashing pump, the water production valve, the backwashing valve, the first feeding pump and the second feeding pump are all in signal connection with the process controller.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114920356A (en) * | 2022-06-10 | 2022-08-19 | 青岛双元水务有限公司 | Intelligent cleaning method for MBR (membrane bioreactor) |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114920356A (en) * | 2022-06-10 | 2022-08-19 | 青岛双元水务有限公司 | Intelligent cleaning method for MBR (membrane bioreactor) |
| CN114920356B (en) * | 2022-06-10 | 2023-06-16 | 青岛水务集团有限公司 | Intelligent cleaning method for MBR (Membrane bioreactor) |
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