CN116736745A - Control method, device and system of mixing equipment - Google Patents
Control method, device and system of mixing equipment Download PDFInfo
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- CN116736745A CN116736745A CN202310827684.1A CN202310827684A CN116736745A CN 116736745 A CN116736745 A CN 116736745A CN 202310827684 A CN202310827684 A CN 202310827684A CN 116736745 A CN116736745 A CN 116736745A
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- 238000000034 method Methods 0.000 title claims abstract description 31
- 239000000463 material Substances 0.000 claims abstract description 120
- 238000003756 stirring Methods 0.000 claims description 95
- 238000012937 correction Methods 0.000 claims description 44
- 238000007599 discharging Methods 0.000 claims description 40
- 230000001965 increasing effect Effects 0.000 claims description 25
- 230000003247 decreasing effect Effects 0.000 claims description 12
- 238000012545 processing Methods 0.000 claims description 11
- 238000004891 communication Methods 0.000 claims description 7
- 238000012423 maintenance Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 26
- 230000001276 controlling effect Effects 0.000 description 23
- 230000000694 effects Effects 0.000 description 22
- 230000000875 corresponding effect Effects 0.000 description 12
- 238000005086 pumping Methods 0.000 description 12
- 238000004537 pulping Methods 0.000 description 11
- 239000002699 waste material Substances 0.000 description 11
- 239000011343 solid material Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000011344 liquid material Substances 0.000 description 6
- 238000012544 monitoring process Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 230000008859 change Effects 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 5
- 230000001960 triggered effect Effects 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 3
- 238000007664 blowing Methods 0.000 description 3
- 230000002925 chemical effect Effects 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 3
- 239000002920 hazardous waste Substances 0.000 description 3
- 230000006978 adaptation Effects 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000013585 weight reducing agent Substances 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 238000013135 deep learning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 239000010720 hydraulic oil Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 239000010816 packaging waste Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B19/00—Programme-control systems
- G05B19/02—Programme-control systems electric
- G05B19/04—Programme control other than numerical control, i.e. in sequence controllers or logic controllers
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention provides a control method, a device and a system of mixing equipment, wherein the control method comprises the following steps: acquiring index parameters when the mixing equipment mixes materials; determining the current material state in the mixing bin of the mixing equipment according to the index parameters; generating a control signal according to the material state in the mixing bin of the mixing equipment; and controlling the running state of the mixing equipment according to the control signal. The scheme provided by the invention can improve the working efficiency of the mixing equipment and reduce the power consumption and the manual maintenance cost of the mixing equipment.
Description
Technical Field
The present invention relates to the field of control technologies of mixing devices, and in particular, to a method, an apparatus, and a system for controlling a mixing device.
Background
The mixer in the hazardous waste pretreatment system is used for realizing the compatibility effect among different wastes, and the mixing effect and the working efficiency of the mixer are critical to the whole pretreatment system.
The internal structure of the mixer is generally divided into a mixing area and a discharging area, and the waste materials mixed in the mixing area enter the discharging area through an isolation discharging gate plate and enter a pumping link. In the actual running process of the mixer, the mixing area has poor compatibility effect of the waste materials, and when the comprehensive waste materials mixed by the mixer enter the subsequent conveying link, the mixed pulping effect directly influences the conveying of the materials in the subsequent link, so that the power consumption in the running process of the mixer is increased, and the functions of the mixer are seriously influenced;
when entering the blowing district after mixing through the compounding district and carrying out the blowing, owing to can not accurate blowing, can lead to the direct card of system to hinder (for example the jam of follow-up delivery pump and pipeline), need be forced to shut down this moment, carry out artifical clearance to the pump chamber and the high pressure pipeline of jam, this clearance work is not only the heavy task, and faces personnel and the dangerous condition of waste material direct contact.
Disclosure of Invention
The invention aims to solve the technical problem of providing a control method, a device and a system of mixing equipment, so as to solve the problem that the mixing effect is affected due to poor compatibility effect of the mixing equipment in the prior art, and effectively improve the working efficiency of the mixing equipment.
In order to solve the technical problems, the technical scheme of the invention is as follows:
a control method of a mixing apparatus, comprising:
acquiring index parameters when the mixing equipment mixes materials;
determining the current material state in a mixing bin of the mixing equipment according to the index parameters, wherein the index parameters comprise the weight of the material in the mixing bin, the torque of a stirring shaft of the mixing equipment and the temperature in the mixing bin;
generating a control signal according to the material state in the mixing bin of the mixing equipment;
and controlling the running state of the mixing equipment according to the control signal.
Optionally, when the index parameter is the weight of the material in the mixing bin and indicates that the material in the mixing bin is in an increasing or decreasing state, generating a control signal according to the state of the material in the mixing bin of the mixing device, including:
acquiring a first graph of the weight of materials in the mixing bin and the running time of mixing equipment;
and generating a gate position control signal according to the first graph and a preset weight value in a preset discharging time.
Optionally, controlling the operation state of the mixing device according to the control signal includes:
and controlling the opening or closing distance of the gate during discharging operation of the mixing equipment according to the gate position control signal.
Optionally, when the index parameter is a torque of a stirring shaft of the mixing device and an operation pressure of a driver corresponding to the torque of the stirring shaft is in an increasing or decreasing state, generating a control signal according to a state of a material in a mixing bin of the mixing device, including:
acquiring a second graph of the operating pressure and the operating time of the mixing device;
and generating a stirring shaft rotating speed control signal according to the second graph.
Optionally, when the index parameter is a temperature in the mixing bin and indicates that the temperature in the mixing bin is in an increasing or decreasing state, generating a control signal according to a state of materials in the mixing bin of the mixing device, including:
acquiring a third graph of the temperature in the mixing bin and the running time of the mixing equipment;
and generating a stirring shaft rotating speed control signal according to the third graph.
Optionally, controlling the operation state of the mixing device according to the control signal includes:
and controlling the stirring shaft of the mixing equipment to run at a preset stirring speed according to the stirring shaft rotating speed control signal.
Optionally, when the operating pressure is within a preset pressure range, the method further includes:
acquiring a correction coefficient of the running pressure and a preset pressure;
generating a feeding control signal according to the correction coefficient;
and controlling feeding and mixing operation of the mixing equipment according to the feeding control signal.
Optionally, the control method of the mixing device further includes:
and generating a compatibility list of the mixing equipment for mixing according to the correction coefficient and the feeding control signal.
A control device of a mixing apparatus, comprising:
the acquisition module is used for acquiring index parameters when the mixing equipment performs mixing operation;
the processing module is used for determining the current material state in the mixing bin of the mixing device according to the index parameters, wherein the index parameters comprise the weight of the material in the mixing bin, the torque of the stirring shaft of the mixing device and the temperature in the mixing bin; generating a control signal according to the material state in the mixing bin of the mixing equipment;
and the control module is used for controlling the running state of the mixing equipment according to the control signal.
A control system for a mixing device, comprising:
a mixing device having a mixing chamber;
a driver for driving the mixing device to operate;
the sensor is electrically connected with the driver and is arranged on the driver and used for detecting index parameters when the driver drives the mixing equipment to operate;
the processor is in communication connection with the driver and is used for determining the current material state in the mixing bin of the mixing equipment according to the index parameters; generating a control signal according to the material state in the mixing bin of the mixing equipment;
and the controller is in communication connection with the processor and is used for controlling the running state of the mixing equipment according to the control signal.
The scheme of the invention at least comprises the following beneficial effects:
1. the material weight in the mixing bin of the mixing equipment is monitored in real time, and the opening degree of the gate is controlled, so that the material discharging control in the mixing bin of the mixing equipment can be realized, and the working efficiency is improved;
2. the torque of the stirring shaft of the mixing equipment is monitored in real time, and the stirring speed of the stirring shaft of the mixing equipment is automatically adjusted; the stirring shaft of the mixing equipment is controlled to run at an accelerated speed according to a preset stirring speed, so that the aim of rapid stirring and mixing is fulfilled; or the stirring shaft of the mixing equipment is controlled to run at a reduced speed according to a preset stirring speed, the mixed materials are maintained in a homogeneous state, and meanwhile, the energy consumption of the mixing equipment is reduced, and the energy-saving effect is realized;
3. capturing correction coefficients when a dry or thin warning signal of the mixed materials is triggered and the correction coefficients after the correction of the mixing materials are finished, forming a correction coefficient trend curve, monitoring the running pressure of the mixing equipment in real time, adjusting the mixing condition in time, optimizing the mixing material pulping effect of the mixing equipment, and improving the mixing work efficiency of the mixing equipment; meanwhile, after the mixed materials are stirred by the mixer, the comprehensive waste materials with good pulping effect enter a subsequent conveying link, so that the blocking and damage to subsequent equipment can be avoided, and the effect of treating hazardous waste materials by the whole hazardous waste pretreatment system is avoided.
Drawings
Fig. 1 is a flowchart of a control method of a mixing apparatus provided by an embodiment of the present invention;
FIG. 2 is a graph of a trend of correction coefficients provided by an alternative embodiment of the present invention;
fig. 3 is a block diagram schematically illustrating a control apparatus of a mixing device according to an alternative embodiment of the present invention.
Detailed Description
Exemplary embodiments of the present invention will be described in more detail below with reference to the accompanying drawings. While exemplary embodiments of the present invention are shown in the drawings, it should be understood that the present invention may be embodied in various forms and should not be limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art.
As shown in fig. 1, an embodiment of the present invention proposes a control method of a mixing apparatus, including:
step 11, acquiring index parameters of the mixing equipment when materials are mixed;
step 12, determining the current material state in the mixing bin of the mixing equipment according to the index parameters;
step 13, generating a control signal according to the material state in the mixing bin of the mixing equipment;
and 14, controlling the running state of the mixing equipment according to the control signal.
In this embodiment, the index parameter is generated during the process of mixing the materials in the mixing device, and is used to represent the state of the materials in the mixing device or the current operation state of the mixing device; the index parameters may include: the weight of materials in the mixing bin of the mixing device, the torque of the stirring shaft of the mixing device and the temperature in the mixing bin of the mixing device; the weight of the material can be monitored in real time through a preset weight sensor, and the torque of the stirring shaft can be reflected through the corresponding operating pressure of the driver when the driver drives the stirring shaft to rotate; here, the operating pressure corresponds to a driving pressure of hydraulic oil when the driver is hydraulically driven; of course, the driver is not limited to hydraulic driving, but can also be electric driving, and when the driver is electric driving, the torque of the stirring shaft can be represented by the corresponding running current of the driving motor when the driving motor drives the stirring shaft to rotate; preferably, in the actual operation process, the temperature can be monitored in real time through a preset pressure sensor or a preset current sensor on the driver, and the temperature can be monitored in real time through a preset temperature sensor;
in the process of mixing materials, the mixing equipment monitors and collects index parameters in real time through a preset sensor, generates corresponding control signals according to the material state in the mixing bin of the mixing equipment, and further realizes accurate control on the operation of the mixing equipment according to the control signals, so that the working efficiency of the mixing equipment is improved, and the equipment power consumption is reduced.
In an optional implementation of the present invention, when the index parameter is a weight of the material in the mixing bin and indicates that the material in the mixing bin is in an increased or decreased state, the step 13 may include:
step 131a, obtaining a first graph of the weight of materials in the mixing bin and the running time of mixing equipment;
in step 132a, a gate position control signal is generated according to the first graph and the preset weight value within the preset discharging time.
In this embodiment, when the index parameter is the weight of the material in the mixing bin monitored in real time, the weight of the material is taken as a dependent variable, the running time of the mixing device is taken as an independent variable, and a first graph of the weight of the material and the running time of the mixing device is drawn;
it should be appreciated that when the material weight indicates a decrease in material in the mixing chamber, the first plot may then characterize the material weight as inversely related to the mixing device run time; when the material weight indicates that the material in the mixing bin is increasing, the first graph can then characterize that the material weight is positively correlated with the mixing device operating time; the first graph represents a tendency of the mixing apparatus to increase or decrease in weight;
further, in a preset discharging time of the mixing equipment, generating a gate position control signal when the gate of the mixing equipment performs discharging according to the first graph and the preset weight value, so as to precisely control the gate height of the mixing equipment during discharging, and further assist in enhancing the movement of the mixed materials to a discharging area and improving the working efficiency of the mixing equipment;
the preset discharging time can be set according to the viscosity or actual requirements of the mixed materials; the preset weight value is the discharging amount set according to the actual requirement during discharging.
In an optional implementation of the present invention, the step 14 may include:
and step 141a, controlling the distance when the gate is opened during the discharging operation of the mixing equipment according to the gate position control signal.
According to the embodiment, according to the gate position control signal, the gate opening distance, namely the gate opening height, of the mixing equipment during discharging operation after mixing is controlled within the preset discharging time, so that the gate height of the mixing equipment during discharging can be accurately controlled, the gate height of the mixing equipment is ensured to be a certain distance below the level height of the mixed materials, and further, when the gate position control signal is generated and the gate is triggered to be opened, a large amount of materials cannot enter a discharging area in an uncontrolled manner due to strong material flowability, and the influence on subsequent procedures caused by accumulation of large materials in the discharging area is avoided;
it should be noted that when the gate of the mixing device does not receive the gate position control signal, the gate is in a closed state, but not in a completely closed state, so that the height of the mixed gate is ensured to be a certain distance above the level of the mixed material, and the gate is not required to be completely closed in place, thus ensuring that the gate can quickly respond after the gate position control signal is generated, and further improving the working efficiency of the mixing device.
In an implementation example of the present invention, when the gate of the mixing device receives the gate position control signal, when the actual discharging time of the mixing device exceeds the preset discharging time, it is proved that the viscosity of the mixed material is higher and the fluidity is poor, at this time, the gate can be controlled to be further opened, the height distance between the material and the material is increased, the distance difference is automatically adjusted according to the first graph of the weight reduction of the mixing device, that is, the weight reduction trend of the mixing device is smaller than the set value, the distance difference between the gate and the material level is increased, the movement of the waste material to the discharging area is assisted to be enhanced, and the working efficiency of the mixing device during discharging is improved.
In an embodiment of the present invention, the mixing device may communicate with the pumping device at the back end thereof in real time, and the mixing device collects the pumping output and the pumping time of a single cycle of the pumping device in real time, and draws a trend chart of the pumping output and the pumping time;
further, according to the change trend graph, calculating and setting the single discharging amount of the mixing equipment, and ensuring that the mixed materials in the mixing bin of the mixing equipment can be completely pumped through a plurality of pumping circulation times, so as to avoid the risk that the mixed materials in the chute cannot be pumped away for a long time when the single discharging amount of the mixing equipment is too large, solid-liquid separation layering risk is generated, and high-pressure blockage of the pumping equipment is caused, thereby affecting the safe and smooth proceeding of subsequent procedures; or the single discharging amount of the mixing equipment is too small, the discharging frequency is increased, the gate switching times and the abrasion degree are increased, the discharging time is shortened, the discharging working efficiency of the mixing equipment is improved, and the service life of the gate is prolonged.
In an optional implementation of the present invention, when the index parameter is a torque of a stirring shaft of the mixing device and an operating pressure of a driver corresponding to the torque of the stirring shaft is in an increasing or decreasing state, the step 13 may include:
step 131b, obtaining a second graph of the operating pressure and the operating time of the mixing device;
step 132b, generating a stirring shaft rotating speed control signal according to the second graph.
In this embodiment, when the index parameter is the real-time monitored torque of the stirring shaft of the mixing device during the mixing operation, the torque of the stirring shaft corresponds to the operating pressure of the driver that drives the stirring shaft to rotate, that is, the operating pressure of the current driver may be directly obtained, the operating pressure is taken as a dependent variable, the operating time of the mixing device is taken as an independent variable, and a second graph of the operating pressure and the operating time of the mixing device is drawn;
the stirring shaft rotational speed control signal may include: when the second curve is in an ascending trend, the running pressure of the driver is gradually increased along with time, which indicates that the weight of materials in a mixing bin of the mixing equipment is continuously increased at the moment, and the mixing equipment is still continuously put in new materials to participate in the compatibility and mixing of the materials; generating a control signal for increasing the rotation speed of the stirring shaft according to the current continuous feeding state of the mixing equipment; when the second curve is gradually flattened, the feeding and mixing compatibility of the mixing equipment is finished, and a reduced stirring shaft rotating speed control signal is generated according to the current finishing state of the feeding and mixing compatibility of the mixing equipment;
further, the step 14 may include:
and step 141b, controlling the stirring shaft of the mixing equipment to run at a preset stirring speed according to the stirring shaft rotating speed control signal.
In this embodiment, according to the control signal for increasing the rotation speed of the stirring shaft, the stirring shaft is controlled to accelerate according to a preset stirring speed, so as to achieve the purpose of rapid stirring and mixing; or the control signal for reducing the rotation speed of the stirring shaft is used for controlling the stirring shaft to run at a reduced speed according to a preset stirring speed, and the mixed materials are maintained in a homogeneous state, and meanwhile, the energy consumption of the mixing equipment is reduced, so that the energy-saving effect is realized.
In an achievable embodiment of the invention, the mixing equipment can communicate with the crushing equipment at the front end of the mixing equipment in real time, the mixing equipment collects the running pressure and the crushing time of a cutter shaft driver which drives a cutter shaft to rotate in the crushing equipment in real time, and draws a change trend chart of the running pressure and the crushing time of the cutter shaft driver;
further, judging whether the front-end crushing equipment finishes the work of conveying materials into the mixing equipment according to the change trend graph; when the change trend chart shows that the crushing equipment is still in crushing work, the mixing equipment is required to continuously receive new materials for feeding, mixing and compatibility, and a control signal for increasing the rotation speed of the stirring shaft can be generated according to the current continuous feeding state of the mixing equipment so as to improve the working efficiency of the mixing equipment; when the change trend graph shows that the crushing operation of the crushing equipment is finished and the second graph is gradually flattened, the feeding and mixing compatibility of the mixing equipment is finished, and a reduced stirring shaft rotating speed control signal is generated according to the current finishing state of the feeding and mixing compatibility of the mixing equipment so as to reduce the energy consumption of the mixing equipment;
further, in the process of discharging the material by opening the gate of the mixing device, when the fact that the actual discharging time of the gate exceeds the preset discharging time is monitored, the fact that the mixed material in the mixing bin is sticky at the moment is indicated, and an accelerating stirring shaft rotating speed control signal can be generated at the moment so as to improve the rotating speed of the stirring shaft, assist in enhancing the movement of the mixed material to the discharging area and improve the working efficiency of the mixing device.
In an optional implementation of the present invention, when the index parameter is a temperature in the mixing bin and indicates that the temperature in the mixing bin is in an increasing or decreasing state, the step 13 may include:
step 131c, obtaining a third graph of the temperature in the mixing bin and the running time of the mixing equipment;
step 132c, generating a stirring shaft rotating speed control signal according to the third graph.
In this embodiment, when the index parameter is the temperature in the mixing bin monitored in real time, the temperature in the mixing bin is taken as a dependent variable, the operation time of the mixing device is taken as an independent variable, and a third graph of the temperature in the mixing bin and the operation time of the mixing device is drawn;
when the third curve is in an ascending trend, the reaction state of each material in the mixing bin is shown, a large amount of heat is released, the rotating speed of the stirring shaft is required to be controlled at the moment, so that safe mixing of the materials in the mixing bin can be ensured, and a speed-reducing stirring shaft rotating speed control signal is also generated at the moment, so that mixing operation of the mixing equipment is accurately controlled, safe operation of the equipment is ensured, and energy consumption of the mixing equipment is reduced.
Further, the step 14 may include:
and 141c, controlling the stirring shaft of the mixing equipment to run at a preset stirring speed according to the stirring shaft rotating speed control signal.
In this embodiment, according to the rotation speed control signal of the speed-reducing stirring shaft, the stirring shaft of the mixing device is controlled to perform speed-reducing operation according to a preset stirring speed;
preferably, different levels of alarm signals can be set according to a third graph of temperature and time, and further stirring shaft rotating speed control signals with different speeds can be correspondingly generated according to the different levels of alarm signals;
specific: when the slope delta T/delta T of the third curve is larger than 1, generating a first-stage alarm signal, generating a first rotation speed control signal of the stirring shaft according to the first-stage alarm signal, and further controlling the stirring shaft to rotate at a low speed according to the first rotation speed control signal of the stirring shaft;
when the slope delta T/delta T of the third curve is larger than 2, generating a second-level alarm signal, and generating a stirring shaft second rotating speed control signal according to the second-level alarm signal, and further controlling the stirring shaft to rotate at a low speed according to the stirring shaft second rotating speed control signal;
when the slope delta T/delta T of the third curve is larger than 3, indicating that the material is in a reaction state, and releasing a large amount of heat, generating a three-level alarm signal at the moment, and simultaneously generating a stirring shaft rotation stopping control signal according to the three-level alarm signal, and further controlling the stirring shaft to stop rotating according to the stirring shaft rotation stopping control signal;
through the alarm signals of different levels and the stirring shaft rotating speed control signals of different rotating speeds, the energy conservation and emission reduction of the mixing equipment are realized, and meanwhile, when chemical effects of reaction between different types of materials causing the internal temperature of the mixing equipment to rise are avoided, a certain buffer time is given when the chemical effects are within an acceptable range; meanwhile, the reaction time is prolonged by reducing the speed in the reaction process, so that the chemical effect generated by the reaction is slowed down, and the efficient, safe and reliable operation of the mixing equipment is ensured.
In an optional implementation of the present invention, when the operating pressure is within a preset pressure range, the step 13 may include:
step 131d, obtaining a correction coefficient of the running pressure and the preset pressure;
step 132d, generating a feeding control signal according to the correction coefficient;
and step 133d, controlling feeding and mixing operation of the mixing equipment according to the feeding control signal.
In this embodiment, the operation pressure of the driver for driving the stirring shaft to rotate is monitored and collected in real time by a preset pressure sensor, and the operation pressure is calculated by a calculation unitThe force reflects the actual pulping condition after the materials are mixed, and the pulping condition at the moment directly influences the discharging operation of the mixing equipment and the operation of subsequent equipment; by means of the real-time operating pressure MiX of the corresponding drive of the mixing shaft of the mixing device during operation P Monitoring and generating a correction coefficient of the real-time operation pressure and a preset pressure value; preferably, an alarm signal and a feeding control signal can be generated according to the correction coefficient, and then feeding of the mixing equipment is controlled according to the feeding control signal, and mixing operation is performed, so that actual mixing pulping effect of material compatibility is monitored, mixing compatibility pulping effect of the mixing equipment is optimized, mixing compatibility efficiency is improved, and normal operation of back-end equipment is facilitated;
the correction coefficient is the ratio of the real-time operating pressure to the preset pressure, and when the correction coefficient is 1, the real-time operating pressure MiX P The actual compatibility effect after the stirring shaft is used for stirring and mixing materials at the moment is equal to the preset pressure value, so that the follow-up pumping and conveying links are not affected by serious high-pressure blocking, and the follow-up discharging and pumping links can be continuously fed;
when the correction factor is much greater than 1, and is the real-time operating pressure MiX P Greater than or equal to a first preset pressure value MiX Pmax The actual form and the expected form of the mixed materials are not consistent at the moment, for example, packaging waste liquid is solidified into crystalline salt through long-time storage of the waste materials, so that the content of the solid materials of the batch of materials is high, the current mixed materials are required to be subjected to pulping state adjustment, at the moment, a dry warning signal of the mixed materials is triggered, meanwhile, a feeding control signal of the liquid materials is generated, the liquid materials are fed into a waste liquid conveying pipeline of the mixing equipment according to the feeding control signal of the liquid materials, the pressure of a stirring shaft is relieved, and the pulping effect of the mixed materials is optimized; simultaneously, the liquid material is put into the stirring shaft, the quantity of the liquid material is recorded, and the correction coefficient of the operation pressure of the driver for driving the stirring shaft to rotate after the liquid material is put into the stirring shaft is monitored in real time;
when saidThe correction coefficient is much smaller than 1, and the real-time operating pressure MiX P Less than or equal to a second preset pressure value MiX Pmin The method is characterized in that the actual compatibility effect is poor, a large amount of liquid is likely to be generated due to chemical reaction between different wastes, the mixed wastes are likely to generate solid-liquid layering phenomenon, the current mixed materials are required to be subjected to slurry state adjustment, a mixed material dilution warning signal is triggered at the moment, meanwhile, a feeding control signal of solid materials is generated, and a sludge conveying pipeline of the mixing equipment is controlled to throw in the solid materials according to the feeding control signal of the solid materials so as to optimize the slurry mixing effect; simultaneously, the solid material is put into the device, the amount of the solid material is recorded, and the correction coefficient of the running pressure of the solid material is monitored in real time;
when the correction coefficient is close to 1, the second preset pressure value MiX Pmin Less than the real-time operating pressure MiX P And the real-time operating pressure is less than the first preset pressure value MiX Pmax The actual compatibility effect does not generate serious high-pressure blocking influence on the subsequent pumping and conveying links at the moment, so that the feeding and mixing operation of the mixing equipment can be continued and the subsequent processing links can be continued;
when the correction coefficient is close to 1, monitoring the correction coefficient and the real-time operation pressure according to the operation of the mixing equipment; when the real-time operating pressure is greater than or equal to a third preset pressure value MiX Pg1 And is less than or equal to a fourth preset pressure value MiX Pg2 And when the final mixed materials are compatible, the pulping effect is optimal, namely, the correction coefficient of the real-time operating pressure at the stage is 1, and the correction coefficient is the optimal correction coefficient. When the real-time operating pressure is greater than the third preset pressure value MiX Pg1 When the correction coefficient= MiX P /MiX Pg1 The real-time operating pressure is less than or equal to the fourth preset pressure value MiX Pg2 When the correction coefficient mx= MiX P /MiX Pg2 Simultaneously generating a correction coefficient trend curve, when the correction coefficient trend curve is delta MX/delta t>0, indicating the drive of the stirring shaftThe running pressure of the device is increased, and dry sludge is added in the mixture; when DeltaMX/Deltat of the correction coefficient trend curve<0, the running pressure is reduced, and the waste liquid is increased in the mixture;
in a specific implementation example, when the third preset pressure value MiX Pg1 Set to 40, the fourth preset pressure value MiX Pg2 When the correction coefficient trend curve is set to be 60, the generated correction coefficient trend curve is shown in fig. 2; if the second preset pressure value MiX is set Pmin 35, the first preset pressure value MiX Pmax When the value is 120, namely, the effective value of the correction coefficient is between 0.875 and 2, the correction coefficient can be further corrected and optimized according to feedback data of a subsequent processing link;
the correction coefficient when the dry or thin warning signal of the mixed material is triggered and the correction coefficient after the correction of the mixed material is finished are captured, a trend curve of the correction coefficient is formed, the running pressure is monitored in real time, the mixing condition of the mixed material is timely adjusted, the mixing material forming effect of the mixed material of the mixing equipment is optimized, the mixing working efficiency of the mixing equipment is improved, the first preset pressure value, the second preset pressure value, the third preset pressure value and the fourth preset pressure value can be set according to the actual condition, and the second preset pressure value MiX Pmin < said third preset pressure value MiX Pg1 < the fourth preset pressure value MiX Pg2 < said first preset pressure value MiXPmax.
In an optional implementation of the present invention, based on the steps 131d-133d, the method may further include:
and step 134d, generating a compatibility list of the mixing equipment during feeding and mixing according to the correction coefficient and the feeding control signal.
In this embodiment, the compatibility list includes: the mixing equipment controls the type of the input materials and the quality of the input materials according to the feeding control signals; real-time monitoring is carried out on the real-time operation pressure of the corresponding driver of the stirring shaft of the mixing equipment during rotation, and a compatibility list of mixed materials of the mixing equipment is adjusted according to a monitoring result so as to optimize a pulping effect after compatibility and mixing, improve the mixing work efficiency of the mixing equipment and facilitate the operation and the operation of rear-end equipment of the mixing equipment.
As shown in fig. 3, an embodiment of the present invention further provides a control apparatus 30 of a mixing device, including:
an obtaining module 31, configured to obtain an index parameter when the mixing device performs a mixing operation;
the processing module 32 is configured to determine a current material state in the mixing bin of the mixing device according to the index parameter, where the index parameter includes a weight of a material in the mixing bin, a torque of a stirring shaft of the mixing device, and a temperature in the mixing bin; generating a control signal according to the material state in the mixing bin of the mixing equipment;
a control module 33 for controlling the operation state of the mixing device according to the control signal.
Optionally, when the index parameter is a weight of the material in the mixing bin and indicates that the material in the mixing bin is in an increased or decreased state, the processing module 32 is configured to generate a control signal according to a state of the material in the mixing bin of the mixing device, and includes:
acquiring a first graph of the weight of materials in the mixing bin and the running time of mixing equipment;
and generating a gate position control signal according to the first graph and a preset weight value in a preset discharging time.
Optionally, the control module 33 is configured to control an operation state of the mixing device according to the control signal, and includes:
and controlling the opening or closing distance of the gate during discharging operation of the mixing equipment according to the gate position control signal.
Optionally, when the index parameter is a torque of a stirring shaft of the mixing device and an operation pressure of a driver corresponding to the torque of the stirring shaft is in an increasing or decreasing state, the processing module 32 is configured to generate a control signal according to a state of a material in a mixing bin of the mixing device, where the control signal includes:
acquiring a second graph of the operating pressure of the stirring shaft and the operating time of the mixing equipment;
and generating a stirring shaft rotating speed control signal according to the second graph.
Optionally, when the index parameter is a temperature in the mixing bin and indicates that the temperature in the mixing bin is in an increasing or decreasing state, the processing module is configured to generate a control signal according to a state of a material in the mixing bin of the mixing device, and includes:
acquiring a third graph of the temperature in the mixing bin and the running time of the mixing equipment;
and generating a stirring shaft rotating speed control signal according to the third graph.
Optionally, the control module 33 is configured to control an operation state of the mixing device according to the control signal, and includes:
and controlling the stirring shaft of the mixing equipment to run at a preset stirring speed according to the stirring shaft rotating speed control signal.
Optionally, when the operating pressure is within a preset pressure range, the processing module 32 is further configured to:
acquiring a correction coefficient of the running pressure and a preset pressure;
generating a feeding control signal according to the correction coefficient;
and controlling feeding and mixing operation of the mixing equipment according to the feeding control signal.
Optionally, the processing module 32 is further configured to:
and generating a compatibility list of the mixing equipment during feeding and mixing according to the correction coefficient and the feeding control signal.
It should be noted that, the device is a device corresponding to the control method of the above-mentioned mixing device, and all implementation manners in the above-mentioned method embodiment are applicable to the embodiment of the device, so that the same technical effects can be achieved.
The embodiment of the invention also provides a control system of the mixing equipment, which comprises the following components:
a mixing device having a mixing chamber;
a driver for driving the mixing device to operate;
the sensor is electrically connected with the driver and is arranged on the driver and used for detecting index parameters when the driver drives the mixing equipment to operate;
the processor is in communication connection with the driver and is used for determining the current material state in the mixing bin of the mixing equipment according to the index parameters; generating a control signal according to the material state in the mixing bin of the mixing equipment;
and the controller is in communication connection with the processor and is used for controlling the running state of the mixing equipment according to the control signal.
In this embodiment, the driver is electrically connected to the stirring shaft of the mixing device, and the mixing operation of the mixing device is controlled by driving the stirring shaft to operate; the driver can be hydraulically driven or motor driven;
one end of the sensor is electrically connected with an output line of the driver, and the other end of the sensor is in communication connection with the processor and is used for monitoring index parameters generated when the driver drives the mixing equipment to operate in real time and transmitting the index parameters to the processor; the index parameters further reflect the material state in a mixing bin of the mixing equipment; the sensor may include a torque sensor, a temperature sensor, a weight sensor;
the index parameters of the driver are monitored in real time through the sensor, and are transmitted to the processor for processing, and the corresponding control signals are automatically output after logic operation and are transmitted to the controller; the controller accurately controls the operation of the mixing equipment according to the corresponding control signals, so that the energy consumption of the mixing equipment is reduced, and the working efficiency of the mixing equipment is improved;
in this embodiment, the processor may store the received index parameter and the corresponding control signal, perform iterative storage operation based on a deep learning algorithm, increase automatic logic calculation and judgment, and strengthen automatic output of control signals for rotation and stop of the stirring shaft of the mixing device, so as to realize automatic judgment, and reduce costs of manual operation and judgment.
While the foregoing is directed to the preferred embodiments of the present invention, it will be appreciated by those skilled in the art that various modifications and adaptations can be made without departing from the principles of the present invention, and such modifications and adaptations are intended to be comprehended within the scope of the present invention.
Claims (10)
1. A control method of a mixing apparatus, characterized by comprising:
acquiring index parameters when the mixing equipment mixes materials;
determining the current material state in a mixing bin of the mixing equipment according to the index parameters, wherein the index parameters comprise the weight of the material in the mixing bin, the torque of a stirring shaft of the mixing equipment and the temperature in the mixing bin;
generating a control signal according to the material state in the mixing bin of the mixing equipment;
and controlling the running state of the mixing equipment according to the control signal.
2. The control method of a mixing apparatus according to claim 1, wherein when the index parameter is a weight of a material in a mixing bin and indicates that the material in the mixing bin is in an increased or decreased state, generating a control signal according to a state of the material in the mixing bin of the mixing apparatus, comprises:
acquiring a first graph of the weight of materials in the mixing bin and the running time of mixing equipment;
and generating a gate position control signal according to the first graph and a preset weight value in a preset discharging time.
3. The control method of a mixing apparatus according to claim 2, wherein controlling an operation state of the mixing apparatus according to the control signal includes:
and controlling the opening or closing distance of the gate during discharging operation of the mixing equipment according to the gate position control signal.
4. The control method of a mixing apparatus according to claim 1, wherein when the index parameter is a torque of a stirring shaft of the mixing apparatus and an operation pressure of a driver corresponding to the torque of the stirring shaft is in an increasing or decreasing state, generating a control signal according to a state of a material in a mixing bin of the mixing apparatus, comprises:
acquiring a second graph of the operating pressure and the operating time of the mixing device;
and generating a stirring shaft rotating speed control signal according to the second graph.
5. The control method of a mixing apparatus according to claim 1, wherein generating a control signal according to a state of a material in a mixing chamber of the mixing apparatus when the index parameter is a temperature in the mixing chamber and indicates that the temperature in the mixing chamber is in an increasing or decreasing state, comprises:
acquiring a third graph of the temperature in the mixing bin and the running time of the mixing equipment;
and generating a stirring shaft rotating speed control signal according to the third graph.
6. The control method of a mixing apparatus according to claim 4 or 5, characterized by controlling an operation state of the mixing apparatus according to the control signal, comprising:
and controlling the stirring shaft of the mixing equipment to run at a preset stirring speed according to the stirring shaft rotating speed control signal.
7. The method of controlling a mixing device of claim 4, further comprising, when the operating pressure is within a predetermined pressure range:
acquiring a correction coefficient of the running pressure and a preset pressure;
generating a feeding control signal according to the correction coefficient;
and controlling feeding and mixing operation of the mixing equipment according to the feeding control signal.
8. The control method of the mixing apparatus according to claim 7, characterized by further comprising:
and generating a compatibility list of the mixing equipment during feeding and mixing according to the correction coefficient and the feeding control signal.
9. A control device of a mixing apparatus, characterized by comprising:
the acquisition module is used for acquiring index parameters when the mixing equipment performs mixing operation;
the processing module is used for determining the current material state in the mixing bin of the mixing device according to the index parameters, wherein the index parameters comprise the weight of the material in the mixing bin, the torque of the stirring shaft of the mixing device and the temperature in the mixing bin; generating a control signal according to the material state in the mixing bin of the mixing equipment;
and the control module is used for controlling the running state of the mixing equipment according to the control signal.
10. A control system of a mixing apparatus, comprising:
a mixing device having a mixing chamber;
a driver for driving the mixing device to operate;
the sensor is electrically connected with the driver and is arranged on the driver and used for detecting index parameters when the driver drives the mixing equipment to operate;
the processor is in communication connection with the driver and is used for determining the current material state in the mixing bin of the mixing equipment according to the index parameters; generating a control signal according to the material state in the mixing bin of the mixing equipment;
and the controller is in communication connection with the processor and is used for controlling the running state of the mixing equipment according to the control signal.
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Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2333029A1 (en) * | 1998-05-22 | 1999-12-02 | Miroslav Sedlacek | Hydraulic motor |
| CN101446191A (en) * | 2008-11-17 | 2009-06-03 | 文必用 | Drilling well control parameter intelligent monitoring system |
| CN106907260A (en) * | 2015-12-22 | 2017-06-30 | 马涅蒂-马瑞利公司 | Method for controlling fuel injection in motor vehicles explosive motor |
| WO2018133807A1 (en) * | 2017-01-20 | 2018-07-26 | 比亚迪股份有限公司 | Hybrid electric vehicle and active vibration damping control method and device therefor |
| CN109186272A (en) * | 2018-10-18 | 2019-01-11 | 中冶北方（大连）工程技术有限公司 | Sintered compound feed bin level control system and method |
| US20190277129A1 (en) * | 2018-03-12 | 2019-09-12 | Halliburton Energy Services, Inc. | Marking the start of a wellbore flush volume |
| CN114432951A (en) * | 2021-12-31 | 2022-05-06 | 三一汽车制造有限公司 | Unloading control method and device and stirring equipment |
| CN114803382A (en) * | 2022-04-28 | 2022-07-29 | 天津美腾科技股份有限公司 | Conveying control method, system, device, conveyor equipment and readable storage medium |
| CN115253871A (en) * | 2022-07-14 | 2022-11-01 | 浙江古茗科技有限公司 | Automatic stirring device and control method thereof |
-
2023
- 2023-07-06 CN CN202310827684.1A patent/CN116736745B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2333029A1 (en) * | 1998-05-22 | 1999-12-02 | Miroslav Sedlacek | Hydraulic motor |
| CN101446191A (en) * | 2008-11-17 | 2009-06-03 | 文必用 | Drilling well control parameter intelligent monitoring system |
| CN106907260A (en) * | 2015-12-22 | 2017-06-30 | 马涅蒂-马瑞利公司 | Method for controlling fuel injection in motor vehicles explosive motor |
| WO2018133807A1 (en) * | 2017-01-20 | 2018-07-26 | 比亚迪股份有限公司 | Hybrid electric vehicle and active vibration damping control method and device therefor |
| US20190277129A1 (en) * | 2018-03-12 | 2019-09-12 | Halliburton Energy Services, Inc. | Marking the start of a wellbore flush volume |
| CN109186272A (en) * | 2018-10-18 | 2019-01-11 | 中冶北方（大连）工程技术有限公司 | Sintered compound feed bin level control system and method |
| CN114432951A (en) * | 2021-12-31 | 2022-05-06 | 三一汽车制造有限公司 | Unloading control method and device and stirring equipment |
| CN114803382A (en) * | 2022-04-28 | 2022-07-29 | 天津美腾科技股份有限公司 | Conveying control method, system, device, conveyor equipment and readable storage medium |
| CN115253871A (en) * | 2022-07-14 | 2022-11-01 | 浙江古茗科技有限公司 | Automatic stirring device and control method thereof |
Non-Patent Citations (2)
| Title |
|---|
| MARIWAN MIRHAJ MOHAMEDSALIH: "《Effect of type, amount and configuration of reinforcement in HSC box-girders reinforced with BFRP bars and steel stirrups under torsion-shear-bending》", 《AIN SHAMS ENGINEERING JOURNAL》, pages 101787 * |
| 李慧莱: "《高扭矩密度仿人机器人驱动单元研究》", 《机械工程学报》, no. 18, pages 192 * |
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