CN113213481A - Novel continuous cooling equipment is used in active carbon production - Google Patents
Novel continuous cooling equipment is used in active carbon production Download PDFInfo
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- CN113213481A CN113213481A CN202110474416.7A CN202110474416A CN113213481A CN 113213481 A CN113213481 A CN 113213481A CN 202110474416 A CN202110474416 A CN 202110474416A CN 113213481 A CN113213481 A CN 113213481A
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- cooling
- cooling device
- kiln
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- kiln body
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- 238000001816 cooling Methods 0.000 title claims abstract description 106
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 6
- 238000004519 manufacturing process Methods 0.000 title claims description 14
- 239000000463 material Substances 0.000 claims abstract description 29
- 238000007599 discharging Methods 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000000498 cooling water Substances 0.000 claims description 7
- 238000005096 rolling process Methods 0.000 claims description 7
- 239000003610 charcoal Substances 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims description 2
- 238000003763 carbonization Methods 0.000 abstract description 9
- 239000005539 carbonized material Substances 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 description 6
- 238000012856 packing Methods 0.000 description 2
- 239000011265 semifinished product Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/39—Apparatus for the preparation thereof
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
Abstract
The invention provides novel continuous cooling equipment for producing activated carbon, which comprises a carbonization kiln, a primary cooling device and a secondary cooling device, wherein the carbonization kiln is used for high-temperature carbonization of a formed carbon strip, a discharge port of the carbonization kiln is connected with a feeding port of the primary cooling device, a discharge port of the primary cooling device is connected with a feeding port of the secondary cooling device, a cooled material is discharged from a discharge port of the secondary cooling device, the primary cooling device comprises a spiral cooler, the spiral cooler consists of a plurality of layers of cooling grooves spirally extending in a spiral shape, the cooling grooves are provided with grooves for containing the material, the scheme is characterized in that the carbonized material is subjected to primary cooling through the primary cooling device, secondary cooling is performed through the secondary cooling device, the temperature of the material subjected to secondary cooling is reduced to room temperature, the material can be directly bagged and packaged, and two-stage cooling is adopted, so that the cooling efficiency is very high. The spiral cooler has the characteristics of compact structure, large treatment capacity, small occupied space and high cooling efficiency.
Description
Technical Field
The invention relates to the technical field of activated carbon preparation, in particular to novel continuous cooling equipment for activated carbon production.
Background
The temperature of the carbonized activated carbon semi-finished product reaches 800 ℃ and 900 ℃, and the carbonized activated carbon semi-finished product can be bagged or packaged only by cooling in time. The existing equipment lifts the carbonized material to an output mechanism by a bucket elevator, and then the carbonized material is cooled by natural cooling and other modes. The structure has the defects of low material cooling speed and large occupied space.
Disclosure of Invention
There is a need for a new continuous cooling apparatus for activated carbon production.
The utility model provides a novel active carbon production is with continuous cooling equipment which characterized in that: including carbomorphism kiln, one-level cooling device, second grade cooling device, the carbomorphism kiln is used for the charcoal strip high temperature carbomorphism after the shaping, and the material loading mouth of one-level cooling device is connected to the discharge gate of carbomorphism kiln, and the material loading mouth of second grade cooling device is connected to one-level cooling device's feed opening, and the material after the discharge gate discharge cooling of second grade cooling device, one-level cooling device includes the spiral cooler, and the spiral cooler comprises a plurality of layers of cooling tank that are the helical shape and spiral the extension, and the cooling tank sets up the recess that holds the material.
This scheme is once cooled off through the material of one-level cooling device after to the carbomorphism, carries out the secondary cooling through second grade cooling device, and the material temperature after twice cooling reduces to the room temperature, can directly the bagging-off packing, adopts the cooling of two grades formula, and cooling efficiency is very high. The spiral cooler has the characteristics of compact structure, large treatment capacity, small occupied space and high cooling efficiency.
Drawings
Fig. 1 is a schematic structural view of the apparatus.
Fig. 2 is a schematic sectional view of the cooling bath 21.
Fig. 3 is a schematic view of a base.
Fig. 4 is a schematic structural view of the secondary cooling device 30.
Fig. 5 is a cross-sectional view of a kiln section.
In the figure: the device comprises a carbonization kiln 10, a primary cooling device 20, a cooling tank 21, a groove 22, a jacket 221, a base 23, a vibration motor 24, a flexible connector 25, a first water return pipe 26, a first water supply pipe 27, a secondary cooling device 30, a feeding end head 31, a kiln body section 32, a feeding end plate 321, a feeding opening 3211, a discharging end plate 322, a discharging opening 3221, a material pipeline 323, a second water supply pipe 324, a second water return pipe 325, a discharging end head 33, a rotary mechanism 34, a rolling ring 341 and a driving gear 342.
Detailed Description
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without creative efforts.
Referring to fig. 1 to 5, an embodiment of the present invention provides a novel continuous cooling apparatus for producing activated carbon, including a carbonization kiln 10, a primary cooling device 20, and a secondary cooling device 30, where the carbonization kiln 10 is used to carbonize a formed carbon strip at a high temperature, a discharge port of the carbonization kiln 10 is connected to a feeding port of the primary cooling device 20, a discharge port of the primary cooling device 20 is connected to a feeding port 3211 of the secondary cooling device 30, and a discharge port 3221 of the secondary cooling device 30 discharges a cooled material, the primary cooling device 20 includes a spiral cooler, the spiral cooler is composed of a plurality of layers of cooling grooves 21 spirally extending in a spiral shape, and the cooling grooves 21 are provided with grooves 22 for holding the material.
This scheme is once cooled off through the material of one-level cooling device 20 after to the carbomorphism, is carrying out the secondary cooling through second grade cooling device 30, and the material temperature after twice cooling reduces to the room temperature, can directly bag the packing, adopts the cooling of two grades formula, and cooling efficiency is very high. The spiral cooler has the characteristics of compact structure, large treatment capacity, small occupied space and high cooling efficiency.
Further, the secondary cooling device 30 includes a cooling kiln and a swing mechanism 34, the cooling kiln is obliquely arranged, a feeding port 3211 of the cooling kiln is connected with an outlet of the primary cooling device 20, the cooling kiln includes a feeding end 31, a kiln body section 32 and a discharging end 33 which are connected in sequence, the swing mechanism 34 drives the kiln body section 32 to rotate, the feeding end 31 is movably and hermetically connected with the kiln body section 32, the discharging end 33 is movably and hermetically connected with the kiln body section 32, the kiln body section 32 is provided with a feeding end plate 321 and a discharging end plate 322, the feeding end plate 321 and the discharging end plate 322 seal the kiln body section 32 to form a sealed inner cavity, a plurality of material pipelines 323 are arranged inside the kiln body section 32, two ends of each material pipeline 323 respectively penetrate through the feeding end plate 321 and the discharging end plate 322 to extend into the feeding end 31 and the discharging end plate 33, a channel for cooling water to flow is formed in the space of the kiln body section 32 between adjacent material pipes, the end of the feeding end head 31 is provided with a feeding port 3211, the end of the discharging end head 33 is provided with a discharging port 3221, and the circle centers of the feeding end plate 321 and the discharging end plate 322 of the kiln body section 32 are respectively provided with a second feeding pipe 324 and a second water return pipe 325. This scheme adopts and presss from both sides the cover 221 mode, and the tube side lets in the material, and the shell side lets in cooling water, and so shell side surface area is bigger, makes more water and tube side contact, and the cooling effect is better.
Further, a base 23 for supporting is arranged at the bottom of the spiral cooler, the base 23 is connected with the spiral cooler, and a vibration motor 24 is arranged at the bottom of the base 23. The vibration of the vibration motor 24 may ensure a smooth downward movement of the material or the vibration frequency may be adjusted to increase the downward movement of the material.
Further, flexible connectors 25 are respectively arranged at two ends of the spiral cooler. The flexible connector 25 is used as a transition connector, so that the vibrating spiral cooler is directly and flexibly connected with the carbonization kiln 10 and the secondary cooling device 30, and mechanical damage caused by rigid connection is avoided.
Furthermore, a first water return pipe 26 and a first upper water pipe 27 for introducing cooling water are respectively arranged on the uppermost layer cooling tank 21 and the lowermost layer cooling tank 21 of the spiral cooler, the cooling tank 21 is provided with a jacket 221 layer, and the jacket 221 layer is used for introducing cooling water.
Further, the cooling tank 21 is in the shape of a groove 22 with an open top, and a jacket 221 is provided on the side wall of the groove 22.
Further, the revolving mechanism 34 includes a rolling ring 341 and a driving gear 342, the rolling ring 341 is fixedly sleeved on the outer wall of the kiln body section 32, the driving gear 342 is meshed with the rolling ring 341, and the driving gear 342 is driven by an external motor.
Furthermore, the feeding end head 31 is movably and hermetically connected with the kiln body section 32, and the discharging end head 33 is movably and hermetically connected with the kiln body section 32. For example, the movable connection can be a bearing connection, and the sealing connection can be realized by adding a sealing ring.
Furthermore, the second water feeding pipe 324 is movably connected with the feeding end plate 321 in a sealing manner, and the second water returning pipe 325 is movably connected with the discharging end plate 322 in a sealing manner. For example, the movable connection can be a bearing connection, and the sealing connection can be realized by adding a sealing ring.
The modules or units in the device of the embodiment of the invention can be combined, divided and deleted according to actual needs.
The above disclosure is only illustrative of the preferred embodiments of the present invention, which should not be taken as limiting the scope of the invention, but rather the invention can be embodied in other specific forms without departing from the spirit or essential characteristics thereof. It will be understood by those skilled in the art that all or a portion of the above-described embodiments may be practiced and equivalents thereof may be resorted to as falling within the scope of the invention as claimed. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (9)
1. The utility model provides a novel active carbon production is with continuous cooling equipment which characterized in that: including carbomorphism kiln, one-level cooling device, second grade cooling device, the carbomorphism kiln is used for the charcoal strip high temperature carbomorphism after the shaping, and the material loading mouth of one-level cooling device is connected to the discharge gate of carbomorphism kiln, and the material loading mouth of second grade cooling device is connected to one-level cooling device's feed opening, and the material after the discharge gate discharge cooling of second grade cooling device, one-level cooling device includes the spiral cooler, and the spiral cooler comprises a plurality of layers of cooling tank that are the helical shape and spiral the extension, and the cooling tank sets up the recess that holds the material.
2. The novel continuous cooling apparatus for activated carbon production as claimed in claim 1, wherein: the secondary cooling device comprises a cooling kiln and a rotary mechanism, the cooling kiln is obliquely arranged, a feeding hole of the cooling kiln is connected with an outlet of the primary cooling device, the cooling kiln comprises a feeding end, a kiln body section and a discharging end which are sequentially connected, the rotary mechanism drives the kiln body section to rotate, the feeding end is movably and hermetically connected with the kiln body section, the discharging end is movably and hermetically connected with the kiln body section, the kiln body section is provided with a feeding end plate and a discharging end plate, the feeding end plate and the discharging end plate seal the kiln body section to form a sealed inner cavity, a plurality of material pipelines are arranged inside the kiln body section, two ends of each material pipeline respectively penetrate through the feeding end plate and the discharging end plate to extend into the feeding end and the discharging end, a channel for cooling water to circulate is formed in the space of the kiln body section between adjacent material pipes, the end part of the feeding end is provided with a feeding hole, and the end part of the discharging end is provided with a discharging hole, and a second water feeding pipe and a second water return pipe are respectively arranged at the circle centers of the feeding end plate and the discharging end plate of the kiln body section.
3. The novel continuous cooling apparatus for activated carbon production as claimed in claim 2, wherein: the bottom of the spiral cooler is provided with a base for supporting, the base is connected with the spiral cooler, and the bottom of the base is provided with a vibrating motor.
4. The novel continuous cooling apparatus for activated carbon production as claimed in claim 2, wherein: and flexible connectors are respectively arranged at two ends of the spiral cooler.
5. The novel continuous cooling apparatus for activated carbon production as claimed in claim 4, wherein: still set up the first return pipe and the first upper hose that are used for letting in cooling water respectively at spiral cooler's the superiors layer cooling bath and the bottommost layer cooling bath, the cooling bath sets up the jacket layer, and the jacket layer is used for letting in cooling water.
6. The novel continuous cooling apparatus for activated carbon production as claimed in claim 5, wherein: the cooling tank is in the shape of a groove with an open top, and a jacket is arranged on the side wall of the groove.
7. The novel continuous cooling apparatus for activated carbon production as claimed in claim 2, wherein: the rotary mechanism comprises a rolling ring and a driving gear, the rolling ring is fixedly sleeved on the outer wall of the kiln body section, the driving gear is meshed with the rolling ring and is driven by an external motor.
8. The novel continuous cooling apparatus for activated carbon production as claimed in claim 2, wherein: the feeding end is movably and hermetically connected with the kiln body section, and the discharging end is movably and hermetically connected with the kiln body section.
9. The novel continuous cooling apparatus for activated carbon production as claimed in claim 2, wherein: the second water feeding pipe is movably and hermetically connected with the feeding end plate, and the second water return pipe is movably and hermetically connected with the discharging end plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110474416.7A CN113213481A (en) | 2021-04-29 | 2021-04-29 | Novel continuous cooling equipment is used in active carbon production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110474416.7A CN113213481A (en) | 2021-04-29 | 2021-04-29 | Novel continuous cooling equipment is used in active carbon production |
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| CN113213481A true CN113213481A (en) | 2021-08-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202110474416.7A Pending CN113213481A (en) | 2021-04-29 | 2021-04-29 | Novel continuous cooling equipment is used in active carbon production |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101318650A (en) * | 2007-06-06 | 2008-12-10 | 张大伟 | Swinging type high temperature active coke refrigerating device |
| CN204151075U (en) * | 2014-10-22 | 2015-02-11 | 天津博尔迈环保科技有限公司 | A kind of sealing cooling discharging device |
| CN104357064A (en) * | 2014-11-03 | 2015-02-18 | 嘉兴市新角机械制造有限公司 | Continuous carbonizing device for biomasses |
| CN205420272U (en) * | 2015-06-25 | 2016-08-03 | 农业部规划设计研究院 | Biological charcoal second grade circulative cooling system |
| CN207435038U (en) * | 2017-08-29 | 2018-06-01 | 衢州市衢江区创辉机械厂（普通合伙） | A kind of activation furnace discharge and cooling device |
| CN109612267A (en) * | 2018-12-11 | 2019-04-12 | 湖南嘉力亚新材料有限公司 | A kind of blanking chute mouth having constant cooling down function |
| CN210765148U (en) * | 2019-11-04 | 2020-06-16 | 河北省农林科学院农业资源环境研究所 | Biochar preparation device |
| CN212955034U (en) * | 2020-07-06 | 2021-04-13 | 河南煜见煜辉生态科技有限公司 | Spiral cooling system for biological coal production |
-
2021
- 2021-04-29 CN CN202110474416.7A patent/CN113213481A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101318650A (en) * | 2007-06-06 | 2008-12-10 | 张大伟 | Swinging type high temperature active coke refrigerating device |
| CN204151075U (en) * | 2014-10-22 | 2015-02-11 | 天津博尔迈环保科技有限公司 | A kind of sealing cooling discharging device |
| CN104357064A (en) * | 2014-11-03 | 2015-02-18 | 嘉兴市新角机械制造有限公司 | Continuous carbonizing device for biomasses |
| CN205420272U (en) * | 2015-06-25 | 2016-08-03 | 农业部规划设计研究院 | Biological charcoal second grade circulative cooling system |
| CN207435038U (en) * | 2017-08-29 | 2018-06-01 | 衢州市衢江区创辉机械厂（普通合伙） | A kind of activation furnace discharge and cooling device |
| CN109612267A (en) * | 2018-12-11 | 2019-04-12 | 湖南嘉力亚新材料有限公司 | A kind of blanking chute mouth having constant cooling down function |
| CN210765148U (en) * | 2019-11-04 | 2020-06-16 | 河北省农林科学院农业资源环境研究所 | Biochar preparation device |
| CN212955034U (en) * | 2020-07-06 | 2021-04-13 | 河南煜见煜辉生态科技有限公司 | Spiral cooling system for biological coal production |
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Application publication date: 20210806 |