CN114477409A

CN114477409A - Data processing method suitable for stirrer system for industrial wastewater treatment

Info

Publication number: CN114477409A
Application number: CN202210308735.5A
Authority: CN
Inventors: 张益昌
Original assignee: Nanjing Aoboer Environmental Protection Equipment Co ltd
Current assignee: Nanjing Aoboer Environmental Protection Equipment Co ltd
Priority date: 2022-03-28
Filing date: 2022-03-28
Publication date: 2022-05-13
Anticipated expiration: 2042-03-28
Also published as: CN114477409B

Abstract

The invention provides a data processing method applicable to a stirrer system for industrial wastewater treatment, which comprises the following steps: acquiring first PH information and first volume information of first liquid to be treated and second PH information and second volume information of second liquid to be treated to generate first neutralization information and second neutralization information; acquiring first temperature information and first suspended matter information at a neutralization area; comparing the first temperature information with the reference temperature information, and then performing power weighting processing to generate first temperature power information; comparing the first flocculating agent information with the reference flocculating information, adjusting and weighting to generate first adjusting information, and comparing the first temperature information with the reference temperature information, adjusting and weighting to generate second adjusting information; and adjusting the first reference stirring power to obtain first adjusted stirring power, and controlling the stirrer system for industrial wastewater treatment according to the first adjusted stirring power, the first flocculating agent information and the first temperature power information.

Description

Data processing method suitable for stirrer system for industrial wastewater treatment

Technical Field

The invention relates to the technical field of data processing and motor control, in particular to a data processing method applicable to a stirrer system for industrial wastewater treatment.

Background

Industrial waste water (industrial water), including industrial waste water, industrial sewage and cooling water, refers to waste water and waste liquid produced in industrial production, which contains industrial production materials, intermediates, by-products and pollutants produced in the production process, which are lost along with water.

The industrial wastewater has various types and complex components. For example, the waste water from electrolytic salt industry contains mercury, the waste water from heavy metal smelting industry contains various metals such as lead and cadmium, the waste water from electroplating industry contains various heavy metals such as cyanide and chromium, the waste water from petroleum refining industry contains phenol, and the waste water from pesticide manufacturing industry contains various pesticides. Because industrial wastewater contains various toxic substances and pollutes the environment, the environment is harmful to human health, so that the industrial wastewater is developed to be comprehensively utilized and turn the harmful into the beneficial, and can be discharged after being treated by adopting corresponding purification measures according to the components and the concentration of pollutants in the wastewater.

One characteristic of industrial waste water is that the quality and quantity of water vary greatly depending on the production process and the mode of production. Even in the same production process, the water quality in the production process can be greatly changed, for example, in the steelmaking of a top-blown oxygen converter, the pH value of the wastewater can be between 4 and 13 and the suspended matters can be changed between 250 and 25000 mg/L in different smelting stages of the same steel. Therefore, different waste water may be neutralized, so that during waste water treatment, various waste water can be neutralized firstly, then the liquid after neutralization treatment can be neutralized uniformly, and during the neutralization treatment of various waste water, the neutralization speed of the waste water is in direct proportion to the treatment efficiency of the whole water body. In the neutralization treatment of the water body, a plurality of factors are influenced, such as the volume of the neutralization liquid, the specific gravity of suspended matters and the temperature during the neutralization, and the prior art cannot perform corresponding data acquisition treatment according to the properties of the liquid during the neutralization, so that the industrial wastewater treatment efficiency is low.

Disclosure of Invention

The embodiment of the invention provides a data processing method suitable for a stirrer system for industrial wastewater treatment, which can be used for acquiring and processing various data during industrial wastewater treatment and improving the industrial wastewater treatment efficiency.

In a first aspect of embodiments of the present invention, a data processing method for a mixer system for industrial wastewater treatment is provided, including:

acquiring first PH information and first volume information of first liquid to be treated, second PH information and second volume information of second liquid to be treated, and generating corresponding first neutralization information and second neutralization information based on the neutralization volume information;

controlling partial liquid in the first liquid to be treated and the second liquid to be treated to flow into a neutralization area according to the first neutralization information and the second neutralization information, and acquiring first temperature information and first suspended matter information at the neutralization area;

generating first flocculant information according to the first suspended matter information, comparing the first temperature information with reference temperature information, and performing power weighting processing to generate first temperature power information;

comparing the first flocculating agent information with reference flocculating information, adjusting and weighting to generate first adjusting information, and comparing the first temperature information with the reference temperature information, adjusting and weighting to generate second adjusting information;

and adjusting first reference stirring power according to the first adjustment information and the second adjustment information to obtain first adjustment stirring power, and controlling the stirrer system for industrial wastewater treatment according to the first adjustment stirring power, the first flocculating agent information and the first temperature power information.

Optionally, in a possible implementation manner of the first aspect, in the step of acquiring first PH information and first volume information of the first liquid to be processed, and generating corresponding first neutralization information and second neutralization information based on the neutralization volume information, second PH information and second volume information of the second liquid to be processed, the step specifically includes:

acquiring PH value proportion information of the first liquid to be treated and the second liquid to be treated according to the first PH information and the second PH information;

obtaining first initial information and second initial information according to the PH value proportion information and the neutralization volume information;

and if the first initial information and the second initial information are respectively smaller than the first volume information and the second volume information, taking values corresponding to the first initial information and the second initial information as first neutralization information and second neutralization information so as to enable the mixer system to be fully loaded and neutralized.

Optionally, in a possible implementation manner of the first aspect, in the step of obtaining the first initial information and the second initial information according to the PH ratio information and the neutralization volume information, the method specifically includes:

comparing the first PH information with standard PH information to obtain a first PH difference value, and comparing the second PH information with the standard PH information to obtain a second PH difference value;

obtaining PH value proportion information according to the first PH value and the second PH value, and obtaining first initial information and second initial information according to the PH value proportion information and the volume information;

calculating the numerical values respectively corresponding to the first initial information and the second initial information by the following formula,

wherein the content of the first and second substances,

is a numerical value corresponding to the first initial information,

is a weight of the first PH, and is,

is a numerical value of the first PH information,

is a weight of the second PH, and,

is a value of the second PH information,

in order to neutralize the value of the volume information,

the value is corresponding to the second initial information.

Optionally, in a possible implementation manner of the first aspect, if the first initial information is greater than the first volume information, the first volume information is used as first neutralization information, and second neutralization information is determined according to the first volume information;

obtaining second neutralization information according to the PH value proportion information and the first volume information so as to enable the stirrer system to be neutralized in a half-load mode;

if the second initial information is larger than the second volume information, taking the second volume information as second neutralization information, and determining first neutralization information according to the second volume information;

obtaining first neutralization information according to the PH value proportion information and the second volume information so as to enable the stirrer system to be neutralized in half load;

the second neutralization information and the first neutralization information are calculated by the following formulas,

wherein the content of the first and second substances,

is the first volume information of the first volume information,

in order to be the second volume information,

in order to be able to neutralize the information for the second time,

in order to be the first neutralizing information,

in order to be the second neutralization weight,

is the first neutralization rightAnd (4) heavy.

Optionally, in a possible implementation manner of the first aspect, the method further includes:

acquiring information of full-load neutralization and half-load neutralization of a stirrer system within a preset time period to obtain a neutralization scene table;

acquiring first to-be-treated liquid and second to-be-treated liquid which flow in through full-load neutralization and half-load neutralization of a stirrer system in a neutralization scene table to obtain first self-neutralization total volume information and second self-neutralization total volume information;

acquiring first treatment total volume information of a first liquid to be treated flowing into the treatment tank and second treatment total volume information of a second liquid to be treated flowing into the treatment tank within a preset time period;

obtaining unprocessed gross volume information according to the first self-neutralizing gross volume information, the second self-neutralizing gross volume information, the first processed gross volume information and the second processed gross volume information;

and obtaining neutralization demand information according to the unprocessed total volume information.

Optionally, in a possible implementation manner of the first aspect, in the step of obtaining the unprocessed total volume information according to the first self-neutralization total volume information, the second self-neutralization total volume information, the first processed total volume information, and the second processed total volume information, the method specifically includes:

obtaining a first unprocessed sub-volume from a difference between the first self-neutralizing total volume information and first processed total volume information;

obtaining a second untreated sub-volume according to the difference between the second self-neutralizing total volume information and second treatment total volume information;

obtaining a first unprocessed sub-demand and a second unprocessed sub-demand from the first unprocessed sub-volume and a second unprocessed sub-volume, the neutralization demand information including the first unprocessed sub-demand and the second unprocessed sub-demand.

determining a first neutralization number of full-load neutralization of the blender system and a second neutralization number of half-load neutralization of the blender system in a neutralization scene table;

generating a neutralization image corresponding to the scene table according to the first unprocessed sub-requirement, the second unprocessed sub-requirement, the first neutralization frequency and the second neutralization frequency;

the neutralization image is calculated by the following formula,

wherein the content of the first and second substances,

for neutralizing the value corresponding to the image,

the weight of the first image is used as the weight of the first image,

for inflow within a predetermined period of time

A volume information value of the first liquid to be treated,

for the upper limit value of the inflow of the first liquid to be treated,

for full-load neutralization of the blender system or inflow during half-load neutralization of the blender system

The first liquid to be treated is introduced into the treatment chamber,

the upper limit of the first fluid to be treated flowing into the full-load neutralization or half-load of the blender system,

for inflow within a predetermined period of time

A volume information value of the second liquid to be treated,

for the upper limit value of the inflow of the second liquid to be treated,

A second liquid to be treated,

the upper limit of the second fluid to be treated flowing into the full-load neutralization or half-load of the blender system,

the first image constant is constant and the second image constant is constant,

the second picture weight, the first number of neutralization,

as the number of times of the second neutralization,

is a second image constant;

acquiring neutralization images of a plurality of industrial wastewater treatment stirrer systems, and sequencing the neutralization images according to descending sequence to obtain an image sequence;

and carrying out operation reminding on an administrator according to the portrait sequence.

Optionally, in a possible implementation manner of the first aspect, the step of performing adjustment and weighting after comparing the first flocculant information with the reference flocculation information to generate first adjustment information, and performing adjustment and weighting after comparing the first temperature information with the reference temperature information to generate second adjustment information specifically includes:

comparing the first flocculating agent information with reference flocculation information to obtain first flocculation difference information, and performing weighting processing on the first flocculation difference information to obtain first adjustment information;

and comparing the first temperature information with reference temperature information to obtain first temperature difference information, and weighting the first temperature difference information to obtain second adjustment information.

Optionally, in a possible implementation manner of the first aspect, in the step of adjusting the first reference stirring power according to the first adjustment information and the second adjustment information to obtain a first adjusted stirring power, the step specifically includes:

the adjusted first adjusted stirring power is calculated by the following formula,

wherein the content of the first and second substances,

to calculate the adjusted first adjusted stirring power,

as the first adjustment information, it is possible to adjust,

in order to be the second adjustment information,

is a reference constant value that is a function of,

is the first reference stirring power and is,

in order to adjust the weight for the first time,

as information on the first flocculating agent, it is,

as information on the second flocculating agent, the flocculating agent,

is a first normalized value of the first normalized value,

in order to adjust the weight for the second time,

as the information on the first temperature, it is,

as the information on the reference temperature, there is,

is the second normalized value.

Optionally, in a possible implementation manner of the first aspect, after the step of controlling the mixer system for industrial wastewater treatment according to the first adjusted mixing power, the first flocculant information, and the first temperature power information, the method specifically includes:

monitoring the use behavior of an administrator, and if the administrator is judged to adjust the first flocculant information and/or the first temperature power information, obtaining adjusted first adjustment information and/or second adjustment information according to the adjusted first flocculant information and/or first temperature power information;

adjusting the first adjusting stirring power for the second time according to the adjusted first adjusting information and/or second adjusting information to obtain adjusted second adjusting stirring power;

if the manager is judged to adjust any one of the first adjustment stirring power and/or the second adjustment stirring power, obtaining a third adjusted stirring power after adjustment;

adjusting the first reference stirring power according to the difference value of the first adjustment stirring power and/or the second adjustment stirring power and the third adjustment stirring power to obtain second reference stirring power;

the adjusted second reference stirring power is obtained by,

wherein the content of the first and second substances,

for the second adjusted stirring power after the adjustment,

for the third adjusted stirring power after adjustment,

is the second reference stirring power and is,

in order to adjust the coefficient in the forward direction,

the coefficients are adjusted in reverse.

In a second aspect of the embodiments of the present invention, a storage medium is provided, in which a computer program is stored, which, when being executed by a processor, is adapted to carry out the method according to the first aspect of the present invention and various possible designs of the first aspect of the present invention.

The invention provides a data processing method suitable for a stirrer system for industrial wastewater treatment. The method can be used for neutralizing the wastewater, and can obtain first neutralization information and second neutralization information according to the first PH information, the first volume information, the second PH information and the second volume information when the neutralization treatment is performed on the wastewater. When the neutralization is in progress, the first adjustment stirring power of the stirrer system is determined according to the first flocculating agent information and the first temperature power information, so that the stirrer system can select an appropriate temperature when processing in the neutralization tank, the stirring speed is reduced as much as possible when the neutralization efficiency is guaranteed to be maximized, liquid splashing and diffusion are avoided, the neutralization efficiency is improved, the neutralization material is saved, and meanwhile, the environment near the neutralization tank is protected.

According to the technical scheme provided by the invention, different neutralization modes can be obtained by judging different volumes of the first liquid to be treated and the second liquid to be treated during mutual neutralization, wherein the neutralization modes comprise full-load neutralization of a stirrer system and half-load neutralization of the stirrer system. According to the invention, the first untreated sub-demand and the second untreated sub-demand are obtained according to the first untreated sub-volume and the second untreated sub-volume, so that an administrator can configure the additionally added neutralizing agent according to the first untreated sub-demand and the second untreated sub-demand, and different types of neutralizing agents can be added for treatment when the volumes and the pH values of the first liquid to be treated and the second liquid to be treated are unbalanced. In addition, the method can obtain the neutralization representation of the scene table according to the first unprocessed sub-requirement, the second unprocessed sub-requirement, the first neutralization frequency and the second neutralization frequency, so that an administrator can obtain the self-neutralization efficiency of the whole wastewater treatment system according to the neutralization representation, corresponding basis is provided for energy-saving and environment-friendly evaluation, and a preparation direction is provided for preparation of subsequent neutralization.

According to the technical scheme provided by the invention, first adjustment information can be obtained according to the difference trend between the first flocculating agent information and the reference flocculation information, second adjustment information can be obtained according to the difference trend between the first temperature information and the reference temperature information, and the first reference stirring power is adjusted according to the first adjustment information and the second adjustment information to obtain the first adjustment stirring power, so that the first adjustment stirring power provided by the invention refers to information of multiple dimensions, and the first adjustment stirring power can be adjusted according to the adjustment of the temperature and the flocculation condition. The method and the device can monitor the use behavior of an administrator, and obtain first adjustment information and/or second adjustment information according to adjustment of the first flocculating agent information and/or the first temperature power information, so as to obtain adaptive third adjustment stirring power. According to the invention, the adjusted third adjusted stirring power is compared with the first adjusted stirring power and/or the second adjusted stirring power, and the first reference stirring power is adjusted according to the corresponding comparison result to obtain the second reference stirring power, so that the adjusted second reference stirring power is more accurate.

Drawings

Fig. 1 is a system structure scene diagram of a first embodiment of the technical solution provided in the present invention;

fig. 2 is a view of a mechanical structure scenario of a second embodiment of the technical solution provided by the present invention;

FIG. 3 is a flow diagram of a first embodiment of a data processing method suitable for use in a blender system for industrial wastewater treatment;

FIG. 4 is a flow diagram of a second embodiment of a data processing method suitable for use with a blender system for industrial wastewater treatment;

fig. 5 is a system configuration scene diagram of a third embodiment of the technical solution provided by the present invention.

Detailed Description

In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

The terms "first," "second," "third," "fourth," and the like in the description and in the claims, as well as in the drawings, if any, are used for distinguishing between similar elements and not necessarily for describing a particular sequential or chronological order. It is to be understood that the data so used is interchangeable under appropriate circumstances such that the embodiments of the invention described herein are capable of operation in sequences other than those illustrated or described herein.

It should be understood that, in various embodiments of the present invention, the sequence numbers of the processes do not mean the execution sequence, and the execution sequence of the processes should be determined by the functions and the internal logic of the processes, and should not constitute any limitation on the implementation process of the embodiments of the present invention.

It should be understood that in the present application, "comprising" and "having" and any variations thereof, are intended to cover a non-exclusive inclusion, such that a process, method, system, article, or apparatus that comprises a list of steps or elements is not necessarily limited to those steps or elements expressly listed, but may include other steps or elements not expressly listed or inherent to such process, method, article, or apparatus.

It should be understood that, in the present invention, "a plurality" means two or more. "and/or" is merely an association describing an associated object, meaning that three relationships may exist, e.g., a and/or B, may mean: a exists alone, A and B exist simultaneously, and B exists alone. The character "/" generally indicates that the former and latter associated objects are in an "or" relationship. "comprises A, B and C" and "comprises A, B, C" means that A, B, C all comprise, "comprises A, B or C" means comprise one of A, B, C, "comprises A, B and/or C" means comprise any 1 or any 2 or 3 of A, B, C.

It should be understood that in the present invention, "B corresponding to a", "a corresponds to B", or "B corresponds to a" means that B is associated with a, and B can be determined from a. Determining B from a does not mean determining B from a alone, but may be determined from a and/or other information. And the matching of A and B means that the similarity of A and B is greater than or equal to a preset threshold value.

As used herein, "if" may be interpreted as "at … …" or "when … …" or "in response to a determination" or "in response to a detection", depending on the context.

The technical solution of the present invention will be described in detail below with specific examples. These several specific embodiments may be combined with each other below, and details of the same or similar concepts or processes may not be repeated in some embodiments.

As shown in fig. 1, a scene diagram of a blender system for industrial wastewater treatment according to the present invention includes a first tank to be treated, a second tank to be treated, and a neutralization tank, wherein the first tank to be treated and the second tank to be treated are respectively communicated with the neutralization tank through a first communication pipeline and a second communication pipeline. The first to-be-treated tank is used for containing a first to-be-treated liquid, and the second to-be-treated tank is used for containing a second to-be-treated liquid. A first peristaltic pump and a second peristaltic pump are arranged in the first communicating pipeline and the second communicating pipeline.

As shown in fig. 2, a machine frame is arranged at the upper part of the neutralization tank, the speed reducer is fixed through the machine frame, the output shaft of the motor is fixed with the speed reducer, the output shaft of the speed reducer is connected with a coupler, the coupler is connected with a stirring shaft, the stirring shaft is connected with a stirring blade, and the liquid neutralized in the neutralization tank is stirred through the stirring blade. Generally, the acid-base properties of the liquids stored in the first tank to be treated and the second tank to be treated are different, and if the first liquid to be treated is acidic, the second liquid to be treated is alkaline. Likewise, if the first liquid to be treated is alkaline, the second liquid to be treated is acidic. The bottom and wall of the neutralizing tank can be provided with heating units, such as heating wires, etc., and the liquid in the neutralizing tank is heated by the heating wires.

The first pond, the second pond and the neutralization pond of waiting to handle are provided with first PH value sensor, second PH value sensor and neutralization PH value sensor respectively, can wait to handle the PH value of the first liquid and the second liquid of waiting to handle in pond, the second pond of waiting to handle of the first pond of waiting to handle of second PH value sensor and detect through first PH value sensor and obtain first PH information and second PH information.

The first to-be-treated pool and the second to-be-treated pool are respectively provided with a first liquid level meter and a second liquid level meter, first liquid level information and second liquid level information of the first to-be-treated pool and the second to-be-treated pool can be obtained through the first liquid level meter and the second liquid level meter, and first volume information and second volume information are obtained through calculation according to the sectional areas of the first to-be-treated pool and the second to-be-treated pool, the first liquid level information and the second liquid level information.

The neutralization tank can be connected with other tank bodies through an output pipeline, and the neutralized mixed liquid is discharged into other tank bodies. And primary neutralization between the primary waste liquid and the waste liquid to be treated is realized. The flocculant can be added manually or automatically, and the method for adding the flocculant is not limited in any way. The invention can perform flocculation treatment on the liquid to be treated in the initial neutralization process, thereby reducing the impurities in the liquid to be treated.

The stirrer system for industrial wastewater treatment comprises a processor, wherein the processor is respectively connected with a first peristaltic pump, a second peristaltic pump, a motor, a first PH value sensor, a second PH value sensor, a neutralization PH value sensor, a first liquid level meter, a second liquid level meter, a suspended matter rapid determinator, a heating wire and the like, and is used for acquiring and controlling information and data.

The present invention provides a data processing method suitable for a stirrer system for industrial wastewater treatment, as shown in fig. 3, comprising:

step S110, acquiring first PH information and first volume information of the first liquid to be processed, second PH information and second volume information of the second liquid to be processed, and generating corresponding first neutralization information and second neutralization information based on the neutralization volume information. The neutralization volume information may be a nominal volume within the neutralization tank in which the liquid may be placed. In general, the nominal volume of the neutralization tank is set in advance. According to the invention, first neutralization information and second neutralization information can be obtained according to the PH information and the volume information of different liquids, wherein the first neutralization information can be regarded as the volume of the liquid flowing into the neutralization tank from the first tank to be treated, and the second neutralization information can be regarded as the volume of the liquid flowing into the neutralization tank from the second tank to be treated.

In a possible implementation manner of the technical solution provided by the present invention, as shown in fig. 4, step S110 specifically includes:

step S1101, obtaining PH value ratio information of the first liquid to be treated and the second liquid to be treated according to the first PH information and the second PH information. In an actual neutralization scenario, the PH values of the first liquid to be treated and the second liquid to be treated may be different, for example, the PH value of the first PH information is 5, the PH value of the second PH information is 8, if the conventional PH value of the conventional liquid is considered to be 7, then there are 2 differences between the first PH information and the conventional PH value 7, and at this time, there are 1 differences between the second PH information and the conventional PH value 7, then it is considered that the acidity intensity corresponding to the first PH information is higher than the alkalinity intensity corresponding to the second PH information. So that the corresponding PH ratio information is obtained according to the first PH information and the second PH information.

And step S1102, obtaining first initial information and second initial information according to the PH value proportion information and the neutralization volume information. The method and the device can obtain corresponding first initial information and second initial information by combining the PH value proportion information and the neutralization volume information, so that the determination of the first initial information and the second initial information not only combines the PH value proportion information, but also combines the neutralization volume information of the neutralization pool, the total volume of the determined first initial information and the second initial information is not larger than the neutralization volume information, and the volume capable of being accommodated is provided for the neutralization pool.

In a possible implementation manner of the technical solution provided by the present invention, step S1102 specifically includes:

and comparing the first PH information with the standard PH information to obtain a first PH difference value, and comparing the second PH information with the standard PH information to obtain a second PH difference value. The invention compares the first PH information and the second PH information with the standard PH information respectively to obtain a first PH difference value and a second PH difference value.

And obtaining PH value proportion information according to the first PH value and the second PH value, and obtaining first initial information and second initial information according to the PH value proportion information and the volume information.

wherein the content of the first and second substances,

is a numerical value corresponding to the first initial information,

is a weight of the first PH, and is,

is a numerical value of the first PH information,

is a weight of the second PH, and,

is a value of the second PH information,

in order to neutralize the value of the volume information,

the value is corresponding to the second initial information.

The PH value ratio information at this time is two types, the 1 st type is

In this scenario, the PH ratio of the first PH information to the total PH information is defined, and the total PH information may be the sum of the first PH information and the second PH information. The 2 nd species are

In this scenario, the PH ratio of the second PH information to the total PH information is, and the total PH information may be the sum of the first PH information and the second PH information.

The technical scheme provided by the invention is that

Obtaining a first pH value according to

A second PH difference is obtained. According to

Obtaining weighted first PH value proportion information corresponding to the first PH information according to

And obtaining weighted second PH value proportion information corresponding to the second PH information. Then respectively connect

And

and multiplying the numerical value of the neutralization volume information to obtain a numerical value corresponding to the first initial information and a numerical value corresponding to the second initial information. In the above manner, the ratio of the first liquid to be treated and the second liquid to be treated in the neutralization treatment is adapted, and the sum of the first liquid to be treated and the second liquid to be treated does not exceed the value of the neutralization volume information.

Step S1103, if the first initial information and the second initial information are smaller than the first volume information and the second volume information, respectively, taking values corresponding to the first initial information and the second initial information as first neutralization information and second neutralization information, so as to neutralize the full load of the blender system. After the first initial information and the second initial information are obtained, the first initial information and the second initial information and the first volume information and the second volume information are firstly obtained, if the first initial information and the second initial information are respectively smaller than the first volume information and the second volume information, the fact that the quantity values of the liquid corresponding to the first initial information and the second initial information can be introduced into the neutralization tank for neutralization treatment is proved, so that the numerical values corresponding to the first initial information and the second initial information can be used as the first neutralization information and the second neutralization information, and the full-load neutralization of the blender system is realized, namely the volume of the liquid in the neutralization tank in the blender system reaches the rated volume. When the blender system is fully loaded and neutralized, then the neutralization efficiency at that time is maximized.

In one possible implementation manner, if the first initial information is greater than the first volume information, the first volume information is used as first neutralization information, and second neutralization information is determined according to the first volume information. When the first initial information is larger than the first volume information, it is proved that the volume of the first liquid to be treated in the first liquid to be treated is smaller, and at the moment, the first liquid to be treated cannot provide the liquid with the volume corresponding to the first initial information, so that the first volume information can be used as the first neutralization information, and as the first neutralization information is smaller than the first initial information, in order to ensure that the pH value of the first liquid and the second liquid after fusion is close to 7, the second neutralization information needs to be reduced, namely the second neutralization information is obtained according to the volume value corresponding to the first volume information.

And obtaining second neutralization information according to the PH value proportion information and the first volume information so as to enable the stirrer system to be neutralized at half load. According to the invention, second neutralization information is obtained according to the PH value proportion information and the first volume information, and at the moment, the stirrer system is controlled to carry out half-load neutralization. At this time, the sum of the first liquid to be treated and the second liquid to be treated in the mixer system does not reach the rated volume, so that the half-load neutralization is needed at this time, and the operation efficiency of the mixer system is poor at this time.

And if the second initial information is larger than the second volume information, taking the second volume information as second neutralization information, and determining first neutralization information according to the second volume information. When the second initial information is larger than the second volume information, it is proved that the volume of the second liquid to be treated in the second liquid to be treated is smaller, and at this time, the second liquid to be treated cannot provide the liquid with the volume corresponding to the second initial information, so that the second volume information can be used as second neutralization information, and as the second neutralization information is smaller than the second initial information, in order to ensure that the pH value of the second liquid and the first liquid after being fused is close to 7, the first neutralization information needs to be reduced, namely the first neutralization information is obtained according to the volume value corresponding to the second volume information.

And obtaining first neutralization information according to the PH value proportion information and the second volume information so as to enable the stirrer system to be neutralized at half load. The invention obtains the first neutralization information according to the PH value proportion information and the second volume information, and controls the stirrer system to carry out half-load neutralization at the moment. At this time, the sum of the first liquid to be treated and the second liquid to be treated in the mixer system does not reach the rated volume, so that the half-load neutralization is needed at this time, and the operation efficiency of the mixer system is poor at this time.

wherein the content of the first and second substances,

is the first volume information of the first volume information,

in order to be the second volume information,

in order to be able to neutralize the information for the second time,

in order to be the first neutralizing information,

in order to be the second neutralization weight,

is a first neutralization weight.

By passing

The PH ratio information may be obtained, where the PH ratio information is a ratio of the type 3, that is, a ratio of the second PH information to the first PH information. By passing

The PH ratio information may be obtained, where the PH ratio information is a ratio of the type 4, that is, a ratio of the first PH information to the second PH information. Through the mode, when the first volume information and the second volume information are smaller, the first neutralization information and the second neutralization information can be obtained according to the magnitude of the first volume information and the second volume information, the calculated first neutralization information and the calculated second neutralization information are in accordance with an objective neutralization scene, on the premise that the PH value of the mixed liquid of the first liquid to be treated and the second liquid to be treated after neutralization is close to 7, the corresponding first liquid to be treated and the second liquid to be treated are introduced to the maximum range, and the volumes of the first liquid to be treated and the second liquid to be treated are adapted.

Step S120, controlling partial liquid in the first liquid to be treated and the second liquid to be treated to flow into a neutralization area according to the first neutralization information and the second neutralization information, and acquiring first temperature information and first suspended matter information at the neutralization area. According to the technical scheme provided by the invention, after the first neutralization information and the second neutralization information are obtained, partial liquid in the first liquid to be treated and the second liquid to be treated is controlled to flow into the neutralization area for neutralization treatment through the peristaltic pump, and when the neutralization treatment is carried out, the first temperature information and the first suspended matter information at the neutralization area can be obtained. The first suspended matter information is different due to different substances of the wastewater discharged under the scene. In addition, in the process of absorbing heat, releasing heat and the like when neutralization is performed, in an actual neutralization scene, if the temperature is also higher, the neutralization efficiency is higher, so that the first temperature information at the neutralization area needs to be obtained.

Step S130, first flocculant information is generated according to the first suspended matter information, and power weighting processing is carried out after the first temperature information is compared with the reference temperature information to generate first temperature power information. According to the technical scheme provided by the invention, first flocculant information can be generated according to the first suspended matter information, the first suspended matter information can be obtained through a suspended matter rapid determinator, the first flocculant information can be obtained according to the numerical value of the first suspended matter information, for example, a flocculant determining function exists, the first flocculant information corresponding to different first suspended matter information can be obtained through the flocculant determining function, and the suspended matter can be subjected to precipitation treatment through a flocculant. This kind of mode for first liquid and the second liquid of treating carry out the flocculation, the sediment of suspended solid promptly at the neutralization in-process, make the pH valve of the material after the sediment more be close to neutrality, and then play the purpose of environmental protection, deposit promptly and can increase substantially the efficiency of non also handling.

In the actual neutralization process, different regions have different temperatures, so that the temperature of the liquid in the neutralization tank needs to be detected and correspondingly heated and adjusted. The invention obtains the first temperature power information according to the first temperature information and the reference temperature information. The reference temperature information may be preset, for example, 30 degrees, 40 degrees, and the like. Wherein the lower the first temperature information is, the higher the first temperature power information is.

Step S140, comparing the first flocculating agent information with the reference flocculating information, adjusting and weighting to generate first adjusting information, and comparing the first temperature information with the reference temperature information, adjusting and weighting to generate second adjusting information.

In an actual neutralizing and stirring scene, the more turbid substances in the liquid, the poorer the neutralizing efficiency, and the larger the required stirring speed, so the first flocculant information and the reference flocculation information are compared and then are adjusted and weighted to generate first adjustment information, and the first flocculant information is in direct proportion to the first adjustment information. In addition, the lower the temperatures of the first liquid to be treated and the second liquid to be treated are, the lower the efficiency of neutralization is, and therefore the required stirring speed is increased, so the present invention compares the first temperature information with the reference temperature information, and then performs adjustment weighting to generate the second adjustment information, wherein the first temperature information is inversely proportional to the first adjustment information.

In a possible implementation manner of the technical solution provided by the present invention, step S140 specifically includes:

and comparing the first flocculating agent information with reference flocculation information to obtain first flocculation difference information, and weighting the first flocculation difference information to obtain first adjustment information. The larger the first flocculation difference information is, the more liquid suspended matters and the more sediments after neutralization are proved to be, so that at this time, first adjustment information needs to be obtained according to the first flocculation difference information, and the adjustment of the stirring power is guided by the first adjustment information.

And comparing the first temperature information with reference temperature information to obtain first temperature difference information, and weighting the first temperature difference information to obtain second adjustment information. The larger the first temperature difference information is, the lower the temperature of the neutralized liquid is, so that at this time, second adjustment information needs to be obtained according to the first temperature difference information, and the adjustment of the stirring power is guided by the second adjustment information.

And S150, adjusting first reference stirring power according to the first adjustment information and the second adjustment information to obtain first adjustment stirring power, and controlling the stirrer system for industrial wastewater treatment according to the first adjustment stirring power, the first flocculating agent information and the first temperature power information. According to the technical scheme provided by the invention, after the first adjustment information and the second adjustment information are obtained, the first reference stirring power is adjusted. It can be understood that the first reference stirring power is the case of the reference flocculation information and the reference temperature information, the case of the liquid neutralization, and the most efficient. Therefore, the present invention obtains the first adjusted stirring power according to the first adjustment information and the second adjustment information, and the larger the absolute value of the first adjustment information and the second adjustment information is, the larger the difference between the adjusted first adjusted stirring power and the first reference stirring power before adjustment is.

In a possible implementation manner of the technical solution provided by the present invention, step S150 specifically includes:

wherein the content of the first and second substances,

to calculate the adjusted first adjusted stirring power,

as the first adjustment information, it is possible to adjust,

in order to be the second adjustment information,

is a reference constant value that is a function of,

is the first reference stirring power and is,

in order to adjust the weight for the first time,

as information on the first flocculating agent, it is,

as information on the second flocculating agent, the flocculating agent,

is a first normalized value of the first normalized value,

in order to adjust the weight for the second time,

as the information on the first temperature, it is,

as the information on the reference temperature, there is,

is the second normalized value. By passing

The weighted first adjustment information can be obtained by

The weighted second adjustment information may be obtained. The invention can preset the reference constant value

Reference constant value

It may be a 1-bit (r) bit,

the larger the first adjusted stirring power after adjustment. Through the mode, the stirring power can be adjusted under different flocculation conditions and different temperatures. The stirring power regulation is the stirring power regulation of the motor, the output shaft of the motor is connected with the speed reducer, and the stirring power regulation is controlled by the corresponding powerThe stirring blade rotates.

In a possible implementation manner, after step S150, the technical solution provided by the present invention specifically includes:

monitoring the use behavior of an administrator, and if the administrator is judged to adjust the first flocculant information and/or the first temperature power information, obtaining the adjusted first adjustment information and/or second adjustment information according to the adjusted first flocculant information and/or first temperature power information. According to the technical scheme provided by the invention, the temperature is heated and the flocculating agent is added according to the calculated first flocculating agent information and/or first temperature power information, and an administrator may think that the current scene needs to add more flocculating agents or adjust the temperature to be high so as to strengthen the precipitation of the liquid in the neutralization tank or increase the temperature. After the first flocculant information and/or the first temperature power information are/is adjusted, the adjusted first adjustment information and/or second adjustment information can be obtained according to the adjustment, so that the adjustment of the power is dynamically changed.

And adjusting the first adjusting stirring power for the second time according to the adjusted first adjusting information and/or second adjusting information to obtain adjusted second adjusting stirring power. After the first adjustment information and/or the second adjustment information are obtained, the adjusted second adjustment stirring power is obtained according to the first adjustment information and/or the second adjustment information, so that the second adjustment stirring power is dynamically changed according to the adjusted first flocculating agent information and/or the adjusted first temperature power information.

And if the judgment manager adjusts any one of the first adjustment stirring power and/or the second adjustment stirring power, obtaining the adjusted third adjustment stirring power. If the administrator is judged to directly adjust any one of the first adjustment stirring power and/or the second adjustment stirring power, the administrator is proved to consider that the first flocculating agent information and the first temperature power information are well adjusted at the moment, so that the first adjustment stirring power and/or the second adjustment stirring power are adjusted at the moment, and a corresponding third adjustment stirring power is obtained.

And adjusting the first reference stirring power according to the difference value of the first adjustment stirring power and/or the second adjustment stirring power and the third adjustment stirring power to obtain second reference stirring power. According to the technical scheme provided by the invention, after the third adjustment stirring power is obtained, the first reference stirring power is corrected and adjusted, so that the corrected and adjusted second reference stirring power is more suitable for the current neutralization scene. Generally, different wastewater treatment systems are fixed facing the wastewater discharged from one or more companies, with relatively little variability in wastewater, so that a first baseline agitation power can be continuously trained to obtain a second baseline agitation power suitable for the properly discharged wastewater.

The adjusted second reference stirring power is obtained by,

wherein the content of the first and second substances,

for the second adjusted stirring power after the adjustment,

for the third adjusted stirring power after adjustment,

is the second reference stirring power and is,

in order to adjust the coefficient in the forward direction,

the coefficients are adjusted in reverse. According to the technical scheme provided by the invention, a forward adjustment coefficient and a reverse adjustment coefficient are preset. It can be understood that the forward adjustment coefficient is a forward adjustment of the first reference stirring power, and the reverse adjustment coefficient is a reverse adjustment of the first reference stirring power.

By passing

And

the second reference stirring power after adjustment obtained when the second adjusted stirring power after adjustment is larger than the first adjusted stirring power before adjustment and the third adjusted stirring power is larger than the first adjusted stirring power before adjustment can be obtained,

and

the larger the second reference stirring power is, the larger the adjusted second reference stirring power is.

By passing

And

the second reference stirring power after adjustment obtained when the second adjusted stirring power after adjustment is smaller than the first adjusted stirring power before adjustment and the third adjusted stirring power is smaller than the first adjusted stirring power before adjustment can be obtained,

and

the larger the second reference stirring power is, the smaller the adjusted second reference stirring power is.

In a possible embodiment, the technical solution provided by the present invention further includes:

and acquiring information of full-load neutralization and half-load neutralization of the stirrer system in a preset time period to obtain a neutralization scene table. The invention can generate a neutralization scene table, and the working condition of the stirrer system for industrial wastewater treatment can be obtained through the neutralization scene table, the higher the full-load neutralization frequency of the stirrer system is, the higher the utilization rate of the stirrer system is, and the higher the neutralization treatment efficiency of the first wastewater to be treated and the second wastewater to be treated is.

And acquiring first to-be-treated liquid and second to-be-treated liquid which are in full-load neutralization and half-load neutralization inflow of the stirrer system in the neutralization scene table every time to obtain first self-neutralization total volume information and second self-neutralization total volume information. The method can be used for counting the first liquid to be treated and the second liquid to be treated to obtain the first self-neutralization total volume information and the second self-neutralization total volume information which need to be treated.

Acquiring first treatment total volume information of a first liquid to be treated flowing into the treatment tank and second treatment total volume information of a second liquid to be treated flowing into the treatment tank within a preset time period. The invention can count the first liquid to be treated and the second liquid to be treated which flow into the neutralization tank to obtain the first total volume processing information and the second total volume processing information.

And obtaining unprocessed gross volume information according to the first self-neutralizing gross volume information, the second self-neutralizing gross volume information, the first processed gross volume information and the second processed gross volume information. All volumes that are not neutralized by the first fluid to be treated and the first fluid to be treated are regarded as the total untreated volume, and the present invention calculates the total untreated volume information.

And obtaining neutralization demand information according to the unprocessed total volume information. The greater the raw total volume information, the greater the need for external neutralizing agent is evidenced, so the present invention will derive the need information based on the need for external neutralizing agent. The external neutralizing agent includes an acidic neutralizing agent, a basic neutralizing agent, and the like. The total volume information is proportional to the neutralizer demand, for example, 0.05 ml of alkaline neutralizer is needed for a 1 liter, PH 5 liquid. If the liquid in the untreated total volume information is 100 liters and the PH value is 5, the alkaline neutralizing agent corresponding to the demand information is 5 liters.

In a possible embodiment, the method for obtaining unprocessed total volume information according to first self-neutralizing total volume information, second self-neutralizing total volume information, first processed total volume information, and second processed total volume information specifically includes:

a first untreated sub-volume is obtained from a difference between the first self-neutralizing total volume information and the first treated total volume information. According to the technical scheme provided by the invention, a first untreated sub-volume is obtained by subtracting the first self-neutralization total volume information from the first treatment total volume information, and the first untreated sub-volume is the volume of the liquid which is not subjected to mutual neutralization in all the first liquid to be treated.

And obtaining a second untreated sub-volume according to the difference between the second self-neutralization total volume information and the second treatment total volume information. According to the technical scheme provided by the invention, a second untreated sub-volume is obtained by subtracting the second self-neutralization total volume information from the second treatment total volume information, and the first untreated sub-volume is the volume of the liquid which is not subjected to mutual neutralization in all the second liquid to be treated.

Obtaining a first unprocessed sub-demand and a second unprocessed sub-demand from the first unprocessed sub-volume and a second unprocessed sub-volume, the neutralization demand information including the first unprocessed sub-demand and the second unprocessed sub-demand. According to the technical scheme provided by the invention, the first untreated sub-demand and the second untreated sub-demand are obtained according to the first untreated sub-volume and the second untreated sub-volume, and the quantity values of the demands of the acid neutralizing agent and the alkaline neutralizing agent, namely the first untreated sub-demand and the second untreated sub-demand, are obtained by calculating according to the first untreated sub-volume and the second untreated sub-volume.

a first number of neutralizations of a full-load neutralization of the blender system and a second number of neutralizations of a half-load neutralization of the blender system within the neutralization scenario table are determined. According to the technical scheme provided by the invention, the first neutralization frequency and the second neutralization frequency are determined firstly. The greater the number of first neutralizations, the greater the efficiency of the blender system in performing the neutralization between the effluents to be treated. The greater the number of second neutralizations, the less efficient the blender system is in neutralizing the effluent to be treated.

And generating a neutralization image corresponding to the scene table according to the first unprocessed sub-requirement, the second unprocessed sub-requirement, the first neutralization frequency and the second neutralization frequency. The greater the first and second untreated sub-requirements, the more neutralising agent required and the greater the amount of liquid that cannot be neutralised between liquids, the less efficient the mixer system will be in neutralising between the effluents to be treated. The invention can perform fusion calculation to obtain a neutralization portrait, and the neutralization portrait reflects the requirement condition of the blender system.

The neutralization image is calculated by the following formula,

wherein the content of the first and second substances,

for neutralizing the value corresponding to the image,

the weight of the first image is used as the weight of the first image,

for inflow within a predetermined period of time

A volume information value of the first liquid to be treated,

for the upper limit value of the inflow of the first liquid to be treated,

The first liquid to be treated is introduced into the treatment chamber,

for the first time period

A volume information value of the second liquid to be treated,

for the upper limit value of the inflow of the second liquid to be treated,

A second liquid to be treated,

the first image constant is constant and the second image constant is constant,

the weight of the second image is used as the weight of the second image,

as the number of the first neutralization times,

as the number of times of the second neutralization,

is the second image constant.

By passing

The sum of the first to-be-treated liquid in the preset time period can be obtained to obtain first treatment total volume information. By passing

The sum of the first liquid to be treated flowing in during full-load neutralization of the blender system or half-load neutralization of the blender system in a preset time period can be obtained to obtain first self-neutralization total volume information. By passing

And obtaining the sum of the second liquid to be treated in the preset time period to obtain second treatment total volume information. By passing

And the sum of the second liquid to be treated flowing in during full-load neutralization of the stirrer system or half-load neutralization of the stirrer system in a preset time period can be obtained to obtain second self-neutralization total volume information. By passing

A sum of the first unprocessed sub-requirement and the second unprocessed sub-requirement may be obtained, and the larger the sum of the first unprocessed sub-requirement and the second unprocessed sub-requirement, the larger the value of the corresponding neutralized sketch.

By passing

The ratio of the second neutralization number to all neutralization numbers can be obtained. If it is not

The larger theThe more times of half-load neutralization, the lower the neutralization efficiency of the mixer system, and the higher the neutralized image.

The present invention will preset the first image weight

And second portrait weight

. First image weight

And second portrait weight

The setting can be carried out according to the actual scene requirement.

The invention can obtain the neutralization images of a plurality of industrial wastewater treatment stirrer systems, and the neutralization images are sequenced according to descending sequence to obtain an image sequence. It can be understood that the more advanced the neutralization image in the image sequence, the poorer the neutralization efficiency of the mixer system for industrial wastewater treatment.

And carrying out operation reminding on an administrator according to the portrait sequence. The neutralizing image larger than the preset value in the image sequence can be displayed, and the administrator can analyze the image sequence, and the neutralizing image larger than the preset value proves that the neutralizing efficiency of the two liquids with different pH values is lower, so that the neutralizing treatment is more suitable.

According to the technical scheme, in a possible real-time scene, as shown in fig. 5, the system comprises a cloud server and a plurality of industrial wastewater treatment stirrer systems, and a neutralized portrait sent by each industrial wastewater treatment stirrer system is received by the cloud server.

The technical scheme provided by the invention can provide the neutralization efficiency condition of each industrial wastewater treatment stirrer system for an administrator according to the neutralization image, so that the administrator can distribute the alkaline neutralizing agent and the acidic neutralizing agent in a plurality of industrial wastewater treatment stirrer systems in advance, analyze the pH value of the wastewater of each industrial wastewater treatment stirrer system, and introduce more diversified wastewater with different pH values into the industrial wastewater treatment stirrer system with higher neutralization image. And a decision basis is provided for the drainage of the wastewater to be treated and the distribution of the neutralizing agent in the later stage of an administrator through the neutralizing image of each stirrer system.

The present invention also provides a storage medium having a computer program stored therein, the computer program being executable by a processor to implement the methods provided by the various embodiments described above.

The storage medium may be a computer storage medium or a communication medium. Communication media includes any medium that facilitates transfer of a computer program from one place to another. Computer storage media may be any available media that can be accessed by a general purpose or special purpose computer. For example, a storage medium is coupled to the processor such that the processor can read information from, and write information to, the storage medium. Of course, the storage medium may also be integral to the processor. The processor and the storage medium may reside in an Application Specific Integrated Circuits (ASIC). Additionally, the ASIC may reside in user equipment. Of course, the processor and the storage medium may reside as discrete components in a communication device. The storage medium may be read-only memory (ROM), random-access memory (RAM), CD-ROMs, magnetic tapes, floppy disks, optical data storage devices, and the like.

The present invention also provides a program product comprising execution instructions stored in a storage medium. The at least one processor of the device may read the execution instructions from the storage medium, and the execution of the execution instructions by the at least one processor causes the device to implement the methods provided by the various embodiments described above.

In the embodiment of the terminal or the server, it should be understood that the Processor may be a Central Processing Unit (CPU), other general-purpose processors, a Digital Signal Processor (DSP), an Application Specific Integrated Circuit (ASIC), and the like. A general purpose processor may be a microprocessor or the processor may be any conventional processor or the like. The steps of a method disclosed in connection with the present invention may be embodied directly in a hardware processor, or in a combination of the hardware and software modules within the processor.

Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; while the invention has been described in detail and with reference to the foregoing embodiments, it will be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.

Claims

1. A data processing method applicable to a stirrer system for industrial wastewater treatment is characterized by comprising the following steps:

2. The data processing method applicable to a blender system for industrial wastewater treatment according to claim 1,

in the step of acquiring first PH information and first volume information of a first liquid to be treated, and second PH information and second volume information of a second liquid to be treated, and generating corresponding first neutralization information and second neutralization information based on the neutralization volume information, the method specifically includes:

3. The data processing method applicable to a blender system for industrial wastewater treatment according to claim 2,

in the step of obtaining the first initial information and the second initial information according to the PH ratio information and the neutralization volume information, the method specifically includes:

wherein the content of the first and second substances,

is a numerical value corresponding to the first initial information,

is a weight of the first PH, and is,

is a numerical value of the first PH information,

is a weight of the second PH, and,

is a numerical value of the second PH information,

in order to neutralize the value of the volume information,

the value is corresponding to the second initial information.

4. The data processing method for use in a blender system for industrial wastewater treatment according to claim 3,

if the first initial information is larger than the first volume information, taking the first volume information as first neutralization information, and determining second neutralization information according to the first volume information;

wherein the content of the first and second substances,

is the first volume information of the first volume information,

in order to be the second volume information,

in order to be able to neutralize the information for the second time,

in order to be the first neutralizing information,

in order to be the second neutralization weight,

is a first neutralization weight.

5. The data processing method for use in a blender system for industrial wastewater treatment according to claim 4, further comprising:

6. The data processing method for use in a blender system for industrial wastewater treatment according to claim 5,

in the step of obtaining unprocessed gross volume information according to the first self-neutralization gross volume information, the second self-neutralization gross volume information, the first processed gross volume information, and the second processed gross volume information, the method specifically includes:

7. The data processing method for use in a blender system for industrial wastewater treatment according to claim 6, further comprising:

the neutralization image is calculated by the following formula,

wherein the content of the first and second substances,

for neutralizing the value corresponding to the image,

the weight of the first image is used as the weight of the first image,

for inflow within a predetermined period of time

A volume information value of the first liquid to be treated,

for the upper limit value of the inflow of the first liquid to be treated,

The first liquid to be treated is introduced into the treatment chamber,

for inflow within a predetermined period of time

A volume information value of the second liquid to be treated,

for the upper limit value of the inflow of the second liquid to be treated,

A second liquid to be treated,

the upper limit of the second fluid to be treated which flows into the blender system at full load and at half load,

the first image constant is constant and the second image constant is constant,

the weight of the second image is used as the weight of the second image,

as the number of the first neutralization times,

as the number of times of the second neutralization,

is a second image constant;

8. The data processing method applicable to a blender system for industrial wastewater treatment according to claim 7,

after the step of controlling the stirrer system for industrial wastewater treatment according to the first adjustment stirring power, the first flocculant information, and the first temperature power information, the method specifically includes:

the adjusted second reference stirring power is obtained by,

wherein the content of the first and second substances,

for the second adjusted stirring power after the adjustment,

for the third adjusted stirring power after adjustment,

is the second reference stirring power and is,

in order to adjust the coefficient in the forward direction,

the coefficients are adjusted in reverse.