CN112250070A - Activated carbon activation device - Google Patents
Activated carbon activation device Download PDFInfo
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- CN112250070A CN112250070A CN202011214862.6A CN202011214862A CN112250070A CN 112250070 A CN112250070 A CN 112250070A CN 202011214862 A CN202011214862 A CN 202011214862A CN 112250070 A CN112250070 A CN 112250070A
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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
Abstract
The invention discloses an activated carbon activation device, which relates to the technical field of activation furnaces and comprises an overhead base and a chimney, wherein a first reaction zone furnace wall, a second reaction zone furnace wall and a third reaction zone furnace wall are respectively arranged on the overhead base, the first reaction zone furnace wall, the second reaction zone furnace wall and the third reaction zone furnace wall are all in an upright cylindrical shape, the third reaction zone furnace wall is positioned inside the second reaction zone furnace wall, the second reaction zone furnace wall is positioned inside the first reaction zone furnace wall, and the first reaction zone furnace wall, the second reaction zone furnace wall and the third reaction zone furnace wall respectively enclose three independent sections, namely a first reaction zone, a second reaction zone and a third reaction zone. The invention solves the problems that the existing activated carbon activation furnace is generally set into three relatively independent split structures according to three steps of activated carbon activation, so that the occupied space is larger, the heat loss is serious and the energy consumption is high.
Description
Technical Field
The invention relates to the technical field of activation furnaces, in particular to an activated carbon activation device.
Background
The active carbon is a black porous solid carbon, and is made up by placing hardwood, fruit shell and bone in a closed container, calcining them into carbon and increasing their pores, or is made up by using coal through the processes of pulverizing, forming or using uniform coal granules through carbonization and activation, and its main component is carbon, and the specific surface area of general active carbon is 500-1700 m/g, so that it possesses strong adsorption property, and the active carbon in the gas mask can be used for filtering gas, and can be used for decolouring and purifying solution. The activated carbon has strong adsorbability and is closely related to the activation in the production process, the porous state and the adsorbability can be achieved only through the activation, and the device adopted in the activated carbon activation process is an activated carbon activation furnace.
The activated carbon activation is mainly divided into three processes, wherein the first process is a drying process, raw materials are preheated to reduce moisture in the raw materials, and the chemical components in the raw materials are not changed due to low temperature; the second process is a pre-carbonization process, the temperature is increased on the basis of the first process, the raw material is heated, unstable components are subjected to decomposition reaction, and chemical components begin to change; the third process is a carbonization process, the temperature is continuously increased, the raw material is rapidly thermally decomposed to realize carbonization, and a porous structure is generated.
The existing activated carbon activation furnace is generally set into three relatively independent split-type structures according to three steps of activated carbon activation, so that the overall occupied space of the existing activated carbon activation furnace is large, and meanwhile, the three parts all need to be heated and all can generate heat loss, so that the energy consumption is high.
Disclosure of Invention
Technical problem to be solved
Aiming at the defects of the prior art, the invention provides an activated carbon activation device, which solves the problems that the existing activated carbon activation furnace is generally set into three relatively independent split structures according to three steps of activated carbon activation, so that the occupied space is large, and the energy consumption is high due to serious heat dissipation.
(II) technical scheme
In order to achieve the purpose, the invention provides the following technical scheme: an activated carbon activation device comprises an overhead base and a chimney, wherein the overhead base is respectively provided with a reaction first-zone furnace wall, a reaction second-zone furnace wall and a reaction third-zone furnace wall, the reaction first-zone furnace wall, the reaction second-zone furnace wall and the reaction third-zone furnace wall are all in vertical cylindrical shapes, and the furnace wall of the reaction third zone is positioned inside the furnace wall of the reaction second zone, the furnace wall of the reaction second zone is positioned inside the furnace wall of the reaction first zone, the first reaction zone furnace wall, the second reaction zone furnace wall and the third reaction zone furnace wall respectively enclose three independent sections of a first reaction zone, a second reaction zone and a third reaction zone, a flat top with a smoke outlet is arranged above the furnace wall of the first reaction area, the furnace wall of the second reaction area and the furnace wall of the third reaction area, a smoke exhaust chamber is arranged above the flat top and communicated with a chimney, a top frame is arranged above the smoke exhaust chamber, and a driving mechanism is arranged on the top frame.
The device is characterized in that a first reaction cylinder, a second reaction cylinder and a third reaction cylinder are respectively arranged in the first reaction zone, the second reaction zone and the third reaction zone, spiral feeders are respectively arranged in the first reaction cylinder, the second reaction cylinder and the third reaction cylinder and are in transmission connection with a driving mechanism, a feed hopper is arranged outside a furnace wall of the first reaction zone, a first channel is arranged between the feed hopper on the furnace wall of the first reaction zone and the first reaction cylinder, a second channel is arranged between the first reaction cylinder and the second reaction cylinder on the furnace wall of the second reaction zone, a third channel is arranged between the second reaction cylinder and the third reaction cylinder on the furnace wall of the third reaction zone, a discharge hopper communicated with the inside of the third reaction cylinder and the outside of a smoke discharge chamber is arranged on the furnace wall of the third reaction zone, an adjustable heating source is arranged below the overhead base, and through holes are respectively arranged on the top and the side surface of the overhead base, and the interiors of the first reaction zone, the second reaction zone and the third reaction zone are respectively provided with an air inlet pipeline communicated with the furnace wall of the reaction three-zone and the outer part of the smoke exhaust chamber.
Preferably, the furnace wall of the first reaction zone, the furnace wall of the second reaction zone and the furnace wall of the third reaction zone are all double-layer hollow structures.
Preferably, the smoke exhaust chamber is arched, and the size of the smoke exhaust chamber is matched with the size of the furnace wall of the reaction three-zone.
Preferably, the driving mechanisms are divided into three groups, and the three groups of driving mechanisms respectively drive the screw feeders of the first reaction zone, the second reaction zone and the third reaction zone.
Preferably, the spiral blade of the spiral feeder is provided with air holes, and the diameter of each air hole is 0.5-0.8 mm.
Preferably, the feed hopper, the first channel and the third channel are respectively located at positions where the side surfaces of the first reaction cylinder and the third reaction cylinder are close to the bottom, the second channel and the discharge hopper are respectively located at positions where the side surfaces of the second reaction cylinder and the third reaction cylinder are close to the top, and the third reaction cylinder is higher than the first reaction cylinder and the second reaction cylinder.
Preferably, the adjustable heating source comprises a burner, a fuel pipeline communicated with the burner and electromagnetic valves arranged on the fuel pipeline, the burner, the fuel pipeline and the electromagnetic valves are divided into three groups, and the burners in the three groups are annularly distributed and respectively correspond to the first reaction zone, the second reaction zone and the third reaction zone.
Preferably, the air inlet pipeline comprises a first air inlet pipeline and a second air inlet pipeline, the first air inlet pipeline and the second air inlet pipeline are arranged in the first reaction area and the second reaction area at intervals, and the first reaction cylinder and the two adjacent second reaction cylinders are communicated with the same first air inlet pipeline and the same second air inlet pipeline respectively.
(III) advantageous effects
The invention provides an activated carbon activation device which has the following beneficial effects.
(1) The first reaction zone, the second reaction zone and the third reaction zone are arranged above the overhead base, and the furnace walls of the first reaction zone, the second reaction zone and the third reaction zone outside the first reaction zone, the second reaction zone and the third reaction zone are surrounded layer by layer to achieve an integration effect, so that the space between two adjacent steps of activation is reduced, and the overall occupied space is reduced; the first reaction zone furnace wall, the second reaction zone furnace wall and the third reaction zone furnace wall are of hollow structures, outward heat dissipation efficiency is reduced, and the first reaction zone furnace wall, the second reaction zone furnace wall and the third reaction zone furnace wall are surrounded layer by layer, so that the effect that the temperature gradually rises from the edge to the middle is achieved, the heat dissipated outwards in the middle can be used as a preheating energy source, the heat transferred inwards in the edge can be used for increasing the temperature for the middle link, the reasonable utilization of the energy source is achieved, the dissipation effect is reduced, energy consumption can be reduced, the problem that the existing activated carbon activation furnace is generally set into three relatively independent split structures according to three steps of activated carbon activation, the occupied space is large, and the heat.
(2) According to the invention, the first reaction cylinder, the second reaction cylinder, the third reaction cylinder, the first channel, the second channel and the third channel are arranged, the first reaction cylinder, the second reaction cylinder and the third reaction cylinder are vertically arranged, the floor area is reduced, the first channel and the third channel are respectively positioned at the positions of the side surfaces of the first reaction cylinder and the third reaction cylinder, which are close to the bottom, and the second channel is positioned at the positions of the side surfaces of the second reaction cylinder and the third reaction cylinder, which are close to the top, so that raw materials move from bottom to top in the first reaction cylinder, then move from top to bottom in the second reaction cylinder, and finally move from bottom to top in the third reaction cylinder, the whole structure is compact, the floor area is reduced, and the process and time for activating the raw materials are not reduced, so that qualified products can be obtained.
(3) According to the invention, the air holes, the adjustable heating source and the air inlet pipeline are arranged, the burner of the adjustable heating source is arranged corresponding to the positions of the first reaction zone, the second reaction zone and the third reaction zone, the first reaction zone, the second reaction zone and the third reaction zone can be independently heated through the electromagnetic valve, meanwhile, air and reaction gas can be introduced into the air inlet pipeline, the effects of cooling and reaction promotion are respectively achieved, the air holes can ensure gas circulation, and therefore, the effect of regulating and controlling the temperatures of the first reaction zone, the second reaction zone and the third reaction zone is achieved, the controllable degree is high, and the practicability is strong.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic view of the internal structure of the present invention;
FIG. 3 is a top plan view of the first, second and third reaction zones of the present invention;
FIG. 4 is a front cross-sectional view of a reaction three zone furnace wall construction of the present invention;
FIG. 5 is a schematic top view of an adjustable heating source according to the present invention;
fig. 6 is a schematic view of the structure of the screw feeder of the present invention.
In the figure: 1. an overhead base; 2. a chimney; 3. the wall of the reaction first zone furnace; 31. a first reaction zone; 32. a first reaction cylinder; 33. a first channel; 4. the furnace wall of the second reaction zone; 41. a second reaction zone; 42. a second reaction cylinder; 43. a second channel; 5. a reaction three-zone furnace wall; 51. a third reaction zone; 52. a third reaction cylinder; 53. a third channel; 6. a smoke outlet; 7. flat top; 8. a smoke exhaust chamber; 9. a top frame; 10. a drive mechanism; 11. a screw feeder; 111. air holes; 12. a feed hopper; 13. a discharge hopper; 14. an adjustable heating source; 141. a burner; 142. a fuel conduit; 143. an electromagnetic valve; 15. a through hole; 16. an air intake duct; 161. a first air inlet pipeline; 162. and a second air inlet pipeline.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
As shown in fig. 1 to 6, the present invention provides a technical solution: an activated carbon activation device comprises an overhead base 1 and a chimney 2, wherein the overhead base 1 is respectively provided with a first reaction zone furnace wall 3, a second reaction zone furnace wall 4 and a third reaction zone furnace wall 5, the first reaction zone furnace wall 3, the second reaction zone furnace wall 4 and the third reaction zone furnace wall 5 are all vertical cylinders, the third reaction zone furnace wall 5 is positioned inside the second reaction zone furnace wall 4, the second reaction zone furnace wall 4 is positioned inside the first reaction zone furnace wall 3, the second reaction zone furnace wall 4 and the third reaction zone furnace wall 5 respectively enclose three independent zones of a first reaction zone 31, a second reaction zone 41 and a third reaction zone 51, a flat top 7 with a smoke exhaust port 6 is arranged above the first reaction zone furnace wall 3, the second reaction zone furnace wall 4 and the third reaction zone furnace wall 5, a smoke exhaust chamber 8 is arranged above the flat top 7, the smoke exhaust chamber 8 is communicated with the chimney 2, a top frame 9 is arranged above the smoke exhaust chamber, the top frame 9 is provided with a driving mechanism 10.
The first reaction zone 31, the second reaction zone 41 and the third reaction zone 51 are respectively provided with a first reaction cylinder 32, a second reaction cylinder 42 and a third reaction cylinder 52 inside, the first reaction cylinder 32, the second reaction cylinder 42 and the third reaction cylinder 52 are arranged from outside to inside in a surrounding way, raw materials in the time of flowing to the adjacent second reaction cylinder 42, third reaction cylinder 52 and feed hopper 12 mutually circulate and finally flow into the third reaction cylinder 52, the whole structure of the reaction second zone furnace wall 4 and the reaction first zone furnace wall 3 is polygonal structure instead of cylindrical structure, the whole volume can be reduced, thereby reducing the surface area, reducing the radiating surface, reducing the manufacturing raw materials and maximizing the cost, and simultaneously realizing the utilization of the internal space, the spiral feeders 11 are arranged inside the first reaction cylinder 32, the second reaction cylinder 42 and the third reaction cylinder 52, and the spiral feeders 11 are in transmission connection with the driving mechanism 10, the outer part of the first reaction zone furnace wall 3 is provided with a feed hopper 12, a first channel 33 is arranged between the feed hopper 12 and the first reaction cylinder 32 on the first reaction zone furnace wall 3, a second channel 43 is arranged between the first reaction cylinder 32 and the second reaction cylinder 42 on the second reaction zone furnace wall 4, a third channel 53 is arranged between the second reaction cylinder 42 and the third reaction cylinder 52 on the third reaction zone furnace wall 5, a discharge hopper 13 communicated with the inside of the third reaction cylinder 52 and the outside of the smoke exhaust chamber 8 is arranged on the third reaction zone furnace wall 5, an adjustable heating source 14 is arranged below the overhead base 1, the top and the side surface of the overhead base 1 are provided with through holes 15, and the inner parts of the first reaction zone 31, the second reaction zone 41 and the third reaction zone 51 are respectively provided with an air inlet pipeline 16 communicated with the outside of the third reaction zone 5 and the smoke exhaust chamber 8.
As a technical optimization scheme of the invention, the first reaction zone furnace wall 3, the second reaction zone furnace wall 4 and the third reaction zone furnace wall 5 are all double-layer hollow structures, the overall structural strength is enhanced between the two layers through connecting ribs, and the heat preservation effect and the effect of reducing heat loss to the outside are enhanced through the hollow structures.
As a technical optimization scheme of the invention, the smoke exhaust chamber 8 is arched, the size of the smoke exhaust chamber 8 is matched with that of the furnace wall 5 of the reaction three-zone, the bottom of the overhead base 1 is heated, hot air flows upwards, meanwhile, smoke generated by the first reaction zone 31, the second reaction zone 41 and the third reaction zone 51 also flows upwards and is exhausted to the outside through the smoke exhaust chamber 8 and the chimney 2, and the chimney 2 is connected with a tail gas treatment device for filtering, cooling and the like of tail gas.
As a technical optimization scheme of the present invention, the driving mechanisms 10 are divided into three groups, the three groups of driving mechanisms 10 respectively drive the screw feeders 11 of the first reaction zone 31, the second reaction zone 41 and the third reaction zone 51, the three groups of screw feeders 11 respectively lift the raw materials of the first reaction zone 31 and the third reaction zone 51 and convey the raw materials of the second reaction zone 41 downwards, the three groups of driving mechanisms 10 correspond to three independent zones of the first reaction zone 31, the second reaction zone 41 and the third reaction zone 51, the driving mechanism 10 corresponding to each independent zone may be one driving multiple screw feeders 11, or each screw feeder 11 may be equipped with one driving mechanism 10, and the driving mechanisms 10 are speed motors and their related components, and the power supply mode is an external power supply.
As a technical optimization scheme of the invention, the spiral blade of the spiral feeder 11 is provided with air holes 111, the diameter of each air hole 111 is 0.5-0.8 mm, and the air holes 111 are used for air circulation and heat transmission.
As a technical optimization scheme of the invention, the feed hopper 12, the first channel 33 and the third channel 53 are respectively positioned at the positions of the side surfaces of the first reaction cylinder 32 and the third reaction cylinder 52 close to the bottom, the second channel 43 and the discharge hopper 13 are respectively positioned at the positions of the side surfaces of the second reaction cylinder 42 and the third reaction cylinder 52 close to the top, the third reaction cylinder 52 is higher than the first reaction cylinder 32 and the second reaction cylinder 42, the raw material moves from bottom to top in the first reaction cylinder 32, then moves from top to bottom in the second reaction cylinder 42, and finally moves from bottom to top in the third reaction cylinder 52, so that the occupied area of the whole device is reduced, and the activation step and time are ensured.
As a technical optimization scheme of the present invention, the adjustable heating source 14 includes a burner 141, a fuel pipeline 142 communicated with the burner 141, and an electromagnetic valve 143 disposed on the fuel pipeline 142, the burner 141, the fuel pipeline 142, and the electromagnetic valve 143 are divided into three groups, the three groups of burners 141 are annularly distributed and disposed to correspond to the first reaction zone 31, the second reaction zone 41, and the third reaction zone 51, respectively, and the three groups of adjustable heating sources 14 can simultaneously or respectively supply heat to the first reaction zone 31, the second reaction zone 41, and the third reaction zone 51.
As a technical optimization scheme of the invention, the air inlet pipeline 16 comprises a first air inlet pipeline 161 and a second air inlet pipeline 162, the first air inlet pipeline 16 is used for supplementing air and reaction gas, the first air inlet pipeline 161 and the second air inlet pipeline 162 are arranged in the first reaction zone 31 and the second reaction zone 41 at intervals, two adjacent first reaction cylinders 32 and two adjacent second reaction cylinders 42 are respectively communicated with the same first air inlet pipeline 161 and the second air inlet pipeline 162, the number of the air inlet pipelines 16 is reduced, and the air inlet pipelines 16 of the same type in the same reaction zone are connected to the same connecting pipe outside the smoke exhaust chamber 8 and are connected with a valve and an air source.
The working principle is as follows: raw materials pass through a feed hopper 12 and a passage I33 to reach a first reaction cylinder 32 in a first reaction zone 31, a driving mechanism 10 drives the raw materials in the first reaction cylinder 32 to move from bottom to top in the first reaction cylinder 32 and then pass through a passage II 43 to reach a second reaction cylinder 42 in a second reaction zone 41, the raw materials move from top to bottom in the second reaction cylinder 42, pass through a passage III 53 at the bottom to reach a third reaction cylinder 52 in a third reaction zone 51, finally move from bottom to top in the third reaction cylinder 52 and are discharged through a discharge hopper 13, the first reaction zone 31, the second reaction zone 41 and the third reaction zone 51 are all arranged above an overhead base 1, heat can be independently or simultaneously supplied to the first reaction zone 31, the second reaction zone 41 and the third reaction zone 51 through electromagnetic valves 143, and air and reaction gas can be introduced into an air inlet pipe 16, the effects of cooling and reaction promotion are achieved respectively, the air holes 111 can ensure gas circulation, and hot air and smoke generated by reaction are discharged through the smoke outlet 6, the smoke discharging chamber 8 and the chimney 2.
In conclusion, the invention solves the problems that the existing activated carbon activation furnace is generally set into three relatively independent split structures according to three steps of activated carbon activation, which results in larger occupied space and high energy consumption due to serious heat loss by arranging the overhead base 1, the first reaction zone 31, the second reaction zone 41, the third reaction zone 51 and the adjustable heating source 14.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (8)
1. The utility model provides an active carbon activation device, includes built on stilts base (1) and chimney (2), its characterized in that: the overhead base (1) is respectively provided with a first reaction zone furnace wall (3), a second reaction zone furnace wall (4) and a third reaction zone furnace wall (5), the first reaction zone furnace wall (3), the second reaction zone furnace wall (4) and the third reaction zone furnace wall (5) are all vertical cylindrical, the third reaction zone furnace wall (5) is positioned inside the second reaction zone furnace wall (4), the second reaction zone furnace wall (4) is positioned inside the first reaction zone furnace wall (3), the second reaction zone furnace wall (4) and the third reaction zone furnace wall (5) are respectively enclosed into three independent zones, namely a first reaction zone (31), a second reaction zone (41) and a third reaction zone (51), a flat top (7) with a smoke exhaust port (6) is arranged above the first reaction zone furnace wall (3), the second reaction zone furnace wall (4) and the third reaction zone furnace wall (5), and a smoke exhaust chamber (8) is arranged above the flat top (7), the smoke exhaust chamber (8) is communicated with the chimney (2), an upper frame (9) is arranged above the smoke exhaust chamber (8), and a driving mechanism (10) is arranged on the upper frame (9);
the inside of the first reaction zone (31), the second reaction zone (41) and the third reaction zone (51) is respectively provided with a first reaction cylinder (32), a second reaction cylinder (42) and a third reaction cylinder (52), the inside of the first reaction cylinder (32), the second reaction cylinder (42) and the third reaction cylinder (52) is provided with a spiral feeder (11), the spiral feeder (11) is in transmission connection with a driving mechanism (10), the outside of the furnace wall (3) of the first reaction zone is provided with a feed hopper (12), a first channel (33) is arranged between the feed hopper (12) on the furnace wall (3) of the first reaction zone and the first reaction cylinder (32), a second channel (43) is arranged between the first reaction cylinder (32) and the second reaction cylinder (42) on the furnace wall (4) of the second reaction zone, and a third channel (53) is arranged between the second reaction cylinder (42) and the third reaction cylinder (52) on the furnace wall (5) of the third reaction zone, and a discharge hopper (13) communicated with the inside of the third reaction cylinder (52) and the outside of the smoke exhaust chamber (8) is arranged on the reaction three-zone furnace wall (5), an adjustable heating source (14) is arranged below the overhead base (1), through holes (15) are formed in the top and the side surface of the overhead base (1), and air inlet pipelines (16) communicated with the outside of the reaction three-zone furnace wall (5) and the smoke exhaust chamber (8) are respectively arranged in the first reaction zone (31), the second reaction zone (41) and the third reaction zone (51).
2. The activated carbon activation apparatus according to claim 1, wherein: the furnace wall (3) of the first reaction zone, the furnace wall (4) of the second reaction zone and the furnace wall (5) of the third reaction zone are all of double-layer hollow structures.
3. The activated carbon activation apparatus according to claim 1, wherein: the smoke exhaust chamber (8) is arched, and the size of the smoke exhaust chamber (8) is matched with that of the furnace wall (5) of the reaction three-zone.
4. The activated carbon activation apparatus according to claim 1, wherein: the driving mechanisms (10) are divided into three groups, and the three groups of driving mechanisms (10) respectively drive the screw feeders (11) of the first reaction zone (31), the second reaction zone (41) and the third reaction zone (51).
5. The activated carbon activation apparatus according to claim 1, wherein: air holes (111) are formed in spiral blades of the spiral feeder (11), and the diameter of each air hole (111) is 0.5-0.8 mm.
6. The activated carbon activation apparatus according to claim 1, wherein: the feeding hopper (12), the first channel (33) and the third channel (53) are respectively positioned at the positions, close to the bottom, of the side surfaces of the first reaction cylinder (32) and the third reaction cylinder (52), the second channel (43) and the discharging hopper (13) are respectively positioned at the positions, close to the top, of the side surfaces of the second reaction cylinder (42) and the third reaction cylinder (52), and the third reaction cylinder (52) is higher than the first reaction cylinder (32) and the second reaction cylinder (42).
7. The activated carbon activation apparatus according to claim 1, wherein: adjustable heating source (14) include combustor (141), fuel pipe (142) and solenoid valve (143) of setting on fuel pipe (142) that communicate with combustor (141), fuel pipe (142) and solenoid valve (143) divide into three groups, three groups combustor (141) all are the annular distribution and set up respectively with first reaction zone (31), second reaction zone (41) and third reaction zone (51) position correspondence.
8. The activated carbon activation apparatus according to claim 1, wherein: the air inlet pipeline (16) comprises a first air inlet pipeline (161) and a second air inlet pipeline (162), the first air inlet pipeline (161) and the second air inlet pipeline (162) are arranged in the first reaction area (31) and the second reaction area (41) at intervals, and the first reaction cylinder (32) and the second reaction cylinder (42) are communicated with the same first air inlet pipeline (161) and the second air inlet pipeline (162) respectively.
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| CN202011214862.6A CN112250070A (en) | 2020-11-04 | 2020-11-04 | Activated carbon activation device |
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| CN202011214862.6A CN112250070A (en) | 2020-11-04 | 2020-11-04 | Activated carbon activation device |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB242659A (en) * | 1924-11-08 | 1926-09-30 | Naamlooze Vennootschap Alge Me | Improvements in the process of and apparatus for, manufacturing active carbon |
| RU2321612C1 (en) * | 2006-09-11 | 2008-04-10 | Общество с ограниченной ответственностью "Научно-технический центр "Альтернатива" | Mode and installation for receiving activated carbon |
| CN101538632A (en) * | 2009-02-05 | 2009-09-23 | 丁家伟 | Preparation process and device of sponge iron |
| CN104099111A (en) * | 2014-07-21 | 2014-10-15 | 武汉海德新能源投资有限公司 | Continuous and overall biomass pyrolysis furnace |
| CN209098194U (en) * | 2018-08-31 | 2019-07-12 | 张子华 | Nonmetallic electricity burns Activated Carbon Production kiln |
| CN209853735U (en) * | 2019-04-04 | 2019-12-27 | 安国神洁环保科技有限公司 | Carbonization-activation integrated activated carbon production device |
| US20200325399A1 (en) * | 2019-10-30 | 2020-10-15 | Zhejiang University Of Science & Technology | Biomass gas-carbon co-production reactor and reaction method thereof |
-
2020
- 2020-11-04 CN CN202011214862.6A patent/CN112250070A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB242659A (en) * | 1924-11-08 | 1926-09-30 | Naamlooze Vennootschap Alge Me | Improvements in the process of and apparatus for, manufacturing active carbon |
| RU2321612C1 (en) * | 2006-09-11 | 2008-04-10 | Общество с ограниченной ответственностью "Научно-технический центр "Альтернатива" | Mode and installation for receiving activated carbon |
| CN101538632A (en) * | 2009-02-05 | 2009-09-23 | 丁家伟 | Preparation process and device of sponge iron |
| CN104099111A (en) * | 2014-07-21 | 2014-10-15 | 武汉海德新能源投资有限公司 | Continuous and overall biomass pyrolysis furnace |
| CN209098194U (en) * | 2018-08-31 | 2019-07-12 | 张子华 | Nonmetallic electricity burns Activated Carbon Production kiln |
| CN209853735U (en) * | 2019-04-04 | 2019-12-27 | 安国神洁环保科技有限公司 | Carbonization-activation integrated activated carbon production device |
| US20200325399A1 (en) * | 2019-10-30 | 2020-10-15 | Zhejiang University Of Science & Technology | Biomass gas-carbon co-production reactor and reaction method thereof |
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