CN110436608A - Aeration monitoring method and device for bed mud residual water treatment equipment - Google Patents
Aeration monitoring method and device for bed mud residual water treatment equipment Download PDFInfo
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- CN110436608A CN110436608A CN201910616865.3A CN201910616865A CN110436608A CN 110436608 A CN110436608 A CN 110436608A CN 201910616865 A CN201910616865 A CN 201910616865A CN 110436608 A CN110436608 A CN 110436608A
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
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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
- C02F7/00—Aeration of stretches of water
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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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
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/04—Oxidation reduction potential [ORP]
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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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)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The present invention is suitable for technical field of sewage, provide a kind of aeration monitoring method and device for bed mud residual water treatment equipment, this method comprises: passing through the concentration for obtaining organic pollutant in aerobic tank, then the concentration of organic pollutant is detected, when the concentration of organic pollutant is greater than the first concentration threshold or less than the second concentration threshold, adjust aeration rate and/or aeration time in the aerobic tank, until when the concentration of organic pollutant is in the range of second concentration threshold to first concentration threshold, water in aerobic tank is discharged, so as to effectively remove the ammonia nitrogen of remaining bed mud Yu Shuizhong, realize the aeration automatic adjustment of aerobic tank, reach energy saving purpose.
Description
Technical field
The invention belongs to technical field of sewage more particularly to a kind of aeration monitoring for bed mud residual water treatment equipment
Method and device.
Background technique
River environmental dredging is the novel industry to grow up in the past 30 years, is hydraulic engineering, environmental project and dredger
The engineering technology that journey is intersected.According to the experience of domestic and international waste water control, under conditions of water body external source pollutes to obtain control, it is necessary to
Endogenous pollution i.e. polluted bed mud is thoroughly removed, water ecosystem is rebuild, river regulation can be only achieved ideal effect, thus river
Road environmental dredging is generally considered one of the important measures that endogenous pollution is removed during water environment treatment.But it is adjoint
The implementation of environmental dredging engineering, a large amount of dredging residual water generate, often in the case where not being effectively addressed just arrange
Enter into neighbouring receiving water body.Due to a variety of dirts such as suspended matter, nitrogen, phosphorus and organic matters in dredging residual water containing high concentration
Object is contaminated, is directly discharged in receiving water body that serious ecological environmental pollution will be caused, it is therefore desirable to handle dredging residual water.
Existing Dredged bed mud residual water treatment mostly uses the mode of flocculating and purifying, but ineffective to ammonia nitrogen removal, is discharged into
New secondary pollution is brought after water body, and to ammonia nitrogen removal during, waste mass energy.
Summary of the invention
In view of this, the embodiment of the invention provides a kind of aeration monitoring methods and dress for bed mud residual water treatment equipment
It sets, it is ineffective to ammonia nitrogen removal in the prior art to solve, new secondary pollution is brought after being discharged into water body, and go to ammonia nitrogen
The problem of except in the process, mass energy is wasted.
The first aspect of the embodiment of the present invention provides a kind of aeration monitoring method for bed mud residual water treatment equipment, packet
It includes:
Obtain the concentration of organic pollutant in aerobic tank；
When the concentration of above-mentioned organic pollutant is greater than the first concentration threshold or less than the second concentration threshold, adjust above-mentioned
Aeration rate and/or aeration time in aerobic tank, above-mentioned first concentration threshold are greater than above-mentioned second concentration threshold；
When the concentration of above-mentioned organic pollutant is in the range of above-mentioned second concentration threshold to above-mentioned first concentration threshold,
Water in above-mentioned aerobic tank is discharged.
In one embodiment, above-mentioned aerobic tank includes at least one；
The concentration of organic pollutant in above-mentioned acquisition aerobic tank, comprising:
Obtain the concentration of organic pollutant in any N number of aerobic tank, above-mentioned N be more than or equal to 1, and less than or equal to M from
So number, above-mentioned M are aerobic tank sum.
In one embodiment, partition is respectively provided between adjacent aerobic tank, each partition is equipped with overflow port, the overflow of each partition
It is in successively to reduce each overflow port to be equipped with cofferdam in the side of the upstream of drainage flow that the height of mouth, which flows to direction along sewage,.
In one embodiment, in above-mentioned acquisition aerobic tank organic pollutant concentration, comprising:
Obtain the ammonia nitrogen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the nitrate concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the dissolved oxygen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the value of the oxidation-reduction potential ORP at the cofferdam position in aerobic tank.
In one embodiment, when the concentration of above-mentioned organic pollutant is greater than the first concentration threshold or less than the second concentration threshold
When value, aeration rate and/or aeration time in above-mentioned aerobic tank are adjusted, comprising:
When the concentration of above-mentioned organic pollutant is greater than the first concentration threshold, the exposure of aerator in above-mentioned aerobic tank is turned up
Gas velocity rate and/or aeration time；
When the concentration of above-mentioned organic pollutant is less than the second concentration threshold, the exposure of aerator in above-mentioned aerobic tank is turned down
Gas velocity rate and/or aeration time.
In one embodiment, above-mentioned aerator includes the multiple aeration coil pipes being respectively arranged in each aerobic tank, installation
In multiple aeration heads on aeration coil pipe and the air blower for being connected with each aeration coil pipe and being used to supply gas to each aeration coil pipe.
In one embodiment, above-mentioned multiple aeration heads are disposed as disc type aeration head, are in shower shape.
The second aspect of the embodiment of the present invention provides a kind of aeration monitoring device for bed mud residual water treatment equipment, packet
It includes:
Module is obtained, for obtaining the concentration of organic pollutant in aerobic tank；
Adjustment module is greater than the first concentration threshold for the concentration when above-mentioned organic pollutant or less than the second concentration threshold
When value, aeration rate and/or aeration time in above-mentioned aerobic tank are adjusted, above-mentioned first concentration threshold is greater than above-mentioned second concentration threshold
Value；
Processing module, for the concentration when above-mentioned organic pollutant in above-mentioned second concentration threshold to above-mentioned first concentration threshold
When in the range of value, water in above-mentioned aerobic tank is discharged.
The third aspect of the embodiment of the present invention provides a kind of terminal device, comprising: memory, processor and is stored in
In above-mentioned memory and the computer program that can be run on above-mentioned processor, when above-mentioned processor executes above-mentioned computer program
Realize such as the above-mentioned step of the above-mentioned aeration monitoring method for bed mud residual water treatment equipment.
The fourth aspect of the embodiment of the present invention provides a kind of computer readable storage medium, comprising: above-mentioned computer can
It reads storage medium and is stored with computer program, realization is such as above-mentioned when above-mentioned computer program is executed by processor is used for water more than bed mud
The above-mentioned step of the aeration monitoring method of processing equipment.
Existing beneficial effect is the embodiment of the present invention compared with prior art: by obtaining organic pollutant in aerobic tank
Concentration, then the concentration of organic pollutant is detected, when above-mentioned organic pollutant concentration be greater than the first concentration threshold
Or when less than the second concentration threshold, aeration rate and/or aeration time in above-mentioned aerobic tank are adjusted, until working as above-mentioned organic dirt
When contaminating the concentration of object in [the second concentration threshold, the first concentration threshold] range, water in above-mentioned aerobic tank is discharged, so as to
The ammonia nitrogen for effectively removing remaining bed mud Yu Shuizhong realizes the aeration automatic adjustment of aerobic tank, reaches energy saving purpose.
Detailed description of the invention
It to describe the technical solutions in the embodiments of the present invention more clearly, below will be to embodiment or description of the prior art
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only of the invention some
Embodiment for those of ordinary skill in the art without any creative labor, can also be according to these
Attached drawing obtains other attached drawings.
Fig. 1 is that the implementation process of the aeration monitoring method provided in an embodiment of the present invention for bed mud residual water treatment equipment is shown
It is intended to；
Fig. 2 is the front view of multi-stage biological contact-oxidation pool provided in an embodiment of the present invention；
Fig. 3 is the side view of multi-stage biological contact-oxidation pool provided in an embodiment of the present invention；
Fig. 4 is the exemplary diagram of the aeration monitoring device provided in an embodiment of the present invention for bed mud residual water treatment equipment；
Fig. 5 is the schematic diagram of terminal device provided in an embodiment of the present invention.
Specific embodiment
In being described below, for illustration and not for limitation, the tool of such as particular system structure, technology etc is proposed
Body details, to understand thoroughly the embodiment of the present invention.However, it will be clear to one skilled in the art that there is no these specific
The present invention also may be implemented in the other embodiments of details.In other situations, it omits to well-known system, device, electricity
The detailed description of road and method, in case unnecessary details interferes description of the invention.
In order to illustrate the technical solution of the present invention, the following is a description of specific embodiments.
Fig. 1 is a kind of realization stream of the aeration monitoring method for bed mud residual water treatment equipment provided in an embodiment of the present invention
Journey schematic diagram, details are as follows.
Step 101, the concentration of organic pollutant in aerobic tank is obtained.
Optionally, the remaining water being discharged from sludge handling factory, the remaining water after pretreatment pool enter multi-stage biological contact oxygen
Change pond, multi-stage biological contact-oxidation pool may include anaerobic pond and aerobic tank.Water body is after multistep treatment, the ammonia nitrogen of Yu Shuizhong
It can also be removed with total nitrogen, water outlet reaches five class of surface water, by multi-stage biological contact-oxidation pool treated remaining water by clear
After pond is stablized, it is discharged into sludge handling factory artificial swamp or irrigates land use for greening, water resource is made to be fully used.
Optionally, as shown in Fig. 2, in order to achieve the effect that preferably to remove ammonia nitrogen and total nitrogen, multi-stage biological catalytic oxidation
The quantity of anaerobic pond and aerobic tank all can be at least one in pond, for example, two, respectively anaerobic pond can be set in anaerobic pond
11 and anaerobic pond 12, aerobic tank three, respectively aerobic tank 21, aerobic tank 22 and aerobic tank 23 can be set.
As shown in Fig. 2, being equipped with partition 31 between two adjacent aerobic tanks, adjacent pond is separated by partition 31.
Partition 31 is arranged simply, convenient for the volume of save the cost and reduction multi-stage biological contact-oxidation pool.Each partition 31 is equipped with overflow
Mouth 32, it is in the ponds at different levels successively reduced, so from front to back that the height of the overflow port 32 of each partition 31, which flows to direction along sewage,
Liquid level gradually decreases, and the reaction time gradually decreases, and the reaction time for both having provided abundance for anaerobism section is also beneficial to aerobic section
Sewage is sufficiently and oxygen mix.
Optionally, the side of upstream of each overflow port 32 in drainage flow is equipped with cofferdam 33, and cofferdam 33 can prevent downstream
Backing up of sewage return upstream, avoid front and back pond from generating interference when handling sewage.Further, cofferdam 33 can also be sewage
Detection provides a test point, convenient for accurately detecting the result of sewage treatment in each pond.
Optionally, aerobic microbiological, including ammonia oxidation bacteria, nitrifier etc. are primarily present in aerobic tank, Yu Shui is by aerobic
The purpose of pond processing is the organic pollutant for removing Yu Shuizhong, and ammoniation is mainly organic nitrogen and ammoniacal nitrogen.Nitrogenous chemical combination
Under microbial action following reaction: aminating reaction and nitration reaction occurs in succession for object.Aminating reaction is that organonitrogen compound exists
Ammoniacal nitrogen is converted under ammonifiers effect.Nitration reaction is that ammoniacal nitrogen carries out nitration reaction under nitrifier effect, can be divided to two
Step, first is that nitrosification occurs under nitrococcus effect, ammoniacal nitrogen is converted into cultured water, and another is nitrification, nitre
Change bacterium and converts nitrate nitrogen for cultured water.It carries out needing oxygen when above-mentioned reflection in aerobic tank, therefore can be by aerobic
The concentration of organic pollutant judges whether aeration is enough in pond.
Optionally, the concentration for obtaining organic pollutant in aerobic tank may include: organic contamination in above-mentioned acquisition aerobic tank
The concentration of object, comprising: obtain the concentration of organic pollutant in any N number of aerobic tank, above-mentioned N is and to be less than or equal to more than or equal to 1
The natural number of M, above-mentioned M are aerobic tank sum.The concentration of organic pollutant in any one aerobic tank can be obtained, can also be obtained
The concentration of organic pollutant in any two or three aerobic tanks is taken, also the organic pollutant in available all aerobic tanks
Concentration.
Optionally, this step may include:
Obtain the ammonia nitrogen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the nitrate concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the dissolved oxygen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the oxidation-reduction potential (Oxidation-Reduction at the cofferdam position in aerobic tank
Potential, ORP) value.By the concentration of the organic pollutant at the cofferdam position in measurement aerobic tank, exposure can detecte
Whether gas is abundant.
Step 102, when the concentration of above-mentioned organic pollutant is greater than the first concentration threshold or less than the second concentration threshold,
Aeration rate and/or aeration time in above-mentioned aerobic tank are adjusted, above-mentioned first concentration threshold is greater than above-mentioned second concentration threshold.
Optionally, after the concentration for obtaining organic pollutant, so that it may be aerated certainly according to the concentration of organic pollutant
It is dynamic to adjust, so that treated that water reaches standard by aerobic tank.
Optionally, this step may include: when the concentration of above-mentioned organic pollutant is greater than the first concentration threshold, in height-regulating
State the aeration rate and/or aeration time of aerator in aerobic tank.I.e. when the concentration of above-mentioned organic pollutant is dense greater than first
When spending threshold value, illustrate to be aerated in aerobic tank insufficient, it is therefore desirable to increase the oxygen content in aerobic tank, therefore be turned up above-mentioned aerobic
Aeration rate and/or aeration time in pond.Optionally, the operating rate of air blower can be turned up or the operation of air blower is turned up
Time.
Optionally, the first concentration threshold and the second concentration threshold can be set according to actual needs, in the application
In do not limit the method for determination and value range of the first concentration threshold and the second concentration threshold, need to only meet above-mentioned first concentration
Threshold value is greater than above-mentioned second concentration threshold.
Optionally, it when the concentration of above-mentioned organic pollutant is less than the second concentration threshold, turns down and is aerated in above-mentioned aerobic tank
The aeration rate and/or aeration time of device.I.e. when the concentration of above-mentioned organic pollutant is less than the second concentration threshold, illustrate
Be aerated in oxygen pond excessive, it is therefore desirable to reduce the oxygen content in aerobic tank, therefore turn down in above-mentioned aerobic tank aeration rate and/
Or aeration time.Optionally, the operating rate of air blower can be turned down or turn down the runing time of air blower, had until above-mentioned
The process of aeration automatic adjustment terminates when the concentration of machine pollutant is in [the second concentration threshold, the first concentration threshold] range.
Optionally, as shown in Figures 2 and 3, above-mentioned aerator is set to the bottom of anaerobic pond and aerobic tank, including respectively
Multiple aeration coil pipes 41 in each aerobic tank, the multiple aeration heads 42 being installed on aeration coil pipe 41 and with each aeration
Coil pipe 41 is connected and the air blower 43 for supplying gas to each aeration coil pipe 41.
Above-mentioned multiple aeration heads 42 are disposed as disc type aeration head, are in shower shape.Disc type aeration head will be for that will be aerated coil pipe
Interior air-flow disperses to send out.Disc type aeration head can disperse gas in aeration, prevent from hanging over microbial film in pond from filling out
It is detached from material, aeration coil pipe 41 can provide enough aeration quantity for each pond.
Step 103, when the concentration of above-mentioned organic pollutant is in above-mentioned second concentration threshold to above-mentioned first concentration threshold
When in range, water in above-mentioned aerobic tank is discharged.
Optionally, when the concentration of above-mentioned organic pollutant is in above-mentioned second concentration threshold to the model of above-mentioned first concentration threshold
When enclosing interior, illustrate that the concentration of the organic pollutant in aerobic tank meets the requirements, the water in aerobic tank can be discharged at this time, discharge
Water is discharged into sludge handling factory artificial swamp or irrigates land use for greening after clear water reserviors are stablized, or water is discharged into it is next good
In oxygen pond.
The above-mentioned aeration monitoring method for bed mud residual water treatment equipment, by obtain aerobic tank in organic pollutant it is dense
Degree, then the concentration of organic pollutant is detected, when above-mentioned organic pollutant concentration be greater than the first concentration threshold or
When less than the second concentration threshold, aeration rate and/or aeration time in above-mentioned aerobic tank are adjusted, until working as above-mentioned organic pollutant
Concentration in the range of above-mentioned second concentration threshold to above-mentioned first concentration threshold when, water in above-mentioned aerobic tank is discharged, from
And the ammonia nitrogen of remaining bed mud Yu Shuizhong can be effectively removed, it realizes the aeration automatic adjustment of aerobic tank, reaches energy saving purpose.
It should be understood that the size of the serial number of each step is not meant that the order of the execution order in above-described embodiment, each process
Execution sequence should be determined by its function and internal logic, the implementation process without coping with the embodiment of the present invention constitutes any limit
It is fixed.
The aeration monitoring method for bed mud residual water treatment equipment above-mentioned corresponding to foregoing embodiments, Fig. 4 show this
The exemplary diagram for the aeration monitoring device for bed mud residual water treatment equipment that inventive embodiments provide.As shown in Fig. 2, the device can
To include: to obtain module 401, adjustment module 402 and processing module 403.
Module 401 is obtained, for obtaining the concentration of organic pollutant in aerobic tank；
Adjustment module 402, the concentration for working as above-mentioned organic pollutant are greater than the first concentration threshold or dense less than second
When spending threshold value, aeration rate and/or aeration time in above-mentioned aerobic tank are adjusted, it is dense that above-mentioned first concentration threshold is greater than above-mentioned second
Spend threshold value；
Processing module 403, for the concentration when above-mentioned organic pollutant in above-mentioned second concentration threshold to above-mentioned first dense
When in the range of degree threshold value, water in above-mentioned aerobic tank is discharged.
Optionally, above-mentioned aerobic tank includes at least one；Above-mentioned acquisition module 401 can be used for obtaining any N number of aerobic
The concentration of organic pollutant in pond, above-mentioned N are the natural number more than or equal to 1, and less than or equal to M, and above-mentioned M is aerobic tank sum.
Optionally, partition is respectively provided between adjacent aerobic tank, each partition is equipped with overflow port, the height of the overflow port of each partition
It is in successively to reduce each overflow port to be equipped with cofferdam in the side of the upstream of drainage flow that degree, which flows to direction along sewage,.
Optionally, above-mentioned acquisition module 401 can be used for obtaining the ammonia nitrogen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the nitrate concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the dissolved oxygen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the value of the oxidation-reduction potential ORP at the cofferdam position in aerobic tank.
Optionally, above-mentioned adjustment module 402 can be used for being greater than the first concentration threshold when the concentration of above-mentioned organic pollutant
When, the aeration rate and/or aeration time of aerator in above-mentioned aerobic tank is turned up；And the concentration when above-mentioned organic pollutant
When less than the second concentration threshold, the aeration rate and/or aeration time of aerator in above-mentioned aerobic tank are turned down.
When the concentration of above-mentioned organic pollutant is greater than the first concentration threshold, illustrate to be aerated deficiency in aerobic tank, therefore need
Increase the oxygen content in aerobic tank, therefore aeration rate and/or aeration time in above-mentioned aerobic tank is turned up.Optionally,
One concentration threshold and the second concentration threshold can be set according to actual needs, not limit the first concentration threshold in this application
It is dense greater than above-mentioned second need to only to meet above-mentioned first concentration threshold for the method for determination and value range of value and the second concentration threshold
Spend threshold value.
When the concentration of above-mentioned organic pollutant is less than the second concentration threshold, illustrate to be aerated excessively in aerobic tank, therefore need
The oxygen content in aerobic tank is reduced, therefore turns down aeration rate and/or aeration time in above-mentioned aerobic tank.Optionally, may be used
To turn down the operating rate of air blower or turn down the runing time of air blower, until the concentration when above-mentioned organic pollutant is upper
Processing module 403 when stating in the range of the second concentration threshold to above-mentioned first concentration threshold, water in above-mentioned aerobic tank is discharged.
The above-mentioned aeration monitoring device for bed mud residual water treatment equipment obtains organic dirt in aerobic tank by obtaining module
The concentration for contaminating object, then detects the concentration of organic pollutant, when the concentration of above-mentioned organic pollutant is greater than the first concentration
Threshold value or when less than the second concentration threshold, adjustment module adjusts aeration rate and/or aeration time in above-mentioned aerobic tank, until
It, will be above-mentioned good when the concentration of above-mentioned organic pollutant is in the range of above-mentioned second concentration threshold to above-mentioned first concentration threshold
Water is discharged in oxygen pond, so as to effectively remove the ammonia nitrogen of remaining bed mud Yu Shuizhong, realizes the aeration automatic adjustment of aerobic tank, reaches
Energy saving purpose.
Fig. 5 is the schematic diagram for the terminal device that one embodiment of the invention provides.As shown in figure 5, the terminal of the embodiment is set
Standby 500 include: processor 501, memory 502 and are stored in above-mentioned memory 502 and can transport on above-mentioned processor 501
Capable computer program 505, such as the aeration monitoring programme for bed mud residual water treatment equipment.On above-mentioned processor 501 executes
The step in the above-mentioned aeration monitoring method embodiment for bed mud residual water treatment equipment, example are realized when stating computer program 505
For step 101 as shown in Figure 1 to 103, above-mentioned processor 501 realizes that above-mentioned each device is real when executing above-mentioned computer program 505
The function of each module in example is applied, such as the function of module 401 to 403 shown in Fig. 4.
Illustratively, above-mentioned computer program 505 can be divided into one or more program modules, said one or
Multiple program modules are stored in above-mentioned memory 502, and are executed by above-mentioned processor 501, to complete the present invention.Above-mentioned one
A or multiple program modules can be the series of computation machine program instruction section that can complete specific function, and the instruction segment is for retouching
Above-mentioned computer program 505 is stated in above-mentioned aeration monitoring device or terminal device 500 for bed mud residual water treatment equipment
Implementation procedure.For example, above-mentioned computer program 505, which can be divided into, obtains module 401, adjustment module 402 and processing mould
Block 403, each module concrete function is as shown in figure 4, this is no longer going to repeat them.
Above-mentioned terminal device 500 can be the calculating such as desktop PC, notebook, palm PC and cloud server and set
It is standby.Above-mentioned terminal device may include, but be not limited only to, processor 501, memory 502.It will be understood by those skilled in the art that
Fig. 5 is only the example of terminal device 500, does not constitute the restriction to terminal device 500, may include more or more than illustrating
Few component perhaps combines certain components or different components, such as above-mentioned terminal device can also be set including input and output
Standby, network access equipment, bus etc..
Alleged processor 501 can be central processing unit (Central Processing Unit, CPU), can also be
Other general processors, digital signal processor (Digital Signal Processor, DSP), specific integrated circuit
(Application Specific Integrated Circuit, ASIC), ready-made programmable gate array (Field-
Programmable Gate Array, FPGA) either other programmable logic device, discrete gate or transistor logic,
Discrete hardware components etc..General processor can be microprocessor or the processor is also possible to any conventional processor
Deng.
Above-mentioned memory 502 can be the internal storage unit of above-mentioned terminal device 500, such as terminal device 500 is hard
Disk or memory.Above-mentioned memory 502 is also possible to the External memory equipment of above-mentioned terminal device 500, such as above-mentioned terminal device
The plug-in type hard disk being equipped on 500, intelligent memory card (Smart Media Card, SMC), secure digital (Secure
Digital, SD) card, flash card (Flash Card) etc..Further, above-mentioned memory 502 can also both include above-mentioned terminal
The internal storage unit of equipment 500 also includes External memory equipment.Above-mentioned memory 502 for store above-mentioned computer program with
And other programs and data needed for above-mentioned terminal device 500.Above-mentioned memory 502 can be also used for temporarily storing defeated
Out or the data that will export.
It is apparent to those skilled in the art that for convenience of description and succinctly, only with above-mentioned each function
Can unit, module division progress for example, in practical application, can according to need and by above-mentioned function distribution by different
Functional unit, module are completed, i.e., the internal structure of above-mentioned apparatus is divided into different functional unit or module, more than completing
The all or part of function of description.Each functional unit in embodiment, module can integrate in one processing unit, can also
To be that each unit physically exists alone, can also be integrated in one unit with two or more units, it is above-mentioned integrated
Unit both can take the form of hardware realization, can also realize in the form of software functional units.In addition, each function list
Member, the specific name of module are also only for convenience of distinguishing each other, the protection scope being not intended to limit this application.Above system
The specific work process of middle unit, module, can refer to corresponding processes in the foregoing method embodiment, and details are not described herein.
In the above-described embodiments, it all emphasizes particularly on different fields to the description of each embodiment, is not described in detail or remembers in some embodiment
The part of load may refer to the associated description of other embodiments.
Those of ordinary skill in the art may be aware that list described in conjunction with the examples disclosed in the embodiments of the present disclosure
Member and algorithm steps can be realized with the combination of electronic hardware or computer software and electronic hardware.These functions are actually
It is implemented in hardware or software, the specific application and design constraint depending on technical solution.Professional technician
Each specific application can be used different methods to achieve the described function, but this realization is it is not considered that exceed
The scope of the present invention.
In embodiment provided by the present invention, it should be understood that disclosed device/terminal device and method, it can be with
It realizes by another way.For example, device described above/terminal device embodiment is only schematical, for example, on
The division of module or unit is stated, only a kind of logical function partition, there may be another division manner in actual implementation, such as
Multiple units or components can be combined or can be integrated into another system, or some features can be ignored or not executed.Separately
A bit, shown or discussed mutual coupling or direct-coupling or communication connection can be through some interfaces, device
Or the INDIRECT COUPLING or communication connection of unit, it can be electrical property, mechanical or other forms.
Above-mentioned unit as illustrated by the separation member may or may not be physically separated, aobvious as unit
The component shown may or may not be physical unit, it can and it is in one place, or may be distributed over multiple
In network unit.It can select some or all of unit therein according to the actual needs to realize the mesh of this embodiment scheme
's.
It, can also be in addition, the functional units in various embodiments of the present invention may be integrated into one processing unit
It is that each unit physically exists alone, can also be integrated in one unit with two or more units.Above-mentioned integrated list
Member both can take the form of hardware realization, can also realize in the form of software functional units.
If above-mentioned integrated module/unit be realized in the form of SFU software functional unit and as independent product sale or
In use, can store in a computer readable storage medium.Based on this understanding, the present invention realizes above-mentioned implementation
All or part of the process in example method, can also instruct relevant hardware to complete, above-mentioned meter by computer program
Calculation machine program can be stored in a computer readable storage medium, the computer program when being executed by processor, it can be achieved that on
The step of stating each embodiment of the method.Wherein, above-mentioned computer program includes computer program code, above-mentioned computer program
Code can be source code form, object identification code form, executable file or certain intermediate forms etc..Above-mentioned computer-readable Jie
Matter may include: can carry above-mentioned computer program code any entity or device, recording medium, USB flash disk, mobile hard disk,
Magnetic disk, CD, computer storage, read-only memory (ROM, Read-Only Memory), random access memory (RAM,
Random Access Memory), electric carrier signal, telecommunication signal and software distribution medium etc..It should be noted that above-mentioned
The content that computer-readable medium includes can carry out increasing appropriate according to the requirement made laws in jurisdiction with patent practice
Subtract, such as does not include electric carrier signal and electricity according to legislation and patent practice, computer-readable medium in certain jurisdictions
Believe signal.
The above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations；Although with reference to the foregoing embodiments
Invention is explained in detail, those skilled in the art should understand that: it still can be to aforementioned each implementation
Technical solution documented by example is modified or equivalent replacement of some of the technical features；And these modification or
Replacement, the spirit and scope for technical solution of various embodiments of the present invention that it does not separate the essence of the corresponding technical solution should all include
Within protection scope of the present invention.
Claims (10)
1. a kind of aeration monitoring method for bed mud residual water treatment equipment characterized by comprising
Obtain the concentration of organic pollutant in aerobic tank；
When the concentration of the organic pollutant is greater than the first concentration threshold or less than the second concentration threshold, adjust described aerobic
Aeration rate and/or aeration time in pond, first concentration threshold are greater than second concentration threshold；
When the concentration of the organic pollutant is in the range of second concentration threshold to first concentration threshold, by institute
Water in aerobic tank is stated to be discharged.
2. being used for the aeration monitoring method of bed mud residual water treatment equipment as described in claim 1, which is characterized in that described aerobic
Pond includes at least one；
The concentration of organic pollutant in the acquisition aerobic tank, comprising:
The concentration of organic pollutant in any N number of aerobic tank is obtained, the N is the natural number more than or equal to 1, and less than or equal to M,
The M is aerobic tank sum.
3. being used for the aeration monitoring method of bed mud residual water treatment equipment as claimed in claim 2, which is characterized in that adjacent aerobic
Partition is respectively provided between pond, each partition is equipped with overflow port, and the height of the overflow port of each partition flows to direction in successively along sewage
It reduces each overflow port and is equipped with cofferdam in the side of the upstream of drainage flow.
4. being used for the aeration monitoring method of bed mud residual water treatment equipment as claimed in claim 3, which is characterized in that the acquisition
The concentration of organic pollutant in aerobic tank, comprising:
Obtain the ammonia nitrogen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the nitrate concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the dissolved oxygen concentration at the cofferdam position in aerobic tank；
Alternatively, obtaining the value of the oxidation-reduction potential ORP at the cofferdam position in aerobic tank.
5. such as the aeration monitoring method of any of claims 1-4 for bed mud residual water treatment equipment, feature exists
In, it is described when the concentration of the organic pollutant is greater than the first concentration threshold or less than the second concentration threshold, described in adjusting
Aeration rate and/or aeration time in aerobic tank, comprising:
When the concentration of the organic pollutant is greater than the first concentration threshold, the aeration speed of aerator in the aerobic tank is turned up
Rate and/or aeration time；
When the concentration of the organic pollutant is less than the second concentration threshold, the aeration speed of aerator in the aerobic tank is turned down
Rate and/or aeration time.
6. being used for the aeration monitoring method of bed mud residual water treatment equipment as claimed in claim 5, which is characterized in that the aeration
Device include the multiple aeration coil pipes being respectively arranged in each aerobic tank, be installed on aeration coil pipe on multiple aeration heads and with
Each aeration coil pipe is connected and the air blower for supplying gas to each aeration coil pipe.
7. being used for the aeration monitoring method of bed mud residual water treatment equipment as claimed in claim 5, which is characterized in that the multiple
Aeration head is disposed as disc type aeration head, is in shower shape.
8. a kind of aeration monitoring device for bed mud residual water treatment equipment characterized by comprising
Module is obtained, for obtaining the concentration of organic pollutant in aerobic tank；
Adjustment module is greater than the first concentration threshold for the concentration when the organic pollutant or less than the second concentration threshold
When, aeration rate and/or aeration time in the aerobic tank are adjusted, first concentration threshold is greater than the second concentration threshold
Value；
Processing module, for the concentration when the organic pollutant in second concentration threshold to first concentration threshold
When in range, water in the aerobic tank is discharged.
9. a kind of terminal device, including memory, processor and storage are in the memory and can be on the processor
The computer program of operation, which is characterized in that the processor realizes such as claim 1 to 7 when executing the computer program
The step of any one the method.
10. a kind of computer readable storage medium, the computer-readable recording medium storage has computer program, and feature exists
In when the computer program is executed by processor the step of any one of such as claim 1 to 7 of realization the method.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115196763A (en) * | 2021-04-13 | 2022-10-18 | 宜维龙环境科技(苏州)有限公司 | Underwater jet aeration device, control method thereof, terminal and storage medium |
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Address after: 518000, Guangdong, Baoan District, Xin'an Xin'an Street 1003 Shenzhen Road, No. six financial port C block Applicant after: China Power Construction Ecological Environment Group Co.,Ltd. Address before: 518000, Guangdong, Baoan District, Xin'an Xin'an Street 1003 Shenzhen Road, No. six financial port C block Applicant before: POWERCHINA WATER ENVIRONMENT GOVERANCE |
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