CN111879541B - Powder preparation system test platform - Google Patents
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- CN111879541B CN111879541B CN202010745576.6A CN202010745576A CN111879541B CN 111879541 B CN111879541 B CN 111879541B CN 202010745576 A CN202010745576 A CN 202010745576A CN 111879541 B CN111879541 B CN 111879541B
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
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- G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
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Abstract
The invention discloses a powder preparation system test platform which comprises a control system, and a feeding unit, a powder making unit, a transferring unit, a powder selecting unit and a returning unit which are sequentially communicated; the materials are sent into the powder making unit by the feeding unit and are crushed into powder, then sent into the powder selecting unit by the transferring unit and are separated into non-selected materials and finished product materials, and the non-selected materials are sent into the returning unit and are returned to the powder making unit for continuous crushing; sampling and detecting materials at each stage through a first sampling port arranged on the transfer unit, a second sampling port arranged on the powder selecting unit and a third sampling port arranged on the return unit; the control system is electrically connected with each unit, and the operating parameters of each unit are adjusted and collected through the control system. According to the invention, the material is sampled through the sampling port, the control system is used for collecting the operation parameters of each unit, the sampling data is matched with the operation parameters, the optimal parameters meeting the particle size requirement are determined, and the most direct basis is provided for the equipment model selection and parameter setting of the powder preparation system.
Description
Technical Field
The invention relates to the technical field of powder preparation system test analysis, in particular to a powder preparation system test platform.
Background
The powder preparation system is widely applied to the industries of metallurgy, chemical industry, building materials, environmental protection, materials and the like, and mainly uses the cooperative operation of crushing equipment, sorting equipment and other mechanisms to crush ore raw materials into powder and then carry out single-stage or multi-stage sorting to obtain corresponding powder. Generally speaking, different ore raw materials have different crushing performances, so that one set of powder preparation system can only be used for powder preparation of one type of material, while the situation that similar ore raw materials in different regions generate larger crushing performance difference even occurs in george manner in China, which causes great troubles in equipment type selection and structure design of the powder preparation system for equipment manufacturers, design research institutes and users.
At present, the crushing effect of the powder preparation system on a certain material can be embodied only after the powder preparation system is put into use, and the powder preparation system is designed and shaped, so that the modification cost is high, and the performance of the powder preparation system can be reduced in the modification process. Therefore, a platform capable of testing a powder preparation system is urgently needed to meet the adaptability requirement of the society on equipment.
Disclosure of Invention
In view of the above, it is necessary to provide a powder preparation system test platform capable of performing a test on a powder preparation system to verify the function of the powder preparation system.
A powder preparation system test platform comprises a control system, and a feeding unit, a powder making unit, a transferring unit, a powder selecting unit and a returning unit which are sequentially communicated; the feeding unit is used for quantitatively feeding the material to be prepared into the powder making unit; the powder making unit receives the material to be prepared and then crushes the material to be prepared into powder material; the powder material is sent to the powder selecting unit after the powder material is received by the transferring unit, and a first sampling port is arranged at the transferring unit and used for sampling and detecting the powder material; the powder selecting unit receives the powdery material, divides the powdery material into non-selected material and finished product material, and sends the non-selected material into the returning unit, and a second sampling port is arranged at the position of the powder selecting unit for outputting the finished product material and is used for sampling and detecting the finished product material; the returning unit is also communicated with the pulverizing unit, weighs the received non-selected materials, and returns the non-selected materials to the pulverizing unit for continuous crushing; a third sampling port is arranged at the position of the return unit and is used for sampling and detecting non-selected materials; the feeding unit, the powder making unit, the transferring unit, the powder selecting unit and the returning unit are all electrically connected with the control system, and the operating parameters of the feeding unit, the powder making unit, the transferring unit, the powder selecting unit and the returning unit are controlled, adjusted, collected and stored through the control system.
In one embodiment, the device also comprises a negative pressure unit electrically connected with the control system, wherein the negative pressure unit is communicated with the powder selecting unit through a dust collecting pipeline and is used for enabling the material channels in all the units to operate in a negative pressure mode and collecting superfine materials; and a fourth sampling port is arranged at the negative pressure unit and used for sampling and detecting the superfine material.
In one embodiment, the negative pressure unit is further communicated with the feeding unit, the pulverizing unit and the transferring unit through dust collecting pipelines respectively and is used for collecting free superfine materials.
In one embodiment, the feeding unit comprises a feeding bin and a weighing belt feeder, the feeding bin is communicated with a feeding hole of the weighing belt feeder, a discharging hole of the weighing belt feeder is communicated with a feeding hole of the powder preparation unit, and a material to be prepared is fed into the powder preparation unit to be crushed and prepared.
In one embodiment, the transfer unit is used for lifting the received powdery material to the feed inlet above the powder selecting unit.
In one embodiment, the transfer unit comprises an impeller airlock valve, a first screw conveyor and a bucket elevator, wherein a feed inlet of the impeller airlock valve is communicated with a discharge outlet of the powder preparation unit and used for receiving the powder material; the first sampling port is formed in one side of the first spiral conveyor.
In one embodiment, the powder selecting unit comprises a blower fan, a static powder selecting machine and a cyclone separator, a first feeding hole, a first air inlet and a first air outlet are arranged at the upper part of the static powder selecting machine, the first feeding hole is communicated with the transferring unit and used for receiving the powdery material, the first air inlet is communicated with the air outlet of the blower fan, and the first air outlet is communicated with the feeding hole of the cyclone separator; a first discharge port is arranged at the lower part of the static powder concentrator and is communicated with the return unit; the second sampling port is formed in one side of the discharge port of the cyclone separator.
In one embodiment, the powder selecting unit further comprises a dynamic powder selecting machine arranged between the static powder selecting machine and the cyclone separator, the dynamic powder selecting machine is provided with a second feeding hole, a second discharging hole and a second air outlet, the second feeding hole is communicated with the first air outlet, and the second air outlet is communicated with the feeding hole of the cyclone separator.
In one embodiment, the returning unit comprises a spiral scale and a second spiral conveyor, and a feeding hole of the spiral scale is communicated with the powder selecting unit and used for receiving non-selected materials; the discharge hole of the spiral scale is communicated with the feed inlet of the second spiral conveyor, and the discharge hole of the second spiral conveyor is communicated with the feed inlet of the pulverizing unit; the third sampling port is formed in one side of the second spiral conveyor.
In one embodiment, the negative pressure unit comprises a bag dust collector and an exhaust fan, a third feeding port and a third air outlet are arranged at the upper part of the bag dust collector, the third feeding port is communicated with the dust collecting pipeline, and the third air outlet is communicated with an air inlet of the exhaust fan; a dust collector discharge screw is arranged at the lower part of the bag dust collector, and a third discharge hole is formed at the bottom of the dust collector discharge screw; the fourth sampling port is arranged at one side of the dust collector discharge screw.
Compared with the prior art, the invention reasonably configures each unit device to perform powder making operation, reasonably sets the sampling port to perform material sampling, controls and adjusts each unit device by using the control system, collects and stores the operation parameters of each unit device, matches the data such as particle size and the like obtained according to the sampled materials with the operation parameters of each unit device at that time, determines the optimal operation parameters meeting the particle size requirements, and provides the most direct basis for the device model selection and the control parameter setting of the powder preparation system.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings of the embodiments can be obtained according to the drawings without creative efforts.
Fig. 1 is a process flow diagram of a powder preparation system test platform according to an embodiment of the present invention;
fig. 2 is a process flow diagram of another powder preparation system test platform according to an embodiment of the present invention;
fig. 3 is a schematic structural diagram of another powder preparation system test platform according to an embodiment of the present invention;
fig. 4 is a schematic structural diagram of a static powder concentrator according to an embodiment of the present invention;
fig. 5 is a schematic structural diagram of a dynamic powder concentrator according to an embodiment of the present invention;
fig. 6 is a schematic structural diagram of a bag dust collector provided in an embodiment of the present invention.
Wherein: 1-a control system, 2-a feeding unit, 21-a feeding bin, 22-a weighing belt feeder, 3-a powder preparation unit, 4-a transfer unit, 41-an impeller airlock valve, 42-a first screw conveyor, 43-a bucket elevator, 5-a powder selection unit, 51-a blower, 52-a static powder selector, 521-a first feeding port, 522-a first air inlet, 523-a first air outlet, 524-a first discharging port, 53-a cyclone separator, 54-a dynamic powder selector, 541-a second feeding port, 542-a second discharging port, 543-a second air outlet, 6-a return unit, 61-a screw scale, 62-a second screw conveyor, 7-a negative pressure unit, 71-a bag-distributing dust collector, 711-a third feeding port, 712-a third air outlet, 713-a dust collector discharge screw, 714-a third discharge hole, 72-an exhaust fan, 73-a dust collection pipeline, 8-a receiving hopper, 10-a first sampling port, 20-a second sampling port, 30-a third sampling port and 40-a fourth sampling port.
Detailed Description
In order to facilitate an understanding of the present invention, a powder preparation system test platform will be described more fully below with reference to the accompanying drawings. The preferred embodiment of the powder preparation system test platform is given in the attached drawings. However, the powder preparation system test platform may be implemented in many different forms and is not limited to the embodiments described herein. Rather, these examples are provided to provide a more thorough disclosure of the powder preparation system test platform.
In the description of the present application, it should be noted that if the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. indicate an orientation or positional relationship based on the orientation or positional relationship shown in the drawings or the orientation or positional relationship which the product of this application is usually placed in when used, this is only for the convenience of describing the present application and simplifying the description, and it does not indicate or imply that the referred unit or element must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as limiting the present application.
It will be understood that when an element is referred to as being "mounted on" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "in communication" with another element, it can be directly in communication with the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used herein in the description of the powder preparation system test platform is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention.
As shown in fig. 1 and fig. 2, an embodiment of the present invention provides a powder preparation system test platform, which includes a control system 1, and a feeding unit 2, a pulverizing unit 3, a transferring unit 4, a powder selecting unit 5, and a returning unit 6, which are sequentially communicated; the feeding unit 2 is used for quantitatively feeding materials to be prepared into the powder making unit 3; the powder preparation unit 3 receives the material to be prepared and then crushes the material to be prepared into powder material; the powder preparation unit 3 is communicated with the powder selecting unit 5 through the transferring unit 4, the transferring unit 4 receives the powdery material and then sends the powdery material into the powder selecting unit 5, and the transferring unit 4 is provided with a first sampling port 10 for sampling and detecting the powdery material; the powder selecting unit 5 receives the powdery material, divides the powdery material into non-selected material and finished product material, and sends the non-selected material into the returning unit 6, and a second sampling port 20 is arranged at the position of the powder selecting unit 5 for outputting the finished product material and is used for sampling and detecting the finished product material; the returning unit 6 is also communicated with the pulverizing unit 3, weighs the received non-selected materials, and returns the non-selected materials to the pulverizing unit 3 for continuous crushing; a third sampling port 30 is arranged at the position of the return unit 6 and is used for sampling and detecting non-selected materials; the feeding unit 2, the powder making unit 3, the transferring unit 4, the powder selecting unit 5 and the returning unit 6 are all electrically connected with the control system 1, and the feeding unit 2, the powder making unit 3, the transferring unit 4, the powder selecting unit 5 and the returning unit 6 are controlled, adjusted, collected and stored through the control system 1. The method comprises the steps of carrying out powder preparation operation by reasonably configuring each unit device, reasonably arranging a sampling port at a proper position of each unit device for material sampling, controlling and adjusting each unit device by using a control system 1, collecting and storing operation parameters of each unit device, matching the data such as particle size and the like obtained according to the sampled materials with the operation parameters of each unit device at that time, determining the optimal operation parameters meeting the particle size requirements, and providing the most direct basis for device model selection and parameter setting of a powder preparation system.
Specifically, the method mainly comprises the steps of changing relevant operation parameters of the powder making unit 3 and the powder selecting unit 5, carrying out sampling analysis on corresponding materials through the first sampling port 10, the second sampling port 20 and the third sampling port 30, and finding out the powder preparation system matched with the current ore raw material correspondingly through matching of the first sampling port, the second sampling port and the third sampling port. The change of the relevant operating parameters of the powder preparation unit 3 and the powder selection unit 5 can be realized by adjusting the structure or data of the same equipment, and can also be changed by replacing equipment with different models as long as the preparation system with better crushing effect can be found out for model selection. The corresponding materials comprise powdery materials, non-selected materials and finished product materials, wherein the powdery materials refer to basic powder sent out from a discharge port of the powder making unit 3; the non-selected material refers to the powder which does not meet the granularity requirement and is separated by the powder selecting unit 5 and needs to be returned to the powder preparing unit 3 for re-crushing, and the non-selected material is usually the powder with the particle size larger than 1 mm; the finished product material refers to available powder meeting the sorting granularity requirement, and is usually powder with the particle size of less than 1 mm. The material sample is selected based on the fact that the weight (namely, the amount of the returned material) of the non-selected material received by the returning unit 6 tends to be stable, the sample of the same sampling port is sampled for more than 5 times, the interval is 5-10 minutes every time, and the numerical value obtained by weighted average after the maximum data and the minimum data in the sample data are removed is used as the sample data to carry out the particle size distribution condition analysis.
In this embodiment, the control system 1 is a PAC control analysis system, and is capable of monitoring and setting parameters of each unit device in a sampling process, wherein the control parameters include a feeding amount and a feeding speed of the feeding unit 2, a rotation speed, a crushing gap and a center distance of the pulverizing unit 3, an air volume, an air speed, a rotation speed, a baffle angle and the like of the pulverizing unit 5, the monitoring parameters include the control parameters, a current, a voltage, energy consumption, a temperature and noise of each unit, a return amount of the return unit 6 and the like, the parameter setting of each unit device is realized by the control parameters, and the operation state of each unit device is monitored by the monitoring parameters, so that each unit device is ensured to be in a normal operation state; selecting a set of equipment model selection, performing test operation on a group of ore raw materials through the equipment model selection, debugging control parameters in the test operation process to ensure that each unit equipment is in a normal operation state, obtaining a powdery material sample from the first sampling port 10, and analyzing the particle size distribution condition of the powdery material sample to obtain the milling efficiency and the primary yield of the milling unit 3; obtaining a finished product material sample from the second sampling port 20, obtaining a non-selected material sample from the third sampling port 30, analyzing the particle size distribution of the finished product material sample and the non-selected material sample, and obtaining the powder selection efficiency of the powder selection unit 5 by combining the particle size distribution of the powdery material sample obtained from the first sampling port 10; and then the cyclic load of the whole powder preparation system can be obtained through the feeding amount, the returning amount and the finished product amount, and the control parameters and the equipment selection are collected as a group of operation parameters and correspondingly stored with the sample data under the condition of meeting the established requirements of the finished product particle size and the cyclic load. On the basis of the selection of the equipment, under the condition of meeting the established requirements of the particle size requirement and the cyclic load of a finished product, adjusting the control parameters to perform trial operation again, obtaining another set of operation parameters for collection and storing the operation parameters corresponding to the sample data. And replacing the equipment for type selection, adopting the method for trial operation again, obtaining another set of operation parameters for collection and correspondingly storing the operation parameters and the sample data. And comparing the plurality of groups of operation parameters to obtain a group of better operation parameters with high powder preparation efficiency and high powder separation efficiency aiming at the current ore raw material, thereby obtaining a set of optimal powder preparation system aiming at the current ore raw material.
Further, as shown in fig. 1 and 2, the device further comprises a negative pressure unit 7 electrically connected with the control system 1, wherein the negative pressure unit 7 is communicated with the powder selecting unit 5 through a dust collecting pipeline 73, and is used for enabling material channels in each unit to operate in a negative pressure mode and collecting superfine materials; a fourth sampling port 40 is arranged at the negative pressure unit 7 and used for sampling and detecting the superfine material. Through setting up negative pressure unit 7 intercommunication selection powder unit 5, can form the negative pressure in the material passageway, prevent that the powder is excessive to carry out recycle to the superfine material that the powder process in-process produced, both can be used to preparation limestone slurry, can avoid polluted air again, green.
Specifically, the ultrafine material generally refers to dust with a particle size of less than 0.045mm, and is discharged into the air to cause air pollution, and the ultrafine material has a small particle size and a light weight and is located at the top of the material channel, so that the dust collection pipeline 73 is mainly arranged at the top of the last device in the powder selecting unit 5 to achieve a good dust collection effect. By adopting the sampling method, a superfine material sample is obtained from the fourth sampling port 40, the particle size distribution condition of the superfine material sample is analyzed, so that the dust collection effect of the negative pressure unit 7 is obtained, the parameter monitoring and setting are carried out on the negative pressure unit 7 through the control system 1, the control parameter of the negative pressure unit 7 is debugged for many times under the condition of meeting the set dust collection requirement, so as to obtain different dust collection effect conditions, the superfine material sample data is brought into the sample data category mentioned in the method, and a group of better operation parameters with good dust collection effect aiming at the current ore raw material is obtained through comparison by the method, so that a set of complete and preferable powder preparation system aiming at the current ore raw material can be obtained.
Further, as shown in fig. 1 and fig. 2, the negative pressure unit 7 is further communicated with the feeding unit 2, the powder making unit 3 and the transferring unit 4 through a dust collecting pipeline 73, the dust collecting pipeline 73 can be arranged at the material passage connection positions among the feeding unit 2, the powder making unit 3 and the transferring unit 4, or the material passage connection positions among the devices in each unit and other dust leakage points which are easy to occur are provided with interfaces of the dust collecting pipeline 73, so that free ultrafine materials can be collected, and the environmental protection requirement is met.
Further, as shown in fig. 2 and fig. 3, the feeding unit 2 includes a feeding bin 21 and a weighing belt feeder 22, the feeding bin 21 is communicated with a feeding port of the weighing belt feeder 22, a discharging port of the weighing belt feeder 22 is communicated with a feeding port of the pulverizing unit 3, and the material to be prepared is fed into the pulverizing unit 3 to be pulverized. Through the connection of the weighing belt feeder 22 and the control system 1, the feeding amount and the feeding speed can be accurately monitored and controlled, and the feeding unit 2 can be accurately monitored and controlled.
Further, as shown in fig. 2 and 3, the transfer unit 4 is configured to lift the received powder material to a feed inlet above the powder selecting unit 5, and the whole powder preparing apparatus for powder selection is expanded in the vertical direction, so as to save floor space and improve space utilization.
Specifically, the milling unit 3 is usually a pulling-breaking high-efficiency milling machine or other various milling machines, and has a feed inlet at the top of the milling machine and a discharge outlet at the bottom of the milling machine, and is large in size, high in weight and not suitable for carrying; the powder selecting unit 5 is usually various powder selecting machines such as a V-shaped powder selecting machine, a feeding hole of the powder selecting unit is positioned at the top of the powder selecting machine, a discharging hole of the powder selecting machine is positioned at the bottom of the powder selecting machine, although the powder selecting machine is large in size, the weight of the powder selecting machine is lighter than that of the powder preparing unit 3, the method for changing the operation parameters of the test platform provided by the invention further comprises the step of changing different types of equipment, and therefore, the arrangement directions of the powder preparing unit 3 and the powder selecting unit 5 are particularly important in consideration of the convenience of equipment change. In this embodiment, consider the vibration intensity and the whole weight of powder process unit 3, set up powder process unit 3 in lower position, select powder unit 5 to set up in higher position, upwards promote the feed inlet to select powder unit 5 top with the powdery material that powder process unit 3 made through transporting unit 4 to make test platform whole firm, and be convenient for change and transportation.
Further, as shown in fig. 2 and 3, the transfer unit 4 comprises an impeller airlock valve 41, a first screw conveyor 42 and a bucket elevator 43, and the three have simple structure, small cross-sectional area, good sealing property, convenient operation and easy maintenance, and meet the requirements of closed transportation and space type selection of the invention; the inlet of the impeller airlock valve 41 is communicated with the outlet of the powder preparation unit 3, the outlet of the impeller airlock valve 41 is communicated with the inlet of the first screw conveyor 42, the outlet of the first screw conveyor 42 is communicated with the inlet of the bucket elevator 43, and the outlet of the bucket elevator 43 is communicated with the inlet of the powder separation unit 5; the first sampling port 10 is opened at one side of the first screw conveyor 42. The impeller airlock valve 41, the first screw conveyor 42 and the bucket elevator 43 are connected with the control system 1, so that the running state of the transfer unit 4 can be accurately monitored and controlled, and the normal running of the transfer unit 4 is ensured. The first sampling port 10 is arranged on one side of the first screw conveyer 42, so that the sampling is convenient, the online real-time sampling in the running process of the equipment can be realized, and the accuracy of the powdery material sample is ensured.
Further, as shown in fig. 2, fig. 3 and fig. 4, the powder selecting unit 5 includes a static powder selecting machine 52, an air make-up machine 51 and a cyclone 53, a first feeding port 521, a first air inlet 522 and a first air outlet 523 are arranged at the upper part of the static powder selecting machine 52, the first air inlet 522 is communicated with an air outlet of the air make-up machine 51, and the first air outlet 523 is communicated with a feeding port of the cyclone 53; a first discharge hole 524 is formed in the lower part of the static powder concentrator 52, and the first discharge hole 524 is communicated with the returning unit 6; the second sampling port 20 is formed at one side of the discharge port of the cyclone 53. The air supplementing machine 51 is connected with the control system 1, so that the air quantity, the air speed and the like of the powder selecting unit 5 can be accurately monitored and controlled, and the powder selecting unit 5 can be accurately monitored and controlled. The second sampling port 20 is arranged on one side of the discharge port of the cyclone separator 53, so that the sampling is convenient, the online real-time sampling in the operation process of the equipment can be realized, and the accuracy of the finished product material sample is ensured.
Specifically, based on the description of the equipment provided by the foregoing transfer unit 4, the first feeding port 521 is used as the feeding port of the powder selecting unit 5 and is communicated with the discharging port of the bucket elevator 43, the powder material is fed by the first feeding port 521 to form a material curtain, the feeding airflow passes through the material curtain from the first air inlet 522 and contacts with the powder material, the powder material is scattered by the inclined plate at the lower right side and collides back and forth on the left and right side plates, so as to achieve the effects of breaking up the material block, fully exposing the fine powder and prolonging the retention time of the material curtain, and then the non-selected material falls and is discharged along the two side plates, and the finished material is discharged from the first air outlet 523 along with the gas and enters the cyclone 53 to perform gas-material separation. In the present embodiment, the cyclone 53 is the last equipment of the dust separation unit 5, and therefore the dust collecting pipeline 73 of the aforementioned negative pressure unit 7 is arranged at the top of the cyclone 53 to achieve a good dust collecting effect.
Further, as shown in fig. 2, 3 and 5, the powder selecting unit 5 further includes a dynamic powder selecting machine 54 disposed between the static powder selecting machine 52 and the cyclone separator 53 to realize multi-stage separation and further subdivide the finished material; the dynamic powder concentrator 54 is provided with a second feed inlet 541, a second discharge outlet 542 and a second air outlet 543, the second feed inlet 541 is communicated with the first air outlet 523, the second air outlet 543 is communicated with the feed inlet of the cyclone separator 53, and the second discharge outlet 542 is connected with a discharge hopper for collecting finished product materials. The dynamic powder concentrator 54 is connected with the control system 1, so that the rotating speed, the baffle angle and the like of the powder concentrating unit 5 can be accurately monitored and controlled, and the powder concentrating unit 5 can be accurately monitored and controlled.
Further, as shown in fig. 2 and 3, the returning unit 6 comprises a screw scale 61 and a second screw conveyor 62, wherein a feed inlet of the screw scale 61 is communicated with the powder selecting unit 5 for receiving non-selected materials; the discharge hole of the spiral scale 61 is communicated with the feed hole of the second spiral conveyor 62, and the discharge hole of the second spiral conveyor 62 is communicated with the feed hole of the milling unit 3; the third sampling port 30 is opened at one side of the second screw conveyor 62. The spiral scale 61 and the second spiral conveyer 62 are connected with the control system 1, so that the material returning amount of the returning unit 6 can be accurately monitored and controlled, the normal operation of the returning unit 6 is ensured, and the accurate monitoring and control of the returning unit 6 are realized. The third sampling port 30 is arranged on one side of the second screw conveyer 62, so that the sampling is convenient, the online real-time sampling in the operation process of the equipment can be realized, and the accuracy of non-selected material samples is ensured.
Specifically, based on the description of the equipment that aforementioned selection powder unit 5 provided, the feed inlet of screw balance 61 communicates with above-mentioned first discharge gate 524 to receive non-selection material, carry out flow, flow direction's control to non-selection material through screw balance 61, and realize accurate measurement management, communicate with the feed inlet of powder process unit 3 through the discharge gate of second screw conveyer 62, realize a confined circulation circuit, the repeated circulation is polished, when obtaining the fine high powder of degree of fineness, compact structure is reasonable, space utilization has been improved.
Further, as shown in fig. 2, 3 and 6, the negative pressure unit 7 includes a bag dust collector 71 and an exhaust fan 72, a third feed port 711 and a third air outlet 712 are provided at an upper portion of the bag dust collector 71, a dust collector discharge screw 713 is provided at a lower portion of the bag dust collector 71, the third feed port 711 is communicated with the dust collecting pipeline 73, the third air outlet 712 is communicated with an air inlet of the exhaust fan 72, a dust collector discharge screw 713 is provided at a lower portion of the bag dust collector 71, and a third discharge port 714 is provided at a bottom of the dust collector discharge screw 713; a fourth sampling port 40 is provided at one side of the dust collector discharge screw 713. The exhaust fan 72 is connected with the control system 1, so that the air quantity, the air speed and the like of the negative pressure unit 7 can be accurately monitored and controlled, and the negative pressure unit 7 can be accurately monitored and controlled. The fourth sampling port 40 is arranged on one side of the dust collector discharge screw 713, so that sampling is convenient, online real-time sampling in the operation process of equipment can be realized, and the accuracy of superfine material samples is ensured.
The above-mentioned embodiments only express several embodiments of the present invention, and the description thereof is more specific and detailed, but not construed as limiting the scope of the present invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention. Therefore, the protection scope of the present patent shall be subject to the appended claims.
Claims (9)
1. A powder preparation system test platform is characterized by comprising a control system, and a feeding unit, a powder making unit, a transferring unit, a powder selecting unit and a returning unit which are sequentially communicated;
the feeding unit is used for quantitatively feeding the material to be prepared into the pulverizing unit;
the powder making unit receives the material to be prepared and then crushes the material to be prepared into powder material;
the powder selecting unit is used for selecting powder materials from the powder selecting unit, and the powder materials are conveyed to the powder selecting unit through the conveying unit;
the powder selecting unit receives the powdery material, divides the powdery material into non-selected material and finished product material, and sends the non-selected material into the returning unit, and a second sampling port for sampling and detecting the finished product material is arranged at the position where the powder selecting unit is used for outputting the finished product material;
The returning unit is also communicated with the pulverizing unit, weighs the received non-selected materials, and returns the non-selected materials to the pulverizing unit for continuous crushing; a third sampling port is arranged at the position of the return unit and is used for sampling and detecting non-selected materials;
the return unit comprises a spiral scale and a second spiral conveyor, and a feed inlet of the spiral scale is communicated with the powder selecting unit and used for receiving non-selected materials; the discharge hole of the spiral scale is communicated with the feed hole of the second spiral conveyer, and the discharge hole of the second spiral conveyer is communicated with the feed hole of the milling unit; the third sampling port is formed in one side of the second spiral conveyor;
the feeding unit, the powder making unit, the transferring unit, the powder selecting unit and the returning unit are all electrically connected with the control system, and the control system controls, adjusts, collects and stores the operating parameters of the feeding unit, the powder making unit, the transferring unit, the powder selecting unit and the returning unit.
2. The powder preparation system test platform of claim 1, further comprising a negative pressure unit electrically connected to the control system, the negative pressure unit being communicated with the powder selection unit through a dust collection pipeline for causing material channels in each unit to operate at negative pressure and collecting ultra-fine materials; and a fourth sampling port is arranged at the negative pressure unit and is used for sampling and detecting the superfine material.
3. The powder preparation system test platform of claim 2, wherein the negative pressure unit is further communicated with the feeding unit, the pulverizing unit and the transferring unit through dust collecting pipelines respectively, and is used for collecting free ultrafine materials.
4. The powder preparation system test platform of claim 1, wherein the feeding unit comprises a feeding bin and a weighing belt feeder, the feeding bin is communicated with a feeding port of the weighing belt feeder, a discharging port of the weighing belt feeder is communicated with a feeding port of the powder preparation unit, and a material to be prepared is fed into the powder preparation unit to be crushed and prepared.
5. The powder preparation system test platform of claim 1, wherein the transfer unit is configured to lift the received powder material to a feed inlet above the powder selecting unit.
6. The powder preparation system test platform of claim 5, wherein the transfer unit comprises an impeller airlock valve, a first screw conveyor and a bucket elevator, a feed port of the impeller airlock valve is communicated with a feed port of the powder preparation unit and used for receiving powder materials, a feed port of the impeller airlock valve is communicated with a feed port of the first screw conveyor, a feed port of the first screw conveyor is communicated with a feed port of the bucket elevator, and a feed port of the bucket elevator is communicated with the powder selection unit; the first sampling port is formed in one side of the first spiral conveyor.
7. The powder preparation system test platform of claim 1, wherein the powder selection unit comprises a blower, a static powder selector and a cyclone separator, a first feed inlet, a first air inlet and a first air outlet are arranged at the upper part of the static powder selector, the first feed inlet is communicated with the transfer unit and used for receiving powdery materials, the first air inlet is communicated with the air outlet of the blower, and the first air outlet is communicated with the feed inlet of the cyclone separator; a first discharge hole is formed in the lower part of the static powder concentrator and communicated with the return unit; the second sampling port is formed in one side of the discharge port of the cyclone separator.
8. A powder preparation system test platform as claimed in claim 7, wherein the powder selection unit further comprises a dynamic powder selection machine arranged between the static powder selection machine and the cyclone separator, the dynamic powder selection machine is provided with a second feed inlet, a second discharge outlet and a second air outlet, the second feed inlet is communicated with the first air outlet, and the second air outlet is communicated with the feed inlet of the cyclone separator.
9. The powder preparation system test platform of claim 2, wherein the negative pressure unit comprises a bag dust collector and an exhaust fan, a third feed port and a third air outlet are arranged at the upper part of the bag dust collector, the third feed port is communicated with the dust collection pipeline, and the third air outlet is communicated with an air inlet of the exhaust fan; a dust collector discharge screw is arranged at the lower part of the bag dust collector, and a third discharge hole is formed in the bottom of the dust collector discharge screw; and the fourth sampling port is formed at one side of the dust collector discharge spiral.
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| CN107051691A (en) * | 2017-04-10 | 2017-08-18 | 太仓金溪粉碎设备有限公司 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
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| CN111298951A (en) * | 2020-03-24 | 2020-06-19 | 桂林鸿程矿山设备制造有限责任公司 | Automatic powder selection control method, system and device for vertical mill classifier |
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