CN113769653A - Ceramic dry particle glaze batch mixing device and method - Google Patents
Ceramic dry particle glaze batch mixing device and method Download PDFInfo
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- CN113769653A CN113769653A CN202111144052.2A CN202111144052A CN113769653A CN 113769653 A CN113769653 A CN 113769653A CN 202111144052 A CN202111144052 A CN 202111144052A CN 113769653 A CN113769653 A CN 113769653A
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- 238000002156 mixing Methods 0.000 title claims abstract description 43
- 239000000919 ceramic Substances 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 82
- 238000003860 storage Methods 0.000 claims abstract description 74
- 239000000375 suspending agent Substances 0.000 claims abstract description 72
- 238000005303 weighing Methods 0.000 claims abstract description 23
- 238000005086 pumping Methods 0.000 claims abstract description 22
- 239000002002 slurry Substances 0.000 claims abstract description 21
- 239000008187 granular material Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 10
- 238000007781 pre-processing Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 5
- 238000012545 processing Methods 0.000 abstract description 14
- 238000012544 monitoring process Methods 0.000 description 6
- 239000008188 pellet Substances 0.000 description 4
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Abstract
The invention relates to a batch mixing device and method for ceramic dry particle glaze. The device comprises: a suspending agent feeding device, a dry particle feeding device, a stirrer and a controller; the suspending agent feeding device comprises a suspending agent slurry storage tank, a discharge port of the suspending agent slurry storage tank is connected with a first feed port of the stirrer through a pipeline, and a glaze pumping pump and a flowmeter are arranged on the pipeline; the dry particle feeding device comprises a storage bin, a discharge port of the storage bin is provided with a storage bin valve, the discharge port of the storage bin is connected with a feeding port of a weighing hopper, a spiral propeller and an electronic scale are arranged at the discharge port of the weighing hopper, and the discharge port of the spiral propeller is connected with a second feeding port of the stirrer; the number of the dry particle feeding devices is N, the dry particle feeding devices are used for containing different types of dry particles, and N is more than or equal to 1; the controller controls the addition of the suspending agent, the addition of the dry particles and the working state of the stirrer. The invention provides the dry particle glaze mixing device which is accurately prepared according to the amount, simple to operate, high in processing efficiency and more uniform in stirring.
Description
Technical Field
The invention relates to the field of stirring and mixing devices, in particular to a batch mixing device for dry ceramic particle glaze.
Background
With the popularity of candy and dry-particle ceramic tile products, the requirement on the processing capacity of dry-particle glaze is higher and higher. The dry particle glaze is produced by adding dry particles with different particle sizes and different functions into a suspending agent according to a proportion, and fully and uniformly stirring. At present, two common processing modes of the dry particle glaze exist, and the first method is to directly process on a production line: the working barrel with the glaze pump is used, the suspending agent is added into the barrel, various dry particles are added, and the mixture is directly used after being uniformly stirred. The second method is to use a modified disperser: and pouring the suspending agent and the dry granules into a barrel, putting the barrel into a dispersion machine, stirring for twenty minutes, and using the mixture after the dry granules and the suspending agent are uniformly stirred. The disadvantages of both methods are that the preparation of dry particle variety and weight is often wrong in the processing process, the processing efficiency of the dry particle glaze is low, and only 800 kilograms of dry particle glaze can be processed per hour. When the using amount of the dry grain glaze is large, the two methods cannot meet the production requirements.
In view of the above, there is a need for an apparatus for batch production of dry glaze granules, which can improve the processing efficiency of dry glaze granules, and at the same time ensure that the preparation of dry glaze granules and suspending agent is not wrong and the mixture is uniformly stirred.
Disclosure of Invention
In order to solve the technical problem, the invention provides a batch mixing device for dry ceramic particle glaze.
The invention is realized by adopting the following technical scheme:
in one aspect, an embodiment of the present invention provides a ceramic dry-particle glaze batch mixing device, including: a suspending agent feeding device, a dry particle feeding device, a stirrer and a controller;
the suspension agent feeding device comprises a suspension agent slurry storage tank 11, a discharge port of the suspension agent slurry storage tank 11 is connected with a first feed port of the stirrer through a pipeline, and a glaze pumping pump 13 and a flowmeter 14 are arranged on the pipeline;
the dry particle feeding device comprises a storage bin 21, a storage bin valve is arranged at a discharge port of the storage bin 21, a discharge port of the storage bin is connected with a feed port of a weighing hopper 23, a spiral propeller 24 and an electronic scale 25 are arranged at the discharge port of the weighing hopper 23, and the discharge port of the spiral propeller 24 is connected with a second feed port of the stirrer;
the number of the dry particle feeding devices is N, the dry particle feeding devices are used for containing different types of dry particles, and N is more than or equal to 1;
the controller controls the adding amount of the suspending agent by controlling the work of the glaze pumping pump 13, controls the adding amount of the dry granules by controlling the switch of the storage bin valve and the work of the spiral propeller 24, and controls the working state of the stirrer.
In some embodiments, the batch mixing device for ceramic dry glaze particles further comprises a conveyor belt 26 and a feed hopper 38, the feed hopper 38 is connected to the second feed port of the stirrer, the conveyor belt 26 receives the dry glaze particles pushed by the screw propeller 24, and the dry glaze particles are conveyed into the feed hopper 38.
In some embodiments, the dry pellet feeding device is disposed on one or both sides of the conveyor belt 26.
In some embodiments, the top of the stirrer is externally connected with a stirring motor 31, and the stirrer is internally provided with a stirring shaft, one end of the stirring shaft is connected with the stirring motor 31, and the other end of the stirring shaft extends towards the bottom of the stirrer and is provided with a stirring blade 35.
In some embodiments, the stirring blade is in an inverted V-shaped structure.
In some embodiments, the ceramic dry-particle glaze batch mixing device further includes a differential 32, two ends of the differential 32 are respectively connected to the stirring motor 31 and the stirring shaft, and the controller controls the rotation speed of the stirring pump through the differential 32 according to different types of the processed dry-particle glaze, so as to control the rotation speed of the stirring blade 35.
In some embodiments, the bottom of the blender is further provided with a gas inlet 36 and a gas inlet valve 37, the gas inlet 36 is connected with a blower through a gas pipe, and the blower blows gas to flow from the bottom to the top of the blender.
In some embodiments, the dry particle feeding device further comprises a flexible connecting pipe, and two ends of the flexible connecting pipe are respectively connected with the discharge hole of the storage bin 21 and the feeding hole of the weighing hopper 23.
On the other hand, the embodiment of the invention provides a batch mixing method of ceramic dry particle glaze, which comprises the following steps:
s1, the suspending agent slurry storage tank 11 is filled with suspending agents to be stirred, the storage bin 21 is filled with dry particles of corresponding varieties to be stirred, the number of the storage bins is N, and N is more than or equal to 1;
s2, the controller receives the addition value of the suspension agent for preprocessing and the addition value of the dry particles for preprocessing;
s3, the ceramic dry particle glaze batch mixing device receives a starting instruction, the controller controls the glaze pumping pump 13 to start working to add the suspending agent into the stirrer, the controller opens the corresponding storage bin valve and controls the corresponding screw propeller 24 to start working according to the adding quantity value of each variety of dry particles, and the stirrer is started to start working to stir and mix;
s4, when the addition amount of the suspending agent is equal to the addition amount of the suspension agent to be preprocessed, the controller controls the glaze pumping pump 13 to stop working, and when the addition amount of the dry particles is equal to the addition amount of the dry particles to be preprocessed, the controller closes the corresponding storage bin valve and controls the corresponding spiral propeller 24 to stop working;
and S5, when the glaze pumping pump 13 stops working, all the storage bin valves are closed, all the spiral propellers stop working, the stirrer continues to be kept to stir and mix, and after the materials are uniformly stirred, the stirrer stops working.
In some embodiments, the agitator is activated while the blower is activated in step S3, the blower blows the gas from the bottom to the top of the agitator, and the agitator and blower are simultaneously deactivated in step S5.
Compared with the prior art, the invention has the following technical effects:
1. the invention uses the controller to control the addition of the suspending agent and the addition of the dry particles, improves the accuracy of the dry particle glaze processing and batching, and controls the error of each batching within 0.1 percent.
2. According to the invention, when the dry glaze is processed, the suspending agent and the dry glaze are controlled by the controller to be added into the stirrer for batching, and the stirrer is started for stirring at the same time, namely batching and stirring are carried out simultaneously, so that the processing time is shortened, 15 tons of dry glaze can be processed per hour, and the processing efficiency of the dry glaze is improved.
3. The stirring blade adopts the inverted V-shaped structural design, so that the problem that dry particles are accumulated on the stirring blade during feeding can be solved.
4. The bottom of the stirrer is connected with the blower, and the blower blows air to flow from the bottom to the top of the stirrer to generate upward stirring force, so that the stirring of the dry particles and the suspending agent is enhanced, and the dry particles and the suspending agent are stirred and mixed more uniformly.
5. The invention is matched with a granary storage system, all dry granules are packaged by ton bags, workers use a crane to complete the granary supplementing work, and one worker can easily complete the workload of the previous 5 workers, so that the labor intensity of the workers is reduced, and the working efficiency is improved.
Drawings
FIG. 1 is a schematic structural diagram of a suspending agent feeding device according to the present invention;
FIG. 2 is a schematic diagram of a dry pellet feeder of the present invention;
FIG. 3 is a schematic view of the structure of the stirrer of the present invention;
FIG. 4 is a schematic structural diagram of a batch mixing device for dry ceramic glaze particles according to the present invention;
FIG. 5 is a flow chart of the batch mixing method of the ceramic dry grain glaze of the invention.
In the figure: 11-a suspending agent slurry storage tank, 12-a slurry storage tank valve, 13-an oil pump, 14-a flow meter, 21-a storage bin, 22-a soft connection pipeline, 23-a weighing hopper, 24-a screw propeller, 25-an electronic scale, 26-a conveyor belt, 31-a stirring motor, 32-a differential, 33-an oil outlet valve, 34-a glaze outlet, 35-a stirring blade, 36-an air inlet, 37-an air inlet valve, 38-a feed hopper and 39-an observation window.
Detailed Description
In order to make those skilled in the art better understand the solution of the present invention, the technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the drawings in the embodiment of the present invention, and it is obvious that the described embodiment is only a part of the embodiment of the present invention, and not all embodiments. Other solutions, which can be obtained by a person skilled in the art without any creative effort based on the embodiments of the present invention, shall fall within the protection scope of the present invention.
Example 1
The invention provides a batch mixing device for ceramic dry particle glaze, which comprises a suspending agent feeding device, a dry particle feeding device, a stirrer and a controller. Fig. 1 shows a suspending agent feeding device structure, which comprises a suspending agent slurry storage tank 11, a slurry storage tank valve 12 is arranged at the discharge port of the suspending agent slurry storage tank 11, the discharge port of the suspending agent slurry storage tank 11 is connected with a first feed port of a stirrer through a pipeline, and a glaze pumping pump 13 and a flowmeter 14 are arranged on the pipeline. Fig. 2 shows a dry particle feeding device structure, which includes a storage bin 21, a storage bin valve is arranged at the discharge outlet of the storage bin 21, the discharge outlet of the storage bin 21 is connected with the feed inlet of a weighing hopper 23, a screw propeller 24 and an electronic scale 25 are arranged at the discharge outlet of the weighing hopper 23, and the discharge outlet of the screw propeller 24 is connected with the second feed inlet of the stirrer.
The controller can be a singlechip, a computer, a mobile phone and the like, and controls the addition amount of the suspending agent, the addition amount of the dry particles and the working state of the stirrer. The flow meter 14 is used for monitoring the adding amount of the suspending agent added into the stirrer in real time and feeding back the adding amount to the controller, and the controller controls the work of the glaze pumping pump 13 according to the monitoring data of the flow meter 14, so that the adding amount of the suspending agent is controlled. The adding amount of the dry granules is monitored in real time by using an electronic scale 25 and fed back to the controller, and the controller controls the opening and closing of the corresponding storage bin valve and the operation of the screw propeller 24 according to the monitoring data of the electronic scale 25, thereby controlling the adding amount of the dry granules.
The dry grain glaze feeding device adds the different types of dry grains of splendid attire in the agitator and stirs and mixes, and its number is 1 at least, and this embodiment chooses for use and figure 4 in the same dry grain feeding device that is 3 of number. The controller controls the dry particle feeding device to add different types of dry particles and adding amount into the stirrer according to different types of dry particle glazes to be processed, and controls the suspending agent feeding device to add suspending agent into the stirrer.
In the embodiment, the addition amount of the suspending agent and the addition amount of the dry particles are controlled by using the controller, so that the accuracy of the dry particle glaze processing and batching is improved, and the error of batching is controlled within 0.1% each time. When the suspending agent and the dry particles are controlled by the controller to be added into the stirrer to process the dry particle glaze, the stirrer is started to stir, namely, the material mixing and the stirring are carried out simultaneously, so that the processing time is shortened, 15 tons of dry particle glaze can be processed per hour, and the processing efficiency of the dry particle glaze is improved.
Example 2
On the basis of embodiment 1, the stirrer is preferably in a stirrer structure as shown in fig. 3, the top of the stirrer is externally connected with a stirring motor 31, one end of a stirring shaft in the stirrer is connected with the stirring motor, the other end of the stirring shaft extends to the bottom of the stirrer, a stirring blade 35 is arranged on the stirring shaft, a glaze outlet 34 is arranged at the bottom of the stirrer, and a glaze outlet valve 33 is arranged on the stirring shaft. In the ceramic dry particle glaze batch mixing device of the embodiment, when in use, it is found that dry particles are often stacked on the stirring blade 35, and in order to solve the problem, the stirring blade 35 is preferably designed to have an inverted V-shaped structure, so that the dry particles are prevented from being stacked on the stirring blade 35 during charging and stirring.
Example 3
Considering that the ceramic dry-particle glaze batch mixing device may include a plurality of dry-particle feeding devices, if the discharge port of each dry-particle feeding device is directly aligned with the second feeding port of the stirrer, the second feeding port of the stirrer may be oversized, and the whole ceramic dry-particle glaze batch mixing device may be quite large, and the occupied space may be quite large, based on this, as shown in fig. 4, the ceramic dry-particle glaze batch mixing device of this embodiment is based on embodiment 1 or 2, and is additionally provided with a conveyor belt 26 and a feeding hopper 38, the feeding hopper 38 is connected with the second feeding port of the stirrer, the conveyor belt 26 receives the dry particles pushed by the screw 24 in the dry-particle feeding device, and conveys the dry particles into the feeding hopper 38. The dry particle feeding devices are respectively arranged on one side or two sides of the conveying belt 26, and preferably, each dry particle feeding device is respectively arranged on two sides of the conveying belt 26, so that the space occupied by the ceramic dry particle glaze batch mixing device can be further reduced.
Example 4
On the basis of the previous embodiment, in order to stir the suspending agent and the dry particles more uniformly, in this embodiment, as shown in fig. 4, a differential mechanism 32 is additionally arranged on the stirrer, two ends of the differential mechanism 32 are respectively connected with a stirring motor 31 and a stirring shaft, the controller controls the stirring shaft to use different rotation speeds through the differential mechanism 32 according to different types of the dry particle glaze to be processed, and further controls the stirring blades 35 to use different rotation speeds, so that the stirring is more sufficient. In order to further enable the stirring to be more uniform, an air inlet 36 and an air inlet valve 37 are additionally arranged at the bottom of a stirrer in the ceramic dry particle glaze batch mixing device, and the air inlet 36 is connected with a blower through an air pipe. When the stirrer is started, the blower is started to blow air, the blower blows air to flow from the bottom to the top of the stirrer, and the air and the stirring blades 35 are stirred and matched to form upward stirring force, so that stirring is more uniform.
Example 5
In this embodiment, in addition to the previous embodiments, in order to reduce the amount of dust generated when the ceramic dry glaze batch mixing device is used for the health of the user, soft connecting pipes 22 are additionally arranged at the dry particle transfer positions of the dry particle feeding device, and the soft connecting pipes 22 are additionally arranged between the storage bin 21 and the weighing hopper 23 and between the weighing hopper and the screw propeller 24. In order to facilitate observation of the condition of dry glaze particles stirred by the stirrer, the observation window 39 is additionally arranged at the top of the stirrer, so that the stirring state can be conveniently observed.
When the ceramic dry particle glaze batch mixing device is used, firstly, a slurry storage tank valve 12 and a glaze outlet valve 33 are closed, a suspending agent slurry storage tank 11 is filled with a suspending agent to be stirred, each storage bin 21 is filled with dry particles of corresponding types to be stirred, a controller is used for selecting the types and the processing quantity of the processed dry particle glaze or directly inputting the adding quantity of the preprocessed suspending agent and the adding quantity of the preprocessed dry particles of various types, an air inlet valve 37 is opened, a blower is started, a slurry storage tank valve 12 is opened, the ceramic dry particle glaze batch mixing device is started, the controller controls a glaze pumping pump 13 to start working, the suspending agent is added into a stirrer, meanwhile, a flowmeter 14 is used for monitoring the adding amount of the suspending agent, and the glaze pumping pump 13 stops working after the adding amount of the suspending agent reaches the input quantity.
The stirring motor 31 drives the stirring blade 35 to rotate through the stirring shaft, and an upward stirring force is formed in the stirrer through the rotation of the stirring blade 35 and the blowing of the gas. After the stirring motor 31 starts working for several minutes, the conveyor belt 26 is opened, the controller controls the storage bin valve 22 to be opened, the dry granules stored in the storage bin 21 enter the weighing hopper 23, the electronic scale 25 monitors the weight of the dry granules in the weighing hopper 23 in real time, when the dry granules in the weighing hopper 23 reach an input value, the storage bin valve 22 is closed, the spiral propeller 24 pushes the dry granules in the weighing hopper 23 to the conveyor belt 26, and the dry granules enter the stirrer through the feed hopper 38 to be stirred and mixed. When the weighing hopper 23 is full of dry granules, but the dry granule amount does not reach the input numerical value at the moment, the controller can control the storage bin valve 22 to close, the spiral propeller 24 pushes the dry granules in the weighing hopper 23 to the conveyor belt 26, after the dry granules in the weighing hopper 23 are all emptied, the controller controls the storage bin valve 22 to open, the dry granules continue to enter the weighing hopper 23, the operation is repeated, and the controller controls the storage bin valve 22 to close until the adding amount is accumulated to reach the input preprocessing dry granule amount value. The pellets to be dried are all fed into the mixer via auger 24 and conveyor 26 and the batching system is shut down. The batching system controls the opening and closing of the storage bin valve by the numerical value input by the controller and controls the closing of the batching system so as to control the adding amount of various dry particles. When the batching system is closed, the stirring blade is continuously kept rotating and stirring and blowing of the blower are continuously carried out for 10-30 minutes, preferably 20 minutes, stirring and mixing are carried out, and after uniform stirring, the air inlet valve 37 is closed. When dry granular glaze is needed to be used, the glaze outlet valve 33 is opened, and glaze is loaded from the glaze outlet 34 and transported to a production line for use.
Example 6
Fig. 5 is a flowchart of a batch mixing method for dry ceramic glaze particles according to an embodiment of the present invention, which includes the following specific steps:
s100, a suspending agent slurry storage tank 11 is used for containing suspending agents to be stirred, a storage bin 21 is used for containing dry particles of corresponding varieties to be stirred, the number of the storage bins is N, and N is larger than or equal to 1.
And closing the slurry storage tank valve 12 and the glaze outlet valve 33, wherein the suspending agent slurry storage tank 11 is filled with the suspending agent to be stirred, and each storage bin 21 is filled with the dry particles of the corresponding variety to be stirred.
S200, the controller receives the addition value of the suspension agent for preprocessing and the addition value of dry particles for preprocessing of various varieties.
The variety and the processing value of the dry grain glaze to be processed are selected by a controller or the addition value of the suspension agent to be preprocessed and the addition value of the dry grains of each variety to be preprocessed are directly input by the controller.
S300, the ceramic dry particle glaze batch mixing device receives a starting instruction, the controller controls the glaze pumping pump 13 to start working to add a suspending agent into the stirrer, and the controller opens the corresponding storage bin valve and controls the corresponding spiral propeller 24 to start working according to the addition quantity value of each variety of dry particles to be preprocessed, and starts the stirrer to start working to stir and mix.
Opening a valve 12 of a slurry storage tank, receiving a starting instruction by a ceramic dry grain glaze batch mixing device to start working, controlling a glaze pumping pump 13 to start working by a controller, adding a suspending agent into a stirrer, simultaneously monitoring the added suspending agent amount by using a flowmeter 14, opening a corresponding storage bin valve by the controller according to the adding amount of the dry grains of each preprocessed variety, enabling the dry grains stored in a storage bin 21 to enter a weighing hopper 23, monitoring the weight of the dry grains in the weighing hopper 23 in real time by using a corresponding electronic scale 25, controlling a corresponding spiral propeller 24 to start working, and adding the dry grains into the stirrer. At the same time as the suspending agent and dry pellets begin to be added to the mixer, the mixer is started to operate for mixing.
And S400, when the addition amount of the suspending agent is equal to the addition amount of the suspension agent to be preprocessed, the controller controls the glaze pumping pump 13 to stop working, and when the addition amount of the dry particles is equal to the addition amount of the dry particles to be preprocessed, the controller closes the corresponding storage bin valve and controls the corresponding spiral propeller 24 to stop working.
When the added suspending agent amount monitored by the flow meter 14 is equal to the added amount of the preprocessed suspending agent, the controller controls the glaze pumping pump 13 to stop working, the suspending agent is stopped being added into the stirrer, when the added dry particle amount monitored by the electronic scale 25 is equal to the added amount of the preprocessed dry particle, the corresponding storage bin valve is closed, the corresponding screw propeller 24 is controlled to stop working, and the dry particle is stopped being added into the stirrer.
S500, when the glaze pumping pump 13 stops working, all the storage bin valves are closed, all the spiral propellers stop working, the stirrer continues to be kept to stir and mix, and after the materials are uniformly stirred, the stirrer stops working.
When the glaze pumping pump 13 stops working, all the storage bin valves are closed, and all the screw propellers stop working, the stirrer is continuously kept to stir and mix for 10-30 minutes, preferably for 20 minutes, and after the materials are uniformly stirred, the stirrer stops working.
Example 7
This example is substantially the same as example 6, except that: in the step S300, when the stirrer is started, the blower is started to blow gas to flow from the bottom to the top of the stirrer, so that upward stirring force is formed, and the stirring is more uniform; in the step S500, when the glaze pumping pump 13 stops working, all the storage bin valves are closed, and all the screw propellers stop working, the stirrer is continuously kept stirring and the blower is continuously blown for 10 to 30 minutes, preferably 20 minutes, stirring and mixing are carried out, and after the stirring is uniform, the stirrer and the blower stop working.
The above embodiments are preferred embodiments of the present invention, but the present invention is not limited to the above embodiments, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be construed as equivalents thereof, and all such changes, modifications, substitutions, combinations, and simplifications are intended to be included in the scope of the present invention.
Claims (10)
1. A ceramic dry particle glaze batch mixing device is characterized by comprising: a suspending agent feeding device, a dry particle feeding device, a stirrer and a controller;
the suspension agent feeding device comprises a suspension agent slurry storage tank (11), a discharge hole of the suspension agent slurry storage tank (11) is connected with a first feed hole of the stirrer through a pipeline, and a glaze pumping pump (13) and a flowmeter (14) are arranged on the pipeline;
the dry particle feeding device comprises a storage bin (21), a storage bin valve is arranged at a discharge port of the storage bin (21), a discharge port of the storage bin valve is connected with a feed port of a weighing hopper (23), a spiral propeller (24) and an electronic scale (25) are arranged at the discharge port of the weighing hopper (23), and the discharge port of the spiral propeller (24) is connected with a second feed port of the stirrer;
the number of the dry particle feeding devices is N, the dry particle feeding devices are used for containing different types of dry particles, and N is more than or equal to 1;
the controller controls the work of the glaze pumping pump (13) so as to control the adding amount of the suspending agent, controls the switch of the storage bin valve and the work of the spiral propeller (24) so as to control the adding amount of the dry granules, and controls the working state of the stirrer.
2. The ceramic dry glaze batch mixing device according to claim 1, further comprising a conveyor belt (26) and a feed hopper (38), wherein the feed hopper (38) is connected with the second feed port of the stirrer, and the conveyor belt (26) receives the dry glaze particles pushed by the screw propeller (24) and conveys the dry glaze particles into the feed hopper (38).
3. The ceramic dry glaze batch mixing device according to claim 2, wherein the dry feeding means are respectively provided on one side or both sides of the conveyor belt (26).
4. The ceramic dry-particle glaze batch mixing device according to claim 1, wherein a stirring motor (31) is externally connected to the top of the stirrer, a stirring shaft is arranged in the stirrer, one end of the stirring shaft is connected with the stirring motor (31), the other end of the stirring shaft extends towards the bottom of the stirrer, and a stirring blade (35) is arranged on the stirring shaft.
5. The ceramic dry glaze batch mixing device of claim 4, wherein the stirring blade has an inverted V-shaped structure.
6. The ceramic dry-particle glaze batch mixing device according to claim 5, further comprising a differential (32), wherein two ends of the differential (32) are respectively connected with the stirring motor (31) and the stirring shaft, and the controller controls the rotation speed of the stirring shaft through the differential (32) according to different types of the dry-particle glaze to be processed, so as to control the rotation speed of the stirring blades (35).
7. The ceramic dry-particle glaze batch mixing device according to any one of claims 1 to 6, wherein the bottom of the stirrer is further provided with a gas inlet (36) and a gas inlet valve (37), the gas inlet (36) is connected with a blower through a gas pipe, and the blower blows gas to flow from the bottom to the top of the stirrer.
8. The ceramic dry-particle glaze batch mixing device according to claim 7, wherein the dry-particle feeding device further comprises a soft connecting pipe, and two ends of the soft connecting pipe are respectively connected with the discharge hole of the storage bin (21) and the feed hole of the weighing hopper (23).
9. A ceramic dry-grain glaze batch mixing method using the ceramic dry-grain glaze batch mixing device according to claim 1 or claim 7, characterized by comprising the steps of:
s1, a suspending agent slurry storage tank (11) is used for containing suspending agents to be stirred, a storage bin (21) is used for containing dry particles of corresponding varieties to be stirred, the number of the storage bins is N, and N is larger than or equal to 1;
s2, the controller receives the addition value of the suspension agent for preprocessing and the addition value of the dry particles for preprocessing;
s3, the ceramic dry particle glaze batch mixing device receives a starting instruction, the controller controls the glaze pumping pump (13) to start working to add the suspending agent into the stirrer, and the controller opens the corresponding storage bin valve and controls the corresponding spiral propeller (24) to start working according to the addition amount of each variety of dry particles to be preprocessed, and starts the stirrer to start working to stir and mix;
s4, when the addition amount of the suspending agent is equal to the addition amount of the suspension agent to be preprocessed, the controller controls the glaze pumping pump (13) to stop working, and when the addition amount of the dry particles is equal to the addition amount of the dry particles to be preprocessed, the controller closes the corresponding storage bin valve and controls the corresponding spiral propeller (24) to stop working;
and S5, when the glaze pumping pump (13) stops working, all the storage bin valves are closed, all the spiral propellers stop working, the stirrer continues to stir and mix, and after the materials are uniformly stirred, the stirrer stops working.
10. The batch mixing method for ceramic dry-grain glaze according to claim 9, wherein in the step S3, the stirrer is started and the blower is started, the blower blows the gas from the bottom to the top of the stirrer, and in the step S5, the stirrer and the blower are stopped simultaneously.
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204522838U (en) * | 2015-01-22 | 2015-08-05 | 新疆科能防水防护材料有限公司 | Special interface agent automatic mixing production system |
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| CN208526534U (en) * | 2018-05-07 | 2019-02-22 | 江西和美陶瓷有限公司 | A kind of coloring material for mixing system |
| CN211546427U (en) * | 2019-12-03 | 2020-09-22 | 河南博海化工有限公司 | Pitch processingequipment |
| CN213966371U (en) * | 2020-08-06 | 2021-08-17 | 淮滨锦绣江淮现代农业有限公司 | Mixing mechanism for producing bulk blend fertilizer |
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| CN204522838U (en) * | 2015-01-22 | 2015-08-05 | 新疆科能防水防护材料有限公司 | Special interface agent automatic mixing production system |
| CN105233731A (en) * | 2015-11-17 | 2016-01-13 | 重庆市渝派农产品开发有限公司 | Dried tofu stirring device with automatic feeding function |
| CN206911196U (en) * | 2017-07-10 | 2018-01-23 | 王小改 | A kind of high security autocontrol mixer |
| CN107790036A (en) * | 2017-12-18 | 2018-03-13 | 沈晓杰 | A kind of cosmetics powder mixing device |
| CN208526534U (en) * | 2018-05-07 | 2019-02-22 | 江西和美陶瓷有限公司 | A kind of coloring material for mixing system |
| CN211546427U (en) * | 2019-12-03 | 2020-09-22 | 河南博海化工有限公司 | Pitch processingequipment |
| CN213966371U (en) * | 2020-08-06 | 2021-08-17 | 淮滨锦绣江淮现代农业有限公司 | Mixing mechanism for producing bulk blend fertilizer |
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