CN211077122U - Automatic powder material jar of unloading - Google Patents

Automatic powder material jar of unloading Download PDF

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Publication number
CN211077122U
CN211077122U CN201921195266.0U CN201921195266U CN211077122U CN 211077122 U CN211077122 U CN 211077122U CN 201921195266 U CN201921195266 U CN 201921195266U CN 211077122 U CN211077122 U CN 211077122U
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fluidized bed
main
powder material
inlet pipe
automatic discharging
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CN201921195266.0U
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张思杭
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Zhejiang Chaoyu Automobile Technology Co ltd
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Zhejiang Chaoyu Automobile Technology Co ltd
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Abstract

Automatic powder material jar of unloading belongs to the technical field of semitrailer material jar, including a jar body and controller, jar body top is equipped with a plurality of feed ports and pressure sensor, its characterized in that: jar body bottom central authorities are equipped with the mainstream fluidized bed, the mainstream fluidized bed both sides are equipped with side fluidized bed, side fluidized bed extends and the downward sloping from jar body both ends to the mainstream fluidized bed, the mainstream fluidized bed passes through main intake-tube connection total intake pipe, be equipped with main admission valve in the main intake pipe, side fluidized bed passes through vice intake-tube connection total intake pipe, be equipped with vice admission valve in the vice intake pipe, total intake-tube connection air compressor machine, air compressor machine connection director, the mainstream fluidized bed top is equipped with the perforated plate, is equipped with level sensor and discharge tube on the perforated plate, is equipped with discharge valve and flow sensor on the discharge tube, the utility model discloses full automatic discharge has improved the efficiency of.

Description

Automatic powder material jar of unloading
Technical Field
The utility model relates to a semitrailer material tank's technical field, concretely relates to automatic powder material tank of unloading.
Background
The powder particle material semi-trailer tank car is manually operated to unload materials for decades, is used for more than 60 years in China, and adopts a unified (single V, double V and triple V) fluidized bed, a material sliding plate, an air chamber and the like in the tank structure. Adopt main trachea and discharge tube and manual valve to constitute etc. outside the jar, explain according to (single V) semi-mounted jar, the basic structure of a manual discharge valve and main air valve, can't master the fluidization density after material and the air mixing at the in-process of unloading, it is many to produce the clout after unloading simultaneously, the easy accident of manual operation (high temperature is scalded operator's hand), the biggest problem is that the time of unloading is long, the air chamber around the tracheal high-pressure gas of main of traditional material car jar body will advance, the gas in the air chamber reentries the gas zone, the strength of gas just so has reduced naturally, thereby reduced fluidization strength, lead to the process of unloading consuming time power, and the emission is big, environmental pollution is serious.
SUMMERY OF THE UTILITY MODEL
The utility model provides an automatic powder material jar of unloading aims at solving among the prior art problem that the semitrailer jar body is unloaded for a long time, the clout is many, manual operation security is poor.
The utility model discloses a solve above-mentioned technical problem, adopt following technical scheme to realize:
The utility model provides an automatic powder material jar of unloading, which comprises a tank body and a controller, jar body top is equipped with a plurality of feed ports and pressure sensor, jar body bottom central authorities are equipped with the mainstream fluidized bed, the mainstream fluidized bed both sides are equipped with side fluidized bed, side fluidized bed extends and the downward sloping to the mainstream fluidized bed from jar body both ends, the mainstream fluidized bed passes through main intake-tube connection total intake pipe, be equipped with main admission valve in the main intake-tube, side fluidized bed passes through vice intake-tube connection total intake pipe, be equipped with vice admission valve in the vice intake-tube, total intake-tube connection air compressor machine, air compressor machine connection director, the mainstream fluidized bed top is fluidization cloth, the top is equipped with the perforated plate, the edge is equipped with level sensor, mainstream fluidized bed center.
Preferably, the main fluidized bed is fixed on a vehicle and is lower than the tank body, air holes are distributed on the fluidized cloth of the main fluidized bed, and the bottom of the main fluidized bed is connected with the main air inlet pipe.
Preferably, the secondary fluidized bed consists of a plurality of branch gas belts, branch gas holes are distributed on the branch gas belts, the outer ends of the branch gas belts are connected with the secondary gas inlet pipe, and the inner ends of the branch gas belts are fixedly connected with the edge of the main fluidized bed.
Preferably, the opening of the suction port of the discharge pipe is downward or upward.
Preferably, the distance between the suction port of the discharge pipe and the main fluidized bed is 5-10cm,
Preferably, the main air inlet pipe is provided with an external air source pipeline, and the external air source pipeline is provided with an external air source valve.
Preferably, the main air inlet pipe is provided with a one-way valve and a pressure regulating valve.
Preferably, the top of the tank body is provided with an exhaust valve.
Preferably, a secondary air supply pipe is arranged between the main air inlet pipe and the discharge pipe, and the secondary air supply pipe is provided with a secondary air supply valve.
Preferably, the perforated plate is distributed with material holes.
Compared with the prior art, the beneficial effects of the utility model are that:
1. The unloading time is short, and the unloading is thorough: the gas in the mainstream fluidized bed directly gets into from main intake pipe, then flow from the gas pocket at mainstream fluidized bed top, get into the main storehouse rapidly, make the material fluidize rapidly and main storehouse atmospheric pressure increase, the high-pressure gas of vice intake pipe gets into the branch gas zone of side fluidized bed, then flow from the branch gas pocket of branch gas zone, get into the main storehouse rapidly, make the material fluidization, under the effect of side fluidized bed slope, make the material flow to the mainstream fluidized bed rapidly, discharge by the discharge tube, it is efficient to unload, more than 30% faster than traditional discharge can, the time of unloading has been saved, and it is very thorough to unload, almost there is not the clout.
2. Degree of automation is high, uses manpower sparingly, improves the security: the flow sensor, the pressure sensor and the level sensor are adopted in the discharging process to sense the flow, the pressure and the material height in the discharging process, and even if sensing signals are transmitted to the controller, the controller controls each valve to work, so that the flow and the density of the material in the discharging process are accurately controlled, the purpose of full-automatic discharging is achieved, manual operation is reduced, and workers are prevented from being injured.
3. Energy conservation and environmental protection: because the unloading time is short, the working time of the equipment is reduced, and the energy consumption and the emission of harmful gas are correspondingly reduced, thereby achieving the purposes of energy conservation and emission reduction.
Drawings
The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention, and together with the description serve to explain the invention and not to limit the invention.
In the drawings:
FIG. 1 is a schematic structural view of example 1;
FIG. 2 is a top plan view of the primary and secondary fluidized beds of FIG. 1;
FIG. 3 is an enlarged view of a portion of FIG. 2 at A;
FIG. 4 is a schematic structural view of embodiment 2;
FIG. 5 is a schematic structural view of example 3;
FIG. 6 is a schematic structural view of example 4;
FIG. 7 is a schematic structural view of example 5.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Example 1
As shown in fig. 1-3: a powder material tank capable of automatically discharging comprises a tank body 1 and a controller 8, wherein the top of the tank body 1 is provided with a plurality of feeding holes 101 and a pressure sensor 102, the center of the bottom of the tank body 1 is provided with a main fluidized bed 2, two sides of the main fluidized bed 2 are provided with auxiliary fluidized beds 3, the auxiliary fluidized beds 3 extend from two ends of the tank body 1 to the main fluidized bed 2 and incline downwards, the main fluidized bed 2 is connected with a main air inlet pipe 4 through a main air inlet pipe 201, the main air inlet pipe 201 is provided with a main air inlet valve 202, the auxiliary fluidized beds 3 are connected with a main air inlet pipe 4 through an auxiliary air inlet pipe 301, the auxiliary air inlet pipe 301 is provided with an auxiliary air inlet valve 302, the main air inlet pipe 4 is connected with an air compressor 7, the air compressor 7 is connected with the controller 8, the top of the main fluidized bed 2 is provided with fluidized, the main fluidized bed 2 is fixed on a vehicle and is lower than the tank body 1, air holes are distributed on the fluidized cloth of the main fluidized bed 2, the bottom of the main fluidized bed 2 is connected with a main air inlet pipe 201, the side fluidized bed 3 is composed of a plurality of air supporting belts 303, the air supporting belts 303 are distributed with the air supporting holes, the outer ends of the air supporting belts 303 are connected with an auxiliary air inlet pipe 301, the inner ends of the air supporting belts are fixedly connected with the edge of the main fluidized bed 2, the opening of a suction port 501 of the discharge pipe 5 is downward or upward, the distance between the suction port 501 of the discharge pipe 5 and the main fluidized bed 2 is 5-10cm, the main air inlet pipe 4 is provided with an external air source pipeline 404, the external air source pipeline 404 is provided with an external air source valve 403, the main air inlet pipe 4 is provided with a one-way valve 401 and a pressure regulating valve 402, the top of the tank body, the perforated plate 203 is distributed with material holes.
In this embodiment, the air compressor 7 supplies air to the main air inlet pipe 4, the main air inlet valve 202 is opened, high-pressure air enters the main fluidized bed 2 from the main air inlet pipe 201, then flows out from the air hole at the top of the main fluidized bed 2, and quickly enters the main bin of the tank body, so that the material is quickly fluidized and the air pressure of the main bin is increased, the auxiliary air inlet valve 302 is opened, high-pressure air enters the branch air zone 303 of the auxiliary fluidized bed 3 from the auxiliary air inlet pipe 301, then flows out from the branch air hole of the branch air zone 303, and quickly enters the main bin of the tank body, so that the material is fluidized, because the auxiliary fluidized bed 3 inclines downwards from two ends to the main fluidized bed 2, the material is quickly flowed to the main fluidized bed 2, is sucked and discharged from the suction port 501 of the discharge pipe 5, the discharge process is completed, the discharge valve 502 controls the discharge pipe to be closed and opened, the flow sensor monitors, when the pressure in the air compressor is higher than a set value, the air is automatically exhausted to guarantee safety, the external air source pipeline 404 is used as a standby air source, when the air compressor cannot work normally, the air compressor can be connected into the standby air source to guarantee the completion of unloading, the unloading speed is increased through the secondary air supply pipe 6, the pressure sensor 102 monitors the pressure of the tank body, and the air in the tank body is exhausted through the air exhaust valve 103.
Example 2
As shown in fig. 4, two sets of the main fluidized bed 2 and the secondary fluidized bed 3 as in embodiment 1 are arranged in the same tank 1, and corresponding pipes, valves and material sensors are arranged, so that the discharging time can be further shortened, and the discharging efficiency can be improved.
Example 3
As shown in fig. 5, three sets of the main fluidized bed 2 and the sub-fluidized bed 3 in the embodiment 1 are adopted in the same tank 1, and corresponding pipelines, valves and material sensors are arranged, so that the discharging time can be further shortened, and the discharging efficiency can be improved.
Example 4
As shown in fig. 6, the tank 1 is divided into two independent bins by the partition board 9, the main fluidized bed 2 and the auxiliary fluidized bed 3 are respectively arranged as in embodiment 1, and corresponding pipelines, valves, material sensors, pressure sensors and exhaust valves are arranged, so that the unloading time can be further shortened, the unloading efficiency can be improved, and the unloading can be independently controlled.
Example 5
As shown in fig. 7, the partition 9 divides the tank 1 into three independent bins, and the arrangement of the main fluidized bed 2 and the auxiliary fluidized bed 3 in embodiment 1 is adopted, and corresponding pipelines, valves, material sensors, pressure sensors and exhaust valves are arranged, so that the unloading time can be further shortened, the unloading efficiency can be improved, and the unloading can be independently controlled.
The above description is only exemplary of the present invention and should not be construed as limiting the present invention, and any modifications, equivalents and improvements made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.

Claims (10)

1. The utility model provides an automatic powder material jar of unloading, includes a jar body and a controller, and jar body top is equipped with a plurality of feed ports and pressure sensor, its characterized in that: the utility model discloses a fluidized bed, including a jar body, a main air inlet pipe, an auxiliary air inlet pipe, an air compressor connection controller, fluidization cloth, the top is equipped with the perforated plate, the edge is equipped with level sensor, the main fluidized bed center top is equipped with the discharge tube, be equipped with discharge valve and flow sensor on the discharge tube.
2. The automatic discharging powder material tank as claimed in claim 1, wherein: the main fluidized bed is fixed on the vehicle and is lower than the tank body, air holes are distributed on the fluidized cloth of the main fluidized bed, and the bottom of the main fluidized bed is connected with the main air inlet pipe.
3. The automatic discharging powder material tank as claimed in claim 1, wherein: the auxiliary fluidized bed consists of a plurality of branch gas belts, branch gas holes are distributed on the branch gas belts, the outer ends of the branch gas belts are connected with the auxiliary gas inlet pipe, and the inner ends of the branch gas belts are fixedly connected with the edge of the main fluidized bed.
4. The automatic discharging powder material tank as claimed in claim 1, wherein: and the opening of the material suction port of the discharge pipe is downward or upward.
5. The automatic discharging powder material tank as claimed in claim 4, wherein: and the distance between the material suction port of the discharge pipe and the main fluidized bed is 5-10 cm.
6. The automatic discharging powder material tank as claimed in claim 1, wherein: the main air inlet pipe is provided with an external air source pipeline, and the external air source pipeline is provided with an external air source valve.
7. The automatic discharging powder material tank as claimed in claim 1, wherein: the main air inlet pipe is provided with a one-way valve and a pressure regulating valve.
8. The automatic discharging powder material tank as claimed in claim 1, wherein: an exhaust valve is arranged at the top of the tank body.
9. The automatic discharging powder material tank as claimed in claim 1, wherein: and a secondary air supply pipe is arranged between the main air inlet pipe and the discharge pipe, and is provided with a secondary air supply valve.
10. The automatic discharging powder material tank as claimed in claim 1, wherein: and material holes are distributed on the perforated plate.
CN201921195266.0U 2019-07-27 2019-07-27 Automatic powder material jar of unloading Active CN211077122U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921195266.0U CN211077122U (en) 2019-07-27 2019-07-27 Automatic powder material jar of unloading

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Application Number Priority Date Filing Date Title
CN201921195266.0U CN211077122U (en) 2019-07-27 2019-07-27 Automatic powder material jar of unloading

Publications (1)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110482038A (en) * 2019-07-27 2019-11-22 浙江超宇汽车科技有限公司 A kind of particle material tank of automatic discharging
CN113562466A (en) * 2021-09-26 2021-10-29 山东万邦石油科技股份有限公司 Bulk material tank for transport ship
CN115710078A (en) * 2022-11-07 2023-02-24 江苏和合水环境有限公司 Bath mud drying pretreatment device and treatment method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110482038A (en) * 2019-07-27 2019-11-22 浙江超宇汽车科技有限公司 A kind of particle material tank of automatic discharging
CN113562466A (en) * 2021-09-26 2021-10-29 山东万邦石油科技股份有限公司 Bulk material tank for transport ship
CN115710078A (en) * 2022-11-07 2023-02-24 江苏和合水环境有限公司 Bath mud drying pretreatment device and treatment method thereof
CN115710078B (en) * 2022-11-07 2024-03-01 江苏和合水环境有限公司 Algae mud drying pretreatment device and treatment method thereof

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