CN210392528U - Viscous granular material continuous conveying device - Google Patents
Viscous granular material continuous conveying device Download PDFInfo
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- CN210392528U CN210392528U CN201921230610.5U CN201921230610U CN210392528U CN 210392528 U CN210392528 U CN 210392528U CN 201921230610 U CN201921230610 U CN 201921230610U CN 210392528 U CN210392528 U CN 210392528U
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Abstract
The utility model provides a granular material continuous feeding device of stickness, include: the conveying cover is provided with a feeding hole, the bottom of the conveying cover is provided with a discharging hole, a conveying belt driven by a first power device to rotate is horizontally installed in the conveying cover, and the conveying belt receives materials at the feeding hole and conveys the materials to the discharging hole; the conveying cover is communicated with the air box through the cooling air inlet pipe, the air box is communicated with the air blowing device, the viscous granular materials enter the conveying cover from the feeding hole and fall onto the conveying belt, and in the conveying process, the conveying belt is used for prolonging the cooling time of the viscous granular materials, so that the cooling effect is improved; meanwhile, cold air is blown into the conveying cover through the air blowing device to cool, the conveying belt is not easy to adhere in the conveying process, and continuous conveying operation of sticky granular materials can be realized.
Description
Technical Field
The utility model belongs to the technical field of the special defeated material equipment of stickness material technique and specifically relates to a granular material continuous feeding device of stickness.
Background
The mode of horizontal transport is mostly adopted to stickness high temperature granular material in transportation process in the past, but the mode of horizontal transport, stickness material very easily bonds on the conveyer belt to influence the continuous transportation of stickness material.
Also some are through the cooling earlier before carrying, reduce the viscosity of stickness material, then transport the material and collect, get into drying process after the collection completion and dry the stickness material again. However, this method is complicated in process, cannot achieve continuous operation, and is low in efficiency.
SUMMERY OF THE UTILITY MODEL
The utility model provides a granular material continuous feeding device of stickness should not cohere the conveyer belt in the transportation process, and can realize the continuous conveyor operation.
The technical scheme of the utility model is realized like this:
viscous granular material continuous conveying device, comprising: the conveying cover is provided with a feeding hole, the bottom of the conveying cover is provided with a discharging hole, a conveying belt driven by a first power device to rotate is horizontally installed in the conveying cover, and the conveying belt receives materials of the feeding hole and conveys the materials to the discharging hole;
the conveying cover is communicated with an air box through a cooling air inlet pipe, and the air box is communicated with a blowing device.
As an improvement mode, the conveying cover is also communicated with the air box through a cooling air outlet pipe;
install heat exchanger on the cooling outlet duct, heat exchanger includes the casing, the cooling outlet duct runs through the casing, the upper end of casing is provided with the coolant liquid inlet, the lower extreme of casing is provided with the coolant liquid outlet.
As an improvement mode, the number of the conveying belts is three, and the three conveying belts are arranged in a staggered mode; and the conveying directions of two adjacent conveying belts are opposite.
As an improved mode, a spiral conveying device is installed at the discharge port, the spiral conveying device comprises a conveying cylinder, one end of the conveying cylinder is provided with a conveying inlet communicated with the discharge port, and the other end of the conveying cylinder is provided with a conveying outlet; and a conveying shaft driven by a second power device is rotatably mounted in the conveying cylinder, and a spiral conveying blade is mounted on the conveying shaft.
As a refinement, the delivery inlet is located below the delivery outlet.
By adopting the technical scheme, the beneficial effects of the utility model are that:
viscous granular material continuous conveying device, comprising: the conveying cover is provided with a feeding hole, the bottom of the conveying cover is provided with a discharging hole, a conveying belt driven by a first power device to rotate is horizontally installed in the conveying cover, and the conveying belt receives materials at the feeding hole and conveys the materials to the discharging hole; the conveying cover is communicated with the air box through the cooling air inlet pipe, the air box is communicated with the air blowing device, the viscous granular materials enter the conveying cover from the feeding hole and fall onto the conveying belt, and in the conveying process, the conveying belt is used for prolonging the cooling time of the viscous granular materials, so that the cooling effect is improved; meanwhile, cold air is blown into the conveying cover through the air blowing device to cool, the conveying belt is not easy to adhere in the conveying process, and continuous conveying operation of sticky granular materials can be realized.
The conveying cover is also communicated with the air box through a cooling air outlet pipe; install heat exchanger on the cooling outlet duct, heat exchanger includes the casing, and the cooling outlet duct runs through the casing, and the upper end of casing is provided with the coolant liquid inlet, and the lower extreme of casing is provided with the coolant liquid outlet, utilizes the coolant liquid to carry out the heat transfer back to the cooling outlet duct, and the cold wind in the cooling outlet duct reentries bellows circulation, has further promoted the cooling effect.
Three conveying belts are arranged in a staggered manner; and the conveying directions of the two adjacent conveying belts are opposite, so that the conveying distance is prolonged, the cooling time is prolonged, the cooling effect on sticky granular materials is improved, and the stickiness is reduced.
The spiral conveying device is arranged at the discharge port and comprises a conveying cylinder, one end of the conveying cylinder is provided with a conveying inlet communicated with the discharge port, and the other end of the conveying cylinder is provided with a conveying outlet; the conveying shaft driven by the second power device is rotatably installed in the conveying cylinder, the conveying shaft is provided with spiral conveying blades, and viscous powdery materials are conveyed by the spiral conveying device and are sealed and leak-free in the whole process.
The conveying inlet is positioned at the lower part of the conveying outlet, so that the position of the conveying outlet is lifted, and a transfer trolley is conveniently placed under the conveying outlet, thereby being beneficial to the continuous transfer of the viscous granular materials.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be 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 can be obtained according to these drawings without inventive exercise.
Fig. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic structural view of the screw conveyor of the present invention;
wherein: 1-conveying cover, 2-feeding hole, 3-discharging hole, 4-first power device, 5-first conveying belt, 6-second conveying belt, 7-third conveying belt, 8-viscous granular material, 9-cooling air inlet pipe, 10-air box, 11-air blowing device, 12-cooling air outlet pipe, 13-heat exchanger, 14-shell, 15-cooling liquid inlet, 16-cooling liquid outlet, 17-spiral conveying device, 18-conveying cylinder, 19-conveying inlet, 20-conveying outlet, 21-second power device, 22-conveying shaft, 23-spiral conveying blade, 24-transfer trolley, 25-driving shaft and 26-driven shaft.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
As shown in fig. 1, the continuous feeding device for viscous granular materials comprises: the conveying device comprises a conveying cover 1, wherein a feeding hole 2 is formed in the conveying cover 1, a discharging hole 3 is formed in the bottom of the conveying cover 1, three conveying belts are horizontally arranged in the conveying cover 1, each conveying belt is driven to rotate by a first power device 4, and the three conveying belts are arranged in a staggered mode; and the conveying direction of two adjacent conveying belts is opposite, in the utility model, three conveying belts are wound on a driving shaft 25 and a driven shaft 26, the driving shaft 25 and the driven shaft 26 are both arranged on the conveying cover 1, the first power device 4 is preferably a driving shaft driving motor, and the driving shaft 25 is driven to rotate by the driving shaft driving motor, thereby realizing the movement of the conveying belts; the three conveying belts are respectively a first conveying belt 5, a second conveying belt 6 and a third conveying belt 7 from top to bottom, after the viscous granular materials 8 fall into the first conveying belt 5 from the feeding hole 2, the viscous granular materials are gradually transferred to the downstream end of the first conveying belt 5 along with the operation of the first conveying belt 5, and the viscous granular materials 8 fall onto the second conveying belt 6 from the first conveying belt 5 under the action of gravity; because the first conveyor belt 5 and the second conveyor belt 6 are in opposite conveying directions, the viscous granular materials 8 falling on the second conveyor belt 6 are conveyed to the downstream end of the second conveyor belt 6, and the viscous granular materials 8 fall on the third conveyor belt 7 from the second conveyor belt 6 under the action of gravity; similarly, because the second conveyor belt 6 and the third conveyor belt 7 are in the opposite conveying directions, the viscous granular materials 8 falling on the third conveyor belt 7 are conveyed to the downstream end of the third conveyor belt 7 and fall into the discharge port 3 under the action of gravity.
The conveying cover 1 is communicated with an air box 10 through a cooling air inlet pipe 9, the air box 10 is communicated with an air blowing device 11, and the air blowing device 11 is preferably an air blower.
The conveying cover 1 is also communicated with an air box 10 through a cooling air outlet pipe 12; the cooling air outlet pipe 12 is provided with a heat exchanger 13, the heat exchanger 13 comprises a shell 14, the cooling air outlet pipe 12 penetrates through the shell 14, the upper end of the shell 14 is provided with a cooling liquid inlet 15, and the lower end of the shell 14 is provided with a cooling liquid outlet 16.
As shown in fig. 1 and fig. 2, a screw conveyor 17 is installed at the discharge port 3, the screw conveyor 17 includes a conveying cylinder 18, one end of the conveying cylinder 18 is provided with a conveying inlet 19 communicated with the discharge port 3, and the other end of the conveying cylinder 18 is provided with a conveying outlet 20; a conveying shaft 22 driven by a second power device 21 is rotatably mounted in the conveying cylinder 18, the second power device 21 is preferably a conveying shaft driving motor, and a spiral conveying blade 23 is mounted on the conveying shaft 22.
For the convenience of the lasting transportation of stickness grain dress material, the utility model discloses to carry entry 19 to set up in the lower part of carrying export 20, utilize screw conveyor 17 to promote stickness granular material 8 to the take the altitude, be convenient for transfer car 24 headspace, conveniently utilize the transfer car 24 to carry the defeated material with the lasting transportation of stickness granular material 8.
When the utility model is used, the viscous granular materials 8 enter the conveying cover 1 from the feed inlet 2 and fall onto the first conveying belt 5, and the viscous granular materials 8 are cooled by cold air blown into the conveying cover 1 by the air blowing device 11; the viscous granular materials 8 are relayed and transferred through the first conveying belt 5, the second conveying belt 6 and the third conveying belt 7, so that the cooling time of the viscous granular materials 8 is prolonged, and the cooling effect is improved; the viscous granular materials 8 fall into the discharge port 3 after being conveyed by the third conveyor belt 7, and because the discharge port 3 is communicated with the conveying inlet 19, the viscous granular materials 8 fall into the conveying cylinder 18 from the discharge port 3 and are conveyed to the conveying outlet 20, the transfer trolley 24 is placed at the conveying outlet 20, and the viscous granular materials 8 are continuously operated by the transfer trolley 24, so that the viscous granular materials 8 are continuously operated to a specified position.
In order to increase the cooling effect on the viscous granular materials 8, the conveying cover 1 is communicated with the air box 10 through a cooling air outlet pipe 12, meanwhile, a heat exchanger 13 for heat exchange is arranged on the cooling air outlet pipe 12, the temperature of air in the conveying cover 1 is increased after the air exchanges heat with the viscous granular materials 8, when the air passes through the heat exchanger 13, cooling liquid enters the shell 14 from a cooling liquid inlet 15 and flows out from a cooling liquid outlet 16 and exchanges heat with the cooling air outlet pipe 12 in the flowing process, so that the air temperature in the cooling air outlet pipe 12 is reduced, and the cooling liquid can be common tap water; after heat exchange, cold air in the supercooling air outlet pipe 12 flows into the air box 10, then enters the air box to be conveyed and carries out next heat exchange with the viscous granular materials 8, and the circulation is carried out, so that the cooling effect is further improved.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (5)
1. Granular material continuous feeding device of stickness, its characterized in that includes:
the conveying cover is provided with a feeding hole, the bottom of the conveying cover is provided with a discharging hole, a conveying belt driven by a first power device to rotate is horizontally installed in the conveying cover, and the conveying belt receives materials of the feeding hole and conveys the materials to the discharging hole;
the conveying cover is communicated with an air box through a cooling air inlet pipe, and the air box is communicated with a blowing device.
2. The continuous viscous granular material conveying device as claimed in claim 1, wherein the conveyance hood is further communicated with the windbox through a cooling air outlet pipe;
install heat exchanger on the cooling outlet duct, heat exchanger includes the casing, the cooling outlet duct runs through the casing, the upper end of casing is provided with the coolant liquid inlet, the lower extreme of casing is provided with the coolant liquid outlet.
3. The continuous feed device for viscous granular material as claimed in claim 1, wherein said conveyor belts are provided with three, three of said conveyor belts being arranged in a staggered manner; and the conveying directions of two adjacent conveying belts are opposite.
4. The continuous feed device for viscous granular materials as claimed in claim 1, wherein said discharge port is provided with an auger delivery device comprising a delivery cylinder having a delivery inlet communicating with said discharge port at one end and a delivery outlet at the other end; and a conveying shaft driven by a second power device is rotatably mounted in the conveying cylinder, and a spiral conveying blade is mounted on the conveying shaft.
5. The continuous feed device of viscous granular material as claimed in claim 4, wherein said feed inlet is located at a lower portion of said feed outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921230610.5U CN210392528U (en) | 2019-08-01 | 2019-08-01 | Viscous granular material continuous conveying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921230610.5U CN210392528U (en) | 2019-08-01 | 2019-08-01 | Viscous granular material continuous conveying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210392528U true CN210392528U (en) | 2020-04-24 |
Family
ID=70357718
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921230610.5U Active CN210392528U (en) | 2019-08-01 | 2019-08-01 | Viscous granular material continuous conveying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210392528U (en) |
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2019
- 2019-08-01 CN CN201921230610.5U patent/CN210392528U/en active Active
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