CN215655013U - Calcined coke is compounding device for granulation - Google Patents
Calcined coke is compounding device for granulation Download PDFInfo
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- CN215655013U CN215655013U CN202122037019.1U CN202122037019U CN215655013U CN 215655013 U CN215655013 U CN 215655013U CN 202122037019 U CN202122037019 U CN 202122037019U CN 215655013 U CN215655013 U CN 215655013U
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Abstract
The utility model relates to a mixing device for calcined coke granulation, which belongs to the field of petroleum product production equipment, the calcined coke granulation mixing device comprises a mixing bin, a feeding bin and a discharging opening, wherein a material enters the feeding bin from a feeding hole, the material bin enters the mixing bin through the feeding bin and the discharging opening to be mixed, the mixed material is discharged from a discharging opening, a rack and a conveying belt are arranged below the mixing bin, a metering groove is arranged on the conveying belt, the position of an inner groove body of the metering groove corresponds to the position of the discharging opening, the material discharged from the discharging opening enters the metering groove, the metering groove is conveyed to a recycling groove through the conveying belt to be transported, the mixed and metered material enters the recycling groove and is transported to the next processing operation for subsequent processing operation.
Description
Technical Field
The utility model belongs to the field of petroleum product production equipment, and particularly relates to a mixing device for calcined coke granulation.
Background
The main application field of the calcined coke in China is electrolytic aluminum industry, which accounts for more than 65 percent of the using amount of the whole calcined coke, and then carbon, industrial silicon and other smelting industries, the calcined coke is used as fuel, and mainly used in the industries of cement, power generation, glass and the like, the occupied proportion is small, the supply and demand conditions of the calcined coke in China are basically kept level at present, but due to the export of a large amount of low-sulfur high-end petroleum coke, the total supply amount of the calcined coke in China is insufficient, the high-sulfur calcined coke in China needs to be supplemented, along with the construction of a large number of coking devices in recent years, the yield of the calcined coke in China can be further enlarged, the raw material of the calcined coke is mainly petroleum coke, the calcined coke is produced by high-temperature calcination of the petroleum coke after mixing, in the existing production process, the quantitative mixing operation needs to be carried out, the quantitative production is avoided, the resource waste is avoided, the production quality is ensured, and the metering and mixing device in the prior art has no corresponding material recovery device, the material after mixing can not be recovered smoothly.
Disclosure of Invention
In order to overcome the problems in the background art, the utility model discloses a mixing device for calcined coke granulation, the calcined coke granulation mixing device comprises a mixing bin, a feeding bin and a discharging opening, wherein a material enters the feeding bin from a feeding hole, the material bin enters the mixing bin through the feeding bin and the discharging opening to be mixed, the mixed material is discharged from a discharging opening, a rack and a conveying belt are arranged below the mixing bin, a metering groove is arranged on the conveying belt, the position of an inner groove body of the metering groove corresponds to the position of the discharging opening, the material discharged from the discharging opening enters the metering groove, the metering groove is conveyed to a recycling groove through the conveying belt to be transported, the mixed and metered material enters the recycling groove and is transported to the next processing operation for subsequent processing operation.
In order to realize the purpose, the utility model is realized by the following technical scheme:
the mixing device for calcined coke granulation mainly comprises a mixing bin, support legs, pulleys, a feeding bin, a feeding port, a discharging port, a frame, a conveying belt, a metering tank and a recycling tank, wherein the support legs are arranged at the bottom of the mixing bin, the pulleys are connected with the bottom of the support legs, the feeding bin is arranged above the mixing bin, the feeding port is arranged at the top of the feeding bin, the discharging port is arranged between a mixing pool and the feeding bin, the discharging port is arranged at the bottom of the mixing bin, the frame is arranged below the mixing bin, the conveying belt is arranged at the top of the frame, the metering tank is arranged on the conveying belt, the recycling tank is arranged beside the conveying belt, a stirring roller is arranged inside the mixing bin, a partition plate is arranged inside the feeding bin, the metering tank consists of a metering device, a metering tank bottom wheel, a metering tank baffle and a body, the metering tank bottom wheel is arranged at the bottom of the metering device, the baffle plate is arranged at the top of the metering device, interior cell body sets up at the metering device top, the recovery silo comprises bottom plate, recovery silo return pulley, recovery silo baffle, silo, flitch down, contact plate, the bottom plate bottom is provided with recovery silo return pulley, and recovery silo baffle sets up at the bottom plate top, and the silo setting is at the bottom plate top, and the flitch setting is at the silo side down, and the contact plate is connected with the flitch down.
The blending bunker is communicated with the feeding bunker through a feed opening.
At least two stirring rollers are arranged inside the mixing bin.
The feeding bin is internally provided with at least two partition plates, the feeding bin is internally divided into at least three spaces through the partition plates, and the three spaces are respectively and correspondingly provided with a feeding port.
The notch of the inner groove body of the metering device is arranged at a position corresponding to the discharge port, and the area of the discharge port is smaller than that of the inner groove body.
The metering tank baffle is provided with two, is located metering device's front and back, and recovery material groove baffle is provided with two, is located the front and the back of bottom plate device.
The inner trough body is detachably arranged at the top of the metering device, and the trough is detachably arranged at the top of the bottom plate.
Lower flitch, contact plate and silo integrated into one piece set up, the contact plate contacts with conveyer belt, and the coating has anti-skidding coating in the contact plate bottom.
The utility model has the beneficial effects that: the calcined coke granulation mixing device comprises a mixing bin, a feeding bin and a discharging opening, wherein a material enters the feeding bin from a feeding hole, the material bin enters the mixing bin through the feeding bin and the discharging opening to be mixed, the mixed material is discharged from a discharging opening, a rack and a conveying belt are arranged below the mixing bin, a metering groove is arranged on the conveying belt, the position of an inner groove body of the metering groove corresponds to the position of the discharging opening, the material discharged from the discharging opening enters the metering groove, the metering groove is conveyed to a recycling groove through the conveying belt to be transported, the mixed and metered material enters the recycling groove and is transported to the next processing operation for subsequent processing operation.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic structural view of a feed bin;
FIG. 3 is a schematic structural view of a mixing bin;
FIG. 4 is a schematic view of a metering tank;
fig. 5 is a schematic structural view of the recovery tank.
In the figure, 1-mixing bin, 2-support leg, 3-pulley, 4-feeding bin, 5-feeding inlet, 6-blanking inlet, 7-discharging outlet, 8-frame, 9-conveying belt, 10-metering tank, 11-recovery tank, 12-stirring roller, 13-clapboard, 14-metering device, 15-metering tank bottom wheel, 16-metering tank baffle, 17-inner tank body, 18-bottom plate, 19-recovery tank bottom wheel, 20-recovery tank baffle, 21-tank, 22-blanking plate and 23-contact plate.
Detailed Description
In order to make the above objects, technical solutions and advantages clearer and more clear, the present invention is specifically described below with reference to the accompanying drawings.
As shown in figures 1-5, the mixing device for granulation of calcined coke mainly comprises a mixing silo 1, support legs 2, pulleys 3, a feeding silo 4, a feeding port 5, a discharging port 6, a discharging port 7, a frame 8, a conveyor belt 9, a metering tank 10 and a recycling tank 11, wherein the support legs 2 are arranged at the bottom of the mixing silo 1, the pulleys 3 are connected with the bottom of the support legs 2, the feeding silo 4 is arranged above the mixing silo 1, the feeding port 5 is arranged at the top of the feeding silo 4, the discharging port 6 is arranged between the mixing tank 1 and the feeding silo 4, the discharging port 7 is arranged at the bottom of the mixing silo 1, the mixing silo 1 is communicated with the feeding silo 4 through the discharging port 6, the frame 8 is arranged below the mixing silo 1, the conveyor belt 9 is arranged at the top of the frame 8, the metering tank 10 is arranged on the conveyor belt, the recycling tank 11 is arranged beside the conveyor belt 9, a stirring roller 12 is arranged inside the mixing silo 1, at least two stirring rollers 12 are arranged inside the mixing bin 1, partition plates 13 are arranged inside the feeding bin 4, at least two partition plates 13 are arranged inside the feeding bin 4, at least three spaces are formed by dividing the inside of the feeding bin 4 through the partition plates 13, the three spaces are respectively and correspondingly provided with the feeding ports 5, the metering tank 10 is composed of a metering device 14, a metering tank bottom wheel 15, metering tank baffles 16 and an inner tank body 17, the metering tank bottom wheel 15 is arranged at the bottom of the metering device 14, the metering tank baffles 16 are arranged at the top of the metering device 14, the metering tank baffles 16 are arranged at two parts and are positioned at the front and the back of the metering device 14, the inner tank body 17 is arranged at the top of the metering device 14, the inner tank body 17 of the metering device 14 is detachably arranged at the top of the metering device 14, the notch of the inner tank body 17 of the metering device 14 is arranged at the position corresponding to the discharging port 7, the area of the discharging port 7 is smaller than that of the inner tank body 17, and the recovery tank 11 is composed of a bottom plate 18, Recovery silo return pulley 19, recovery silo baffle 20, silo 21, unloading board 22, contact plate 23 are constituteed, 18 bottoms of bottom plate are provided with recovery silo return pulley 19, and recovery silo baffle 20 sets up at 19 tops of bottom plate, and silo 21 sets up at 18 tops of bottom plate, and silo 21 can be dismantled and place at 18 tops of bottom plate, and recovery silo baffle 20 is provided with two, is located the front and the back of bottom plate 18, and unloading board 22 sets up at silo 21 side, and contact plate 23 is connected with unloading board 22, and unloading board 22, contact plate 23 and 21 integrated into one piece of silo set up, and contact plate 23 contacts with conveyer 9, and the coating has anti-skidding coating 23 bottom the contact plate.
The mixing device for calcined coke granulation comprises a mixing bin 1, a feeding bin 4 and a discharge opening 6, wherein materials enter the feeding bin 4 from a feeding port 5, at least two partition plates 13 are arranged inside the feeding bin 4, the feeding bin 4 is divided into at least three spaces through the partition plates 13, the three spaces are respectively and correspondingly provided with the feeding port 5, the materials required by calcined coke production enter the feeding bin 4 from the feeding port 5 and enter the mixing bin 1 through the feeding bin 4 and the discharge opening 6 to be mixed, at least two stirring rollers 12 are arranged inside the mixing bin 1 and can fully mix the materials entering the mixing bin 1, the mixed materials are discharged from a discharge opening 7, a frame 8 and a conveying belt 9 are arranged below the mixing bin 1, a metering tank 10 is arranged on the conveying belt 9, and the position of an inner groove body 17 of the metering tank 10 is arranged corresponding to the position of the discharge opening 7, the notch of the inner groove body 17 of the metering device 14 is placed corresponding to the position of the discharge port 7, the area of the discharge port 7 is smaller than that of the inner groove body 17, the material discharged from the discharge port 7 enters the metering groove 10 and does not overflow, the metering groove 10 is conveyed to the recovery groove 11 through the conveying belt 9 for material transfer, the blanking plate 22, the contact plate 23 and the groove 21 are integrally formed, the contact plate 23 is in contact with the conveying belt 9, the bottom of the contact plate 23 is coated with an anti-slip coating, the contact plate 23 is stably in contact with the conveying belt 9, the inner groove body 17 is detachably placed at the top of the metering device 14, the metering groove 10 reaches the contact plate 23 through the conveying belt 9, the material drawn out from the inner groove body 17 is poured into the groove 21, the groove 21 is detachably placed at the top of the bottom plate 18, the mixed and metered material enters the recovery groove 11 and is transferred to the next processing operation for subsequent processing operation, the utility model measures the materials after mixing, and the measured materials are recycled through the conveying belt and the recycling material tank.
Finally, it is noted that the above-mentioned preferred embodiments illustrate rather than limit the utility model, and that, although the utility model has been described in detail with reference to the above-mentioned preferred embodiments, it will be understood by those skilled in the art that various changes in form and detail may be made therein without departing from the scope of the utility model as defined by the appended claims.
Claims (8)
1. A mixing device for calcined coke granulation is characterized by mainly comprising a mixing bin, support legs, pulleys, a feeding bin, a feeding port, a discharging port, a rack, a conveying belt, a metering tank and a recycling tank, wherein the support legs are arranged at the bottom of the mixing bin, the pulleys are connected to the bottom of the support legs, the feeding bin is arranged above the mixing bin, the feeding port is arranged at the top of the feeding bin, the discharging port is arranged between a mixing tank and the feeding bin, the discharging port is arranged at the bottom of the mixing bin, the rack is arranged below the mixing bin, the conveying belt is arranged at the top of the rack, the metering tank is arranged on the conveying belt, the recycling tank is arranged beside the conveying belt, stirring rollers are arranged inside the mixing bin, a partition plate is arranged inside the feeding bin, the metering tank consists of a metering device, a metering tank bottom wheel, a metering tank baffle plate and an inner tank body, the metering tank bottom of the metering device is provided with a metering tank bottom wheel, the baffle sets up at the metering device top, and the internal cell body sets up at the metering device top, the recovery silo comprises bottom plate, recovery silo return pulley, recovery silo baffle, silo, lower flitch, contact plate, the bottom plate bottom is provided with recovery silo return pulley, and recovery silo baffle sets up at the bottom plate top, and the silo setting is at the bottom plate top, and the lower flitch setting is at the silo side, and the contact plate is connected with lower flitch.
2. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: the blending bunker is communicated with the feeding bunker through a feed opening.
3. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: at least two stirring rollers are arranged inside the mixing bin.
4. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: the feeding bin is internally provided with at least two partition plates, the feeding bin is internally divided into at least three spaces through the partition plates, and the three spaces are respectively and correspondingly provided with a feeding port.
5. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: the notch of the inner groove body of the metering device is arranged at a position corresponding to the discharge port, and the area of the discharge port is smaller than that of the inner groove body.
6. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: the metering tank baffle is provided with two, is located metering device's front and back, and the recovery material groove baffle is provided with two, is located the front and the back of bottom plate.
7. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: the inner trough body is detachably arranged at the top of the metering device, and the trough is detachably arranged at the top of the bottom plate.
8. A mixing device for calcined coke granulation as claimed in claim 1, characterized in that: lower flitch, contact plate and silo integrated into one piece set up, the contact plate contacts with conveyer belt, and the coating has anti-skidding coating in the contact plate bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122037019.1U CN215655013U (en) | 2021-08-27 | 2021-08-27 | Calcined coke is compounding device for granulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122037019.1U CN215655013U (en) | 2021-08-27 | 2021-08-27 | Calcined coke is compounding device for granulation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215655013U true CN215655013U (en) | 2022-01-28 |
Family
ID=79956644
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122037019.1U Active CN215655013U (en) | 2021-08-27 | 2021-08-27 | Calcined coke is compounding device for granulation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215655013U (en) |
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2021
- 2021-08-27 CN CN202122037019.1U patent/CN215655013U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221202 Address after: 454000 North of the East Section of Fazhan Avenue, Baishan Town, Boai County, Jiaozuo City, Henan Province Patentee after: Henan Zhongtan New Material Technology Co.,Ltd. Address before: 454000 west of West chemical plant, zhongzhan District, Jiaozuo City, Henan Province Patentee before: JIAOZUO ZHONGZHOU CARBON Co.,Ltd. |
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| TR01 | Transfer of patent right |