CN105219413A - Machine-made carbon powder is dried and carbonizing apparatus - Google Patents
Machine-made carbon powder is dried and carbonizing apparatus Download PDFInfo
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- CN105219413A CN105219413A CN201510712892.2A CN201510712892A CN105219413A CN 105219413 A CN105219413 A CN 105219413A CN 201510712892 A CN201510712892 A CN 201510712892A CN 105219413 A CN105219413 A CN 105219413A
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- coil pipe
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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Abstract
The invention discloses a kind of machine-made carbon powder to dry and carbonizing apparatus, comprise coaxially sheathed inner furnace body and external furnace body, the internal space of described inner furnace body is combustion chamber, space between described inner furnace body and external furnace body is drying shed, described drying shed is provided with and is provided with the first coil pipe and the second coil pipe from the bottom to top, described first coil pipe and the second coil pipe are cylindrical screw wire, the upper end of described first coil pipe is communicated with feeding unit, the lower end of described first coil pipe is communicated with the entrance of the first hydrofuge bucket by the first blower fan, the lower end of described second coil pipe is connected with the outlet of the first hydrofuge bucket, the upper end of described second coil pipe is connected with the second hydrofuge bucket by the second blower fan, first, material is sucked first by two blower fans respectively, in two hydrofuge buckets.Comparatively moist material from top to bottom runs at the first coil pipe, and running resistance is little, after first drying, run from the bottom to top along the second coil pipe, dry fully, overall drying efficiency is high again, and first and second coil pipe is arranged from the bottom to top, structure is neat, compact, is convenient to installation, inspection and maintenance.
Description
Technical field
The present invention is that a kind of machine-made carbon powder is dried and carbonizing apparatus.
Background technology
The powder of machine-made carbon powder as rice husk, Pericarppium arachidis hypogaeae, boll hull, corn cob, corn stalk, kaoliang stalk etc. needs to dry powder before making organic rod.CN201126301Y discloses a kind of powder drying device, this equipment is by first, two coil pipes and first, two hydrofuge buckets realize powder second dries, first coil pipe and the second coil pipe staggered arrangement, the upper inlet entering the first hydrofuge bucket from the upper port of the first coil pipe by the air draught power of the first blower fan after material enters the first coil pipe from the first coil pipe lower port carries out hydrofuge, then material enters the second coil pipe and the second hydrofuge bucket from the lower exit port of the first hydrofuge bucket, Problems existing is, the trend of material in the first coil pipe is from bottom to up, and material has just entered the first coil pipe and has made comparatively moist, the resistance of the operation of such material in the first coil pipe is larger, drying efficiency is low, in addition, first coil pipe and the second coil pipe staggered arrangement, cause the radial space of toasting chamber larger, simultaneously first, disorderly and unsystematic the causing of two coil pipes installs, maintenance, safeguard not convenient.
Summary of the invention
For the deficiency that prior art exists, the object of the invention is to provide a kind of machine-made carbon powder and dries and carbonizing apparatus, and drying efficiency is high, is convenient to installation, maintenance, safeguards.
To achieve these goals, the present invention realizes by the following technical solutions: a kind of machine-made carbon powder is dried and carbonizing apparatus, comprise coaxially sheathed inner furnace body and external furnace body, the internal space of described inner furnace body is combustion chamber, space between described inner furnace body and external furnace body is drying shed, described drying shed is provided with and is provided with the first coil pipe and the second coil pipe from the bottom to top, described first coil pipe and the second coil pipe are cylindrical screw wire, the upper end of described first coil pipe is communicated with feeding unit, the lower end of described first coil pipe is communicated with the entrance of the first hydrofuge bucket by the first blower fan, the lower end of described second coil pipe is connected with the outlet of the first hydrofuge bucket, the upper end of described second coil pipe is connected with the second hydrofuge bucket by the second blower fan, first, material is sucked first by two blower fans respectively, in two hydrofuge buckets.
Further, also comprise the first U-tube, the two ends of described first U-tube respectively with lower end and the combustion chamber of the second coil pipe, the outlet of described first hydrofuge bucket is communicated with the stage casing of the first U-tube.
Further, the 3rd coil pipe be positioned in cylindrical screw wire above the second coil pipe is also provided with in described drying shed, the lower end of described 3rd coil pipe and the outlet of the second hydrofuge bucket be communicated with, the upper end of described 3rd coil pipe is connected with the 3rd hydrofuge bucket by the 3rd blower fan, and the material in the 3rd coil pipe is introduced in the 3rd hydrofuge bucket by described 3rd blower fan.
Further, also comprise the second U-tube, the two ends of described second U-tube respectively with lower end and the combustion chamber of the 3rd coil pipe, the outlet of described second hydrofuge bucket is communicated with the stage casing of the second U-tube.
Further, described second U-tube is provided with the opening for feed that can add new material, through second coil pipe dry after material with send into after the new mixing of materials that opening for feed adds in the 3rd coil pipe.
Further, be provided with flow control valve between the upper end of described first coil pipe and feeding unit, the outlet of described 3rd hydrofuge bucket is provided with the temperature sensor detecting temperature of charge.
Further, described inner furnace body inside is provided with coaming plate, forms open-topped burning chamber between described coaming plate and inner furnace body, is provided with the conducting strip that two ends contact with inner furnace body with coaming plate respectively in described burning chamber.
Beneficial effect of the present invention: a kind of machine-made carbon powder of the present invention is dried and carbonizing apparatus, comprise coaxially sheathed inner furnace body and external furnace body, the internal space of described inner furnace body is combustion chamber, space between described inner furnace body and external furnace body is drying shed, described drying shed is provided with and is provided with the first coil pipe and the second coil pipe from the bottom to top, described first coil pipe and the second coil pipe are cylindrical screw wire, the upper end of described first coil pipe is communicated with feeding unit, the lower end of described first coil pipe is communicated with the entrance of the first hydrofuge bucket by the first blower fan, the lower end of described second coil pipe is connected with the outlet of the first hydrofuge bucket, the upper end of described second coil pipe is connected with the second hydrofuge bucket by the second blower fan, first, material is sucked first by two blower fans respectively, in two hydrofuge buckets.Comparatively moist material from top to bottom runs at the first coil pipe, and running resistance is little, after first drying, run from the bottom to top along the second coil pipe, dry fully, overall drying efficiency is high again, and first and second coil pipe is arranged from the bottom to top, structure is neat, compact, is convenient to installation, inspection and maintenance.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of machine-made carbon powder oven dry of the present invention and carbonizing apparatus;
Embodiment
The technique means realized for making the present invention, creation characteristic, reaching object and effect is easy to understand, below in conjunction with embodiment, setting forth the present invention further.
Refer to figure, the invention provides a kind of technical scheme: a kind of machine-made carbon powder is dried and carbonizing apparatus, comprise coaxially sheathed inner furnace body 1 and external furnace body 2, the internal space of described inner furnace body 1 is combustion chamber 3, space between described inner furnace body 1 and external furnace body 2 is drying shed 4, described drying shed 4 is provided with and is provided with the first coil pipe 5 and the second coil pipe 6 from the bottom to top, described first coil pipe 5 and the second coil pipe 6 are cylindrical screw wire, the upper end of described first coil pipe 5 is communicated with feeding unit 22, the lower end of described first coil pipe 5 is communicated with the entrance of the first hydrofuge bucket 8 by the first blower fan 7, the lower end of described second coil pipe 6 is connected with the outlet of the first hydrofuge bucket 8, the upper end of described second coil pipe 6 is connected with the second hydrofuge bucket 10 by the second blower fan 9, first, two blower fans 7, material is sucked first by 9 respectively, two hydrofuge buckets 8, in 10.
The heat produced in combustion chamber 3 is passed in drying shed 4 through inner furnace body 1, thus carries out heating, drying to the material in first and second coil pipe and powdered biomass.Material is through elevating hopper, separating screen, the feeding units such as spiral pump 22 enter the top of the first coil pipe 5, the air draught power that first blower fan 5 produces makes material 5 internal screws in the first coil pipe run downwards, running resistance is compared when running from the bottom to top little, in operational process in the first coil pipe, material is by first drying, material after first drying enters the first hydrofuge bucket 8, the moisture entered in the first hydrofuge bucket 8 with material discharges the first hydrofuge bucket 8 through the first dehumidification tube 23 from the bottom to top, material then enters the bottom of the second coil pipe 6 from the outlet bottom the first hydrofuge bucket 8, now, material is after first drying, moisture reduces, then the air draught power of the second blower fan 9 makes material enter the second coil pipe 6 and along the second coil pipe 6 spiral from the bottom to top, spiral is compared from top to bottom to run and can be made increase the duration of contact of material and the second coil pipe from the bottom to top, and running resistance to compare the material resistance that enters when drying shed directly runs from the bottom to top of first time little.Material enters after the second hydrofuge bucket 10 through the second blower fan 9, and moisture discharges the second hydrofuge bucket 10 through the second dehumidification tube 24 from the bottom to top, and material is then discharged from the outlet at bottom of the second hydrofuge bucket 10.
Material at the first coil pipe from top to bottom, in the second coil pipe operation scheme from the bottom to top, both ensure that the working time of material, and in turn ensure that simultaneously and namely ensure that the drying efficiency of material by the drying effect of material.
Also comprise the first U-tube 11, the two ends of described first U-tube 11 respectively with lower end and the combustion chamber of the second coil pipe 6, the outlet of described first hydrofuge bucket 8 is communicated with the stage casing of the first U-tube 11.Heat in the outlet material of the first hydrofuge bucket 8 and combustion chamber all together enters after in the first U-tube and enters the second coil pipe 6 again, make the heat exchange of material in the second coil pipe 6 faster, hot gas namely in combustion chamber 3 directly enters the second coil pipe 6 pairs of materials and dries, and drying effect is better.
The 3rd coil pipe 13 be positioned in cylindrical screw wire above the second coil pipe is also provided with in described drying shed 4, the lower end of described 3rd coil pipe 13 and the outlet of the second hydrofuge bucket 10 be communicated with, the upper end of described 3rd coil pipe 13 is connected with the 3rd hydrofuge bucket 15 by the 3rd blower fan 14, and the material in the 3rd coil pipe is introduced in the 3rd hydrofuge bucket 15 by described 3rd blower fan 14.In like manner, material enters the 3rd coil pipe 13 by the 3rd blower fan 14, and material third time is dried, and drying effect is better, moisture in material is discharged with the 3rd dehumidification tube 25 in reason the 3rd hydrofuge bucket 15, and material is then discharged from the outlet bottom the 3rd hydrofuge bucket 15 and entered subsequent technique.
Also comprise the second U-tube 12, the two ends of described second U-tube 12 respectively with lower end and the combustion chamber of the 3rd coil pipe, the outlet of described second hydrofuge bucket 10 is communicated with the stage casing of the second U-tube 12, and the effect of the second U-tube 12 is identical with the first U-tube.In like manner, also the 3rd U-tube is had in the outlet of feeding unit, the effect of the 3rd U-tube is identical with first and second U-tube, sends in the first coil pipe while material being imported the first coil pipe upper end by the hot gas of combustion chamber, accelerates the drying rate of material in the first coil pipe.
Described second U-tube 12 is provided with the opening for feed 16 that can add new material, through second coil pipe dry after material with send into after the new mixing of materials that opening for feed 16 adds in the 3rd coil pipe 13.Due to from feeding unit 22 material out drying shed 4 successively after first and second coil pipe by twice heating, drying, now the temperature of material is higher, the mixing of materials after the material and twice oven dry that new needs dry is added by opening for feed 16, mixed material is dried through the 3rd coil pipe 13 more just directly can meet drying effect, make the material added through opening for feed 16 without the need to just completing oven dry by first and second coil pipe, substantially increase drying efficiency, and save the energy.
Be provided with flow control valve 17 between the upper end of described first coil pipe 5 and feeding unit, the outlet of described 3rd hydrofuge bucket 15 is provided with the temperature sensor 18 detecting temperature of charge.Flow control valve 17 regulates the flow of material, the temperature of finished product materials then measured by temperature sensor 18, by flow control valve 17 adjust flux, to meet the temperature requirements of material outlet, the flow of flow control valve 17 is changed in other words according to the temperature of material, after making the flow of the material entering drying shed and drying, the temperature of material matches, and controls more accurate.
Described inner furnace body inside is provided with coaming plate 19, open-topped burning chamber 20 is formed between described coaming plate and inner furnace body, part in inner furnace body beyond corresponding burning chamber 20 is heat collector cavity 21, is provided with the conducting strip 21 that two ends contact with inner furnace body with coaming plate respectively in described burning chamber.The heat of burning chamber 20 is passed to drying shed 4 and heat collector cavity 21 by conducting strip 20, can place organic rod, utilize the heat in heat collector cavity 21 to carbonize organic rod in heat collector cavity 21 by pyrolysis still.
More than show and describe ultimate principle of the present invention and principal character and advantage of the present invention, to those skilled in the art, obviously the invention is not restricted to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present invention or essential characteristic, the present invention can be realized in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present invention is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the present invention.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (7)
1. a machine-made carbon powder is dried and carbonizing apparatus, comprise coaxially sheathed inner furnace body (1) and external furnace body (2), the internal space of described inner furnace body (1) is combustion chamber (3), space between described inner furnace body (1) and external furnace body (2) is drying shed (4), it is characterized in that: described drying shed (4) is provided with and is provided with the first coil pipe (5) and the second coil pipe (6) from the bottom to top, described first coil pipe (5) and the second coil pipe (6) are cylindrical screw wire, the upper end of described first coil pipe (5) is communicated with feeding unit (22), the lower end of described first coil pipe (5) is communicated with the entrance of the first hydrofuge bucket (8) by the first blower fan (7), the lower end of described second coil pipe (6) and the outlet of the first hydrofuge bucket (8), the upper end of described second coil pipe (6) is connected with the second hydrofuge bucket (10) by the second blower fan (9), first, two blower fans (7, 9) respectively material is sucked first, two hydrofuge buckets (8, 10) in.
2. machine-made carbon powder according to claim 1 is dried and carbonizing apparatus, it is characterized in that: also comprise the first U-tube (11), the two ends of described first U-tube (11) respectively with lower end and the combustion chamber of the second coil pipe, the outlet of described first hydrofuge bucket (8) is communicated with the stage casing of the first U-tube (11).
3. machine-made carbon powder according to claim 2 is dried and carbonizing apparatus, it is characterized in that: in described drying shed (4), be also provided with the 3rd coil pipe (13) be positioned in cylindrical screw wire above the second coil pipe, the lower end of described 3rd coil pipe (13) and the outlet of the second hydrofuge bucket (10) be communicated with, the upper end of described 3rd coil pipe (13) is connected with the 3rd hydrofuge bucket (15) by the 3rd blower fan (14), and the material in the 3rd coil pipe is introduced in the 3rd hydrofuge bucket (15) by described 3rd blower fan (14).
4. machine-made carbon powder according to claim 3 is dried and carbonizing apparatus, it is characterized in that: also comprise the second U-tube (12), the two ends of described second U-tube (12) respectively with lower end and the combustion chamber of the 3rd coil pipe, the outlet of described second hydrofuge bucket (10) is communicated with the stage casing of the second U-tube (12).
5. machine-made carbon powder according to claim 4 is dried and carbonizing apparatus, it is characterized in that: described second U-tube (12) is provided with the opening for feed (16) that can add new material, through second coil pipe dry after material with send into after the new mixing of materials that opening for feed (16) adds in the 3rd coil pipe (13).
6. machine-made carbon powder according to claim 5 is dried and carbonizing apparatus, it is characterized in that: be provided with flow control valve (17) between the upper end of described first coil pipe (5) and feeding unit, the outlet of described 3rd hydrofuge bucket (15) is provided with the temperature sensor (18) detecting temperature of charge.
7. machine-made carbon powder according to claim 6 is dried and carbonizing apparatus, it is characterized in that: described inner furnace body inside is provided with coaming plate (19), form open-topped burning chamber (20) between described coaming plate and inner furnace body, in described burning chamber, be provided with the conducting strip (21) that two ends contact with inner furnace body with coaming plate respectively.
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CN201510712892.2A CN105219413B (en) | 2015-10-28 | 2015-10-28 | Mechanism carbon powder is dried and carbonizing apparatus |
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CN201510712892.2A CN105219413B (en) | 2015-10-28 | 2015-10-28 | Mechanism carbon powder is dried and carbonizing apparatus |
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CN105219413B CN105219413B (en) | 2018-06-01 |
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CN201138117Y (en) * | 2007-10-15 | 2008-10-22 | 姚金福 | Powder drying apparatus |
CN101464091A (en) * | 2008-12-31 | 2009-06-24 | 张文华 | Vent gas circulating type spiral pipe blast drier and its drying method |
CN201883075U (en) * | 2010-11-12 | 2011-06-29 | 西峡龙成特种材料有限公司 | Coal decomposition device |
CN205046057U (en) * | 2015-10-28 | 2016-02-24 | 重庆市竹海新能源开发有限公司 | Dry and carbomorphism device in mechanism powdered carbon end |
CN205300196U (en) * | 2015-10-28 | 2016-06-08 | 重庆市竹海新能源开发有限公司 | Mechanism carbon powder drying -machine |
CN205300187U (en) * | 2015-10-28 | 2016-06-08 | 重庆市竹海新能源开发有限公司 | Mechanism carbon powder drying equipment |
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2015
- 2015-10-28 CN CN201510712892.2A patent/CN105219413B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CN2864532Y (en) * | 2005-12-30 | 2007-01-31 | 项欣平 | Powder drier |
CN201138117Y (en) * | 2007-10-15 | 2008-10-22 | 姚金福 | Powder drying apparatus |
CN101140132A (en) * | 2007-10-26 | 2008-03-12 | 唐勇军 | Powder second drying apparatus |
CN201126301Y (en) * | 2007-10-26 | 2008-10-01 | 唐勇军 | Powder drying apparatus |
CN101464091A (en) * | 2008-12-31 | 2009-06-24 | 张文华 | Vent gas circulating type spiral pipe blast drier and its drying method |
CN201883075U (en) * | 2010-11-12 | 2011-06-29 | 西峡龙成特种材料有限公司 | Coal decomposition device |
CN205046057U (en) * | 2015-10-28 | 2016-02-24 | 重庆市竹海新能源开发有限公司 | Dry and carbomorphism device in mechanism powdered carbon end |
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CN205300187U (en) * | 2015-10-28 | 2016-06-08 | 重庆市竹海新能源开发有限公司 | Mechanism carbon powder drying equipment |
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