A High-Efficiency Ceramic Filter Cluster Scheduling System and Method

Abstract

This invention discloses a highly efficient ceramic filter cluster scheduling system and method, including a control system on each filter for monitoring its processing capacity and slurry characteristics, and a scheduling system on the host machine. The control systems of multiple filters are connected to the scheduling system on the host machine in a star topology. The filter machine control system is responsible for collecting information from individual units and controlling their automated operation, transmitting this information to the scheduling system on the host machine. The scheduling system on the host machine comprehensively analyzes the collected filter operating status information and schedules the number of filters required to participate in production based on equipment characteristics, combined with process and production needs. This invention analyzes the required processing capacity per unit time by calculating the comprehensive processing capacity of the ceramic filters based on slurry characteristics such as concentration and particle size, and the processing capacity of a single ceramic filter, matching the required production capacity to achieve a reasonable allocation of the number of ceramic filters in operation.

Description

Technical Field

[0001] This invention relates to the field of slurry solid-liquid separation control technology, and in particular to a highly efficient ceramic filter cluster scheduling system and method. Background Technology

[0002] Currently, the construction of slurry pipeline transportation has reached a considerable scale, and the pipeline transportation systems are equipped with relatively complete SCADA systems to ensure automated control of pipeline transportation. Solid material pipeline transportation is divided according to process sections: ore solids are ground into slurry, transported to their destination via long-distance pipelines, and then the slurry is dewatered (i.e., solid-liquid separation) and stored in silos or storage yards. Dewatering is the outlet of the slurry pipeline transportation system and plays a crucial role in the process flow. Changes in dewatering capacity and efficiency significantly affect the pipeline transportation capacity, creating constraints on pipeline transportation; therefore, a solid-liquid separation scheduling system is required.

[0003] Currently, most solid-liquid separation control in dewatering workshops at the outlet of slurry pipelines relies on local operation, with some using remote centralized control. However, the level of automation is low. Even those systems that achieve some automation often only involve a single ceramic filter, requiring operator intervention during production. Such systems cannot meet the needs of modern enterprises for efficient and low-cost automated production, and they also hinder the improvement of pipeline transportation capacity, failing to fully utilize the advantages of pipeline transportation. The main equipment for solid-liquid separation is the ceramic filter, including bag filters, ceramic filters, and filter presses, typically operating in multiple units simultaneously. The electrical control systems for ceramic filters are generally designed to meet basic on-site operation requirements, resulting in low levels of automation. This drawback limits the equipment's production efficiency and, overall, restricts the automation and intelligence of the dewatering workshop. Summary of the Invention

[0004] The purpose of this invention is to address the shortcomings of existing technologies by proposing a scheduling and control method for solid-liquid separation. This method involves networking the individual control systems of multiple ceramic filters and installing a self-developed node control system. The scheduling system running on the host machine analyzes the required processing capacity per unit time based on the actual amount of ore transported through pipelines, the dewatering workshop's outlet conveying capacity, and the slurry characteristics (such as concentration and particle size), as well as the processing capacity of a single ceramic filter. By calculating the comprehensive processing capacity of the ceramic filters, the required processing capacity per unit time is analyzed, matching the production capacity target and achieving a reasonable allocation of the number of ceramic filters in operation.

[0005] The technical solution of the present invention is as follows: This invention discloses a high-efficiency ceramic filter cluster scheduling system, including a control system on the filter for monitoring the filter's processing capacity and slurry characteristics, and a scheduling system on the host machine. The control systems of multiple filters are connected to the scheduling system on the host machine in a star topology. The control systems of the filters are responsible for collecting information on the individual sets of equipment and controlling the process-oriented automatic operation, and transmitting the information to the scheduling system on the host machine. The scheduling system on the host machine comprehensively analyzes the collected filter-related operating status information and schedules the number of filters that need to participate in production based on equipment characteristics, combined with process and production requirements.

[0006] Furthermore, the control system of the filter includes a stand-alone control system and a canned stand-alone automatic control software, which has stand-alone multi-mode automated operation control function, provides open network communication and data interface, and connects to a centralized scheduling and control system.

[0007] Furthermore, the control system of the filter machine specifically includes a controller, an I / O control board, a communication board and a human-machine panel, a signal acquisition sensor, a drive controller with speed adjustment function and a signal output indicator, and a voice alarm device; the signal acquisition sensor is installed at the detection point, all input signals are connected to the input board of the I / O control board and pre-allocated channels, and the control adjustment output signal is connected to the drive controller, the signal output indicator and the voice alarm device.

[0008] Furthermore, the filter is equipped with a switch for switching in and out. Switching in indicates that the equipment is in good condition and can participate in scheduling, while switching out indicates that the equipment is not ready.

[0009] Furthermore, the scheduling system on the host is equipped with a monitoring operation station for running the scheduling system screen, which mainly includes necessary parameter setting sub-screens, process overview main screen, solid-liquid separation workshop sub-screens, and single ceramic filter monitoring screens.

[0010] Furthermore, the scheduling system can simultaneously meet the continuous, synchronous, efficient, and automatic operation of 14 sets of ceramic filter machines.

[0011] Furthermore, the filter is equipped with a lifting cleaning device that is connected to the control system.

[0012] This invention also discloses an efficient method for scheduling ceramic filter clusters, comprising the following specific steps: Step 1: Equipment status query and correction, collect and gather the status of all ceramic filters in the solid-liquid separation workshop; Step 2: Grouping and sorting ceramic filters. Select the filters to participate in the control, identify them by number, and store them in the scheduling system. The scheduling system distinguishes between odd and even numbers for the filter numbers participating in the control. Step 3: Execute scheduling. Record the demining working time of the machine and the cleaning running time of the machine in the cleaning stage. The scheduling system performs comprehensive analysis, calculation and judgment based on the above information, generates scheduling instructions and issues them to the corresponding numbered machines for execution. Step 4: Cycle or End. After the filter finishes running, it will be cleaned. After cleaning, it will automatically enter standby mode and be handed over to the scheduling system for scheduling, waiting for the next scheduling instruction.

[0013] Furthermore, in Step 1, it is determined whether the filter is in a remote or connected state, and whether it has no abnormalities or fault alarms. Only if all of the above conditions are met can it participate in scheduling. If any of the above conditions are not met, it needs to be handled and eliminated on-site. If the selector switch is not in the required position, it should be switched to the required position. If the equipment has an abnormality or fault, it needs to be eliminated until the conditions are met. Otherwise, the equipment is removed and will not participate in scheduling. Finally, the control of the intelligent slave station is switched to "automatic" mode. At this time, the ceramic filter will meet the scheduling requirements and wait for scheduling instructions.

[0014] Furthermore, in Step 3, scheduling is divided into two modes: One method is startup scheduling, where the system determines the required number of equipment units based on the flow rate and concentration of the slurry delivered from the concentrate pipeline. The slurry source has two directions: one is direct delivery from the concentrate pipeline, which can be directly supplied to the distribution tank at the front end of the ceramic filter. The system determines the required number of equipment units based on the ore source and schedules the slurry according to the current status of the equipment. The other is existing slurry, which is temporarily stored in the thickener. The concentration of the slurry needs to be adjusted first, with low-concentration slurry being increased and high-concentration slurry being decreased, before being delivered to the distribution tank at the front end of the ceramic filter, where the system schedules the slurry. Another scenario is during operation, when the tailings of the batch-delivered slurry are about to arrive or have already arrived, causing a decrease in flow rate. At this time, the slurry concentration in the operating ceramic filters decreases, and the demineralization efficiency decreases. To ensure equipment efficiency and energy saving, it is necessary to shut down some of the operating ceramic filters. However, if the continuous operation has not reached 8 hours, the system will make a comprehensive judgment and prioritize the filters with the longest current operating time for cleaning. After cleaning, the filters will automatically enter standby mode, waiting for subsequent instructions.

[0015] Compared with existing technologies, the advantages of this invention are: 1. This invention has been successfully tested and proven effective. The system accurately and intuitively reflects the real-time operation of the ceramic filter. Users can visually understand the operation process, status, relevant early warnings and forecasts, and even fault alarms of the ceramic filter through a control panel. This allows for a comprehensive assessment of the overall operation of the ceramic filter, providing effective early warnings and forecasts. In severe cases, the system can automatically trigger a shutdown command to stop the equipment, protecting it and prompting maintenance personnel to perform targeted inspections and maintenance.

[0016] 2. This invention solves the problems of low automation level in the control system of iron concentrate slurry dewatering workshop, cumbersome operation of ceramic filter equipment, easy error, and excessively long process execution time.

[0017] 3. This invention monitors key parameters (such as demineralization time and cleaning time) and monitoring data (such as vacuum pressure and the operating current of the stirring motor frequency converter) that affect the operation of the equipment, and issues early warnings to effectively protect the equipment. It can also guide maintenance personnel to maintain or replace relevant components, thereby improving the automation level of the ceramic filter, extending its service life, and minimizing safety hazards.

[0018] 4. The use of the system of the present invention greatly reduces the probability of misoperation caused by human factors, and avoids situations where human misoperation causes equipment damage or delays in operation, affecting production.

[0019] 5. The system of the present invention improves the automation level of the solid-liquid separation system in the dehydration workshop, realizes rational automatic scheduling among ceramic filter units, and improves the operating efficiency of ceramic filters.

[0020] 6. After using the system of this invention, the problem of continuous automated operation and control of ceramic filter machines is solved, the replacement cycle of ceramic filter plates is accurately predicted, the service life of ceramic filter plates is guaranteed, and the cost of using and maintaining them is reduced. Attached Figure Description

[0021] Figure 1 This is a schematic diagram of the overall process of the present invention; Figure 2 This is a schematic diagram of the layout structure of the ceramic filter in the system of the present invention; Figure 3 This is a schematic diagram of the system topology of the present invention; Figure 4 This is a schematic diagram of the system operation mechanism of the present invention. Detailed Implementation

[0022] It should be noted that relational terms such as "first" and "second" are used merely to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such a process, method, article, or apparatus. Without further limitations, an element defined by the phrase "comprising one..." does not exclude the presence of other identical elements in the process, method, article, or apparatus that includes said element.

[0023] The technical solution of the present invention will be further described in detail below with reference to the embodiments.

[0024] like Figure 2 The ceramic filters in the workshop of this invention are arranged in two symmetrical rows. The feeding belt passes through the lower middle layer between the two rows of ceramic filters. According to the process flow, the ceramic filters can be roughly divided into solid-liquid separation control and combined cleaning control. Due to its own characteristics, combined cleaning is required every 8 hours of continuous demining. Only after the cleaning is completed can it participate in demining again.

[0025] like Figure 1 As shown, this invention adopts a master-slave distributed architecture, using the TCP / IP protocol and a star topology for communication. This ensures fast connection and guarantees that the system's operation is not affected even if a node fails. The control system of the ceramic filter acts as an intelligent slave station, responsible for information collection and automated process control of the single-unit equipment. The master control system, as the core of the solid-liquid separation scheduling system, is primarily responsible for collecting multiple data messages transmitted from the slave stations, processing and analyzing the information, and then issuing instructions to the slave stations. The slave stations are responsible for executing these instructions to achieve efficient, smooth, and reliable operation of the entire scheduling process.

[0026] The individual control systems of multiple ceramic filter presses are networked, and a self-developed node control system is installed. A scheduling system running on the main unit then analyzes the required processing capacity per unit time based on the actual ore volume transported through pipelines and the dewatering workshop's outlet conveying capacity, as well as the slurry characteristics such as concentration and particle size, and the processing capacity of a single ceramic filter press. This comprehensive processing capacity of the ceramic filter presses is calculated to match the required production capacity and achieve a reasonable allocation of the number of ceramic filter presses in operation. During the process, it is crucial to control the moisture content of the dry ore (the dewatered filter cake, being dry ore, still contains a small amount of moisture) to maintain a dynamic balance.

[0027] The control system of the ceramic filter includes a stand-alone control system and a packaged stand-alone automatic control software. It features multi-mode automated operation control, provides open network communication and data interfaces, and connects to a centralized scheduling control system. Specifically, the control system includes a controller, I / O control boards, communication boards, a human-machine interface panel, signal acquisition sensors, a drive controller with speed adjustment function, a signal output indicator, and a voice alarm device. Signal acquisition sensors are installed at detection points. All input signals are connected to the input board of the I / O control board and pre-allocated channels. Control and adjustment output signals are connected to the drive controller, signal output indicator, and voice alarm device. The ceramic filter is equipped with a switch for switching in and out. Switching in indicates that the equipment is in good condition and ready for scheduling, while switching out indicates that the equipment is not ready. The main unit's scheduling system is equipped with a monitoring station for running the scheduling system interface. The interface mainly consists of: a necessary parameter setting sub-screen, a main process diagram screen, a solid-liquid separation workshop (all ceramic filters) sub-screen, and a pop-up sub-screen (monitoring screen for a single ceramic filter). The scheduling system monitors all ceramic filters throughout the process, classifying them into available and unavailable categories, selected by the in / out selection switch on the filter control cabinet. Further filtering is done based on equipment malfunctions or / and emergency stops to identify available filters for scheduling. The system determines the number of ceramic filters to be deployed based on the slurry flow rate transported through the pipeline and the processing capacity of a single ceramic filter, achieving a dynamic balance between the filter's demineralization capacity and the amount of ore transported through the pipeline. The scheduling system can simultaneously support the continuous, synchronous, efficient, and automatic operation of 14 ceramic filters. Each ceramic filter is equipped with a lifting cleaning device connected to the control system.

[0028] The ceramic filter has a single-unit multi-mode automated operation control function. The single-unit system provides an open network communication and data interface to connect to a centralized scheduling and control system.

[0029] like Figure 4 As shown, based on the operating mechanism of the process and equipment (such as slurry input flow rate, single-unit capacity of ceramic filter, filtration coefficient, and moisture requirements of the produced ore), a reasonable scheduling algorithm is studied. The model is extracted by analyzing and processing the three links of "input → production → output". The "production" link is calculated and determined by analyzing the "input" variables, and the "production" link is regulated by the "output" to study the stable and continuous production control requirements, analyze how to improve the use and operation efficiency of ceramic filter, and reasonably balance the service life of the equipment and the service life of the consumable parts. The formula for calculating the number of sets of equipment to be put into operation is based on the incoming ore flow rate. The number of ceramic filter sets required is calculated. The demineralization capacity of a single ceramic filter is determined by the filtration coefficient, the area of ​​the ceramic filter plate, and the attenuation coefficient. The process is repeated in batches: after 10 to 12 cycles, the filtration coefficient and demineralization capacity attenuation coefficient of the ceramic filter in each cycle are converted.

[0030] The system sorts the ceramic filter machines by their cumulative usage time, using an upward sorting method. The machines with shorter usage time are ranked higher and have priority in scheduling. The required number of ceramic filter machines to be put into operation is determined by their numbers from front to back until the required number of machines is collected.

[0031] like Figure 1 As shown, this invention discloses an efficient method for scheduling a cluster of ceramic filters, which mainly includes four stages: equipment status query and correction; ceramic filter grouping and sorting; execution scheduling; and looping or termination.

[0032] Equipment Status Inquiry and Correction: As a key device for solid-liquid separation scheduling and the foundation of the entire system, the ceramic filter must first have its status collected in the solid-liquid separation workshop. This includes checking if it is in remote or connected mode, and if it has no abnormalities or fault alarms. Only if all of these conditions are met can it participate in scheduling. If any of these conditions are not met, it is considered a failure and requires on-site handling and elimination. If the selector switch is not in the required position, it should be switched to the required position. If the equipment has an abnormality or fault, it needs to be eliminated until the conditions are met. Otherwise, the equipment is removed from scheduling. Then, the intelligent slave station's control is switched to "automatic" mode. At this point, the ceramic filter will meet the scheduling requirements and await scheduling instructions.

[0033] Ceramic filter grouping and sequencing: Select the machines to participate in the control (identified by number and stored in the system). In addition to sequential numbering, the system also distinguishes between odd and even numbers for each machine. This step is primarily to ensure that the dewatered dry ore (filter cake with approximately 10% moisture content) received by the feed conveyor maintains belt tension balance, preventing disruption to normal conveyor operation. A self-check of the number of odd and even numbered machines is conducted. For effective scheduling, at least one machine with both odd and even numbers (a total of two machines) must be present, and the difference between the odd and even numbers must not exceed one.

[0034] Execution Scheduling: Based on the query results, the system understands the machine status and prioritizes the machines. Two key factors are the machine's demineralization runtime and the cleaning runtime of machines in the cleaning phase. First, the demineralization runtime is compared, and the machines are ranked from smallest to largest. To ensure a balanced lifespan, machines with longer demineralization runtimes have priority in the next scheduling iteration. Based on this information, a comprehensive analysis, calculation, and judgment are performed to generate scheduling instructions and issue them to the corresponding numbered machines for execution. The specific machine number is used to determine the number of ceramic filter machines participating in production.

[0035] The scheduling modes are divided into two scenarios. One is startup scheduling, where the system determines the required number of equipment units based on the flow rate and concentration of the slurry delivered from the concentrate pipeline. The slurry source has two directions: one is direct delivery from the concentrate pipeline, ensuring a stable and guaranteed concentration, which can be directly supplied to the distribution tank at the front end of the ceramic filter. The system determines the required number of equipment units based on the ore source and the current status of the equipment for scheduling. The other scenario is during operation, when the tail end of a batch of delivered slurry is about to arrive or has already arrived, causing a decrease in flow rate. At this time, the slurry concentration in the operating ceramic filters decreases, reducing demineralization efficiency. To ensure equipment efficiency and energy saving, some operating ceramic filters need to be shut down. However, if continuous operation has not reached 8 hours, the system will comprehensively analyze the situation and prioritize filters based on the duration of this demineralization cycle. Filters with longer demineralization cycles will be put into cleaning first. After cleaning, the filters will automatically enter standby mode, awaiting subsequent instructions. The third scenario involves existing slurry, temporarily stored in the thickener. The slurry concentration needs to be adjusted first (low-concentration slurry is increased, and high-concentration slurry is decreased) before being delivered to the distribution tank at the front end of the ceramic filter, where the system will schedule the slurry.

[0036] During this stage, auxiliary equipment needs to be started—the air compressor (to ensure that the pneumatic valves respond promptly when the ceramic filter is working), and the water pump needs to be started in a timely manner to maintain pressure and supply water, ensuring the cleaning of the ceramic filter with clean water. The timely start and stop of the chemical pump ensures a sufficient supply and safe operation of the cleaning agent (nitric acid of a certain concentration) during the cleaning process of the ceramic filter (the agent is a strong acid and is corrosive).

[0037] Cycle or End: After the ceramic filter finishes cleaning, it automatically enters standby mode, waiting for scheduling instructions to be handed over to the scheduling system.

[0038] Scheduling mechanism: Machines with long running times have priority, and production operations are met with the fewest possible machines.

[0039] The purpose of the scheduling is to utilize ceramic filters rationally and efficiently. Ceramic filter plates, as high-value consumable parts of ceramic filters, need to be replaced based on usage time. Through the scheduling system, the efficiency of ceramic filter plates is maximized throughout their life cycle, achieving optimal cost-effectiveness with the lowest possible energy consumption and the fewest number of ceramic filters in operation. During the scheduling process, machines with longer dewatering times are given priority.

[0040] The specific embodiments described in this application are quite detailed, but they should not be construed as limiting the scope of protection of this application. It should be noted that those skilled in the art can make various modifications and improvements without departing from the concept of the technical solution of this application, and these modifications and improvements all fall within the scope of protection of this application.

Claims

1. A highly efficient method for scheduling ceramic filter clusters, characterized in that, The specific steps include the following: Step 1: Equipment Status Inquiry and Correction. Collect and track the status of all ceramic filters in the solid-liquid separation workshop. Check if they are in remote or in-service status, and if they have no abnormalities or fault alarms. Only if all of the above conditions are met can they participate in scheduling. If any of the above conditions are met, it is considered that the conditions are not met and on-site processing and elimination are required. If the function switch indicating that the equipment is in good condition and can participate in scheduling is not in the required position, switch to the required position. If the equipment has abnormalities or faults, the abnormalities or faults need to be eliminated until the conditions are met. Otherwise, the equipment is removed and does not participate in scheduling. Step 2: Grouping and sorting ceramic filters. Select ceramic filters to participate in the control, identify them by number, and store them in the scheduling system. The scheduling system distinguishes between odd and even numbers for the ceramic filters participating in the control. In order to ensure that the dewatered dry ore received by the feeding belt maintains the belt tension balance and does not affect the normal operation of the belt, it is necessary to ensure that there is more than one device with odd and even numbers, and also to ensure that the difference between the number of odd and even numbers does not exceed one. Step 3: Execute scheduling. Record the demining working time of the machines and the cleaning running time of the machines in the cleaning stage. Sort the machines and compare their demining running time. Arrange them in ascending order of value. To ensure the principle of balanced lifespan, machines with shorter demining running time have priority in the next scheduling. The scheduling system performs comprehensive analysis, calculation and judgment based on the above information, generates scheduling instructions and issues them to the corresponding numbered machines for scheduling. Step 4: Cycle or End. After the ceramic filter has finished running, it will be cleaned. After cleaning, it will automatically enter standby mode and be handed over to the scheduling system for scheduling, waiting for the next scheduling instruction. Scheduling mechanism: Machines with longer running times have priority, and production operations will be met with the fewest possible machines.

2. The efficient ceramic filter cluster scheduling method according to claim 1, characterized in that, In Step 3, scheduling is divided into two modes: One type is the scheduling at startup, where the system determines the required number of equipment sets based on the flow rate and concentration of the slurry delivered from the concentrate pipeline. The slurry comes from two sources: one is direct delivery from the concentrate pipeline, which can be directly supplied to the distribution tank at the front end of the ceramic filter. The system determines the required number of equipment sets based on the source of the ore and schedules the equipment according to its current status. One is the existing slurry, which is temporarily stored in the thickener. The concentration of the slurry needs to be adjusted first. The low-concentration slurry is concentrated, and the high-concentration slurry is diluted. Then it is sent to the distribution tank at the front end of the ceramic filter and the system schedules it. Another scenario is during operation, when the tailings of the batch-delivered slurry are about to arrive or have already arrived, causing a decrease in flow rate. At this time, the slurry concentration in the operating ceramic filters decreases, and the demineralization efficiency decreases. To ensure equipment efficiency and energy saving, it is necessary to shut down some of the operating ceramic filters. However, if the continuous operation has not reached 8 hours, the system will make a comprehensive judgment and prioritize the ceramic filters with the longest current operating time for cleaning. After cleaning, the ceramic filters will automatically enter standby mode, waiting for subsequent instructions.

3. A high-efficiency ceramic filter cluster scheduling system, characterized in that, The efficient ceramic filter cluster scheduling method described in any one of claims 1-2 includes a control system on the ceramic filter for monitoring the processing capacity and slurry characteristics of the ceramic filter, and a scheduling system on the host machine. The control systems of multiple ceramic filters are connected to the scheduling system on the host machine in a star topology. The control system of the ceramic filter is responsible for the information collection and process-oriented automatic operation control of the single-unit complete set of equipment and transmits the information to the scheduling system on the host machine. The scheduling system on the host machine comprehensively analyzes the relevant operating status information of the ceramic filter and schedules the number of ceramic filters that need to participate in production according to the equipment characteristics, combined with the process and production requirements.

4. The efficient ceramic filter cluster scheduling system according to claim 3, characterized in that, The control system of the ceramic filter includes a single-machine control system and a packaged single-machine automatic control software. It has the function of single-machine multi-mode automated operation control, provides open network communication and data interface, and connects to a centralized scheduling and control system.

5. The efficient ceramic filter cluster scheduling system according to claim 4, characterized in that, The control system of the ceramic filter specifically includes a controller, an I / O control board, a communication board and a human-machine panel, a signal acquisition sensor, a drive controller with speed adjustment function and a signal output indicator, and a voice alarm device. The signal acquisition sensor is installed at the detection point, all input signals are connected to the input board of the I / O control board and pre-allocated channels, and the control adjustment output signal is connected to the drive controller, the signal output indicator and the voice alarm device.

6. The efficient ceramic filter cluster scheduling system according to claim 3, characterized in that, The ceramic filter is equipped with a switch for switching in and out. Switching in indicates that the equipment is in good condition and can participate in scheduling, while switching out indicates that the equipment is not ready.

7. The efficient ceramic filter cluster scheduling system according to claim 3, characterized in that, The scheduling system on the host is equipped with a monitoring and operation station for running the scheduling system screen, which mainly includes necessary parameter setting sub-screens, process overview main screen, solid-liquid separation workshop sub-screens, and monitoring screens for individual ceramic filters.

8. The efficient ceramic filter cluster scheduling system according to claim 4, characterized in that, The scheduling system can simultaneously meet the continuous, synchronous, efficient, and automatic operation of 14 sets of ceramic filter machines.

9. A high-efficiency ceramic filter cluster scheduling system according to claim 6, characterized in that, The ceramic filter is equipped with a lifting cleaning device that is connected to the control system.

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