CN205528594U - Continuous retort of multilayer - Google Patents
Continuous retort of multilayer Download PDFInfo
- Publication number
- CN205528594U CN205528594U CN201620113107.1U CN201620113107U CN205528594U CN 205528594 U CN205528594 U CN 205528594U CN 201620113107 U CN201620113107 U CN 201620113107U CN 205528594 U CN205528594 U CN 205528594U
- Authority
- CN
- China
- Prior art keywords
- carbonization chamber
- carbonization
- carbomorphism
- bed
- rotating shaft
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000003763 carbonization Methods 0.000 claims 22
- 210000000078 claw Anatomy 0.000 claims 3
- 238000007599 discharging Methods 0.000 claims 3
- 239000003610 charcoal Substances 0.000 claims 1
- 230000008676 import Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract 4
- 239000002994 raw material Substances 0.000 abstract 4
- 238000002485 combustion reaction Methods 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 238000000197 pyrolysis Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Classifications
-
- 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
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
The utility model discloses a continuous retort of multilayer, it comprises screw feeding ware, carbomorphism room, combustion chamber and spiral discharge ware. The utility model discloses a dry distillation technology, timber, the carbomorphism room is added from the screw feeding ware in succession to wooden raw materials such as shell, it makes the indoor raw materials carbomorphism of carbomorphism to heat the carbomorphism room through the combustion chamber, unload through rotatory drive of motor that the harrow is rotatory unloads the raw materials from top carbomorphism bed successive layer in that the carbomorphism is indoor, the raw materials good up to the carbomorphism gets into the spiral discharge ware, discharge from the export of spiral discharge ware again, reach serialization production, the accessory substance flue gas that produces in the production passes through the retort gas outlet and discharges. The utility model discloses simple structure, each part combine to link up closely, convenient operation, safety and stability, and efficient, the production process is totally closed, can not produce the environment and pollute, has also realized serialization production.
Description
Technical field
This utility model relates to a kind of multilamellar continuous carbonization furnace, belongs to carbonization device technical field.
Background technology
The wood material such as timber, shell anoxia or hypoxic under the conditions of, heating can occur degradation reaction, generates wood
Charcoal, Linesless charcoal is to maintain the impure amorphous carbon of residual tar in the original structure of timber and hole, is widely used as industry metallurgy also
Former dose and fuel, also play significant role in fields such as purification of water quality, pollutant absorption.
At present, Linesless charcoal produces the overwhelming majority and uses local method burning process, by a burning part in soil system or brick kiln
Raw material, reaches carbonization temperature in making kiln, then cold stoking, thus there is a lot of problem, as big in fuel consumption, the thermal efficiency is low, raw
The product cycle is long, unstable product quality, it is often more important that can not operate continuously, impact batch production.
Summary of the invention
This utility model is to solve existing problem in the art, it is provided that a kind of multilamellar continuous carbonization furnace.
Problem described in the utility model is solved by techniques below scheme: a kind of multilamellar continuous carbonization furnace, it is by spiral
Feeder, carbonization chamber, combustor and spiral discharging device composition, described carbonization chamber is provided with charging aperture, discharging opening, described carbonization chamber
Charging aperture be connected with the outlet of feeding screw, the discharging opening of described carbonization chamber is connected with the import of spiral discharging device,
Described carbonization chamber is provided with multiple carbonization bed, and described carbonization bed is two or more, and described carbonization bed is semi-circular structure, institute
The semicircle circumference stating carbonization bed is connected with inside carbonization chamber, and described carbonization bed is crisscross arranged in carbonization chamber from top to bottom, described
Being provided with central rotating shaft in carbonization chamber, described central rotating shaft is located at the axle center of carbonization chamber, and described central rotating shaft is from carbonization chamber top
Extending to bottom of carbonization chamber, described central rotating shaft self can rotate around center, described central rotating shaft is welded with and unloads
Claw, described in unload claw and be located at and be close to bed surface on carbonization bed, described in unload claw and be provided with rake teeth, described carbonization ceiling outer circle face
Center is provided with motor, and the rotary shaft of described motor is connected with central rotating shaft, and described carbonization chamber has combustor, described burning
Room and carbonization chamber junction are provided with heat sink, and described combustor is provided with hot gas conduit, and described hot gas conduit extends to carbonization chamber
Interior bottom, described hot gas conduit is provided with pore, and described carbonization chamber upper end is provided with retort gas outlet.
This utility model uses distillation process, and the wood material such as timber, shell is added continuously to charcoal from feeding screw
Change room, by combustor carbonization chamber heated and make the raw material carbonization in carbonization chamber produce Linesless charcoal, by electricity in carbonization chamber
Machine rotarily drives and unloads claw rotation by raw material from top carbonization bed successively discharging, until the raw material entrance spiral discharging that carbonization is good
Device, then discharging from spiral discharging device outlet, reaching continuous prodution, the by-product flue gas produced in production is by carbonization furnace gas
Body outlet is discharged.
This utility model simple in construction, each parts combine linking closely, easy to operate, safety and stability, and efficiency is high, produces
Journey is totally-enclosed, will not produce environment and pollute, also achieve continuous prodution.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, each part numbers is: 1-carbonization chamber；2-combustor；3-motor；4-feeding screw；5-spiral discharging device；
6-charging aperture；7-discharging opening；8-carbonization bed；9-unloads claw；10-retort gas outlet；11-heat sink；12-hot gas conduit；
13-pore；14-central rotating shaft；15-rake teeth.
Detailed description of the invention
With reference to the accompanying drawings this utility model detailed description of the invention is described in detail.
Seeing Fig. 1, a kind of multilamellar continuous carbonization furnace, it is by feeding screw 4, carbonization chamber 1, combustor 2 and spiral discharging
Device 5 forms, and described carbonization chamber 1 is provided with charging aperture 6, discharging opening 7, the charging aperture 6 of described carbonization chamber 1 and feeding screw 4
Outlet is connected, and the discharging opening 7 of described carbonization chamber 1 is connected with the import of spiral discharging device 5, and described carbonization chamber 1 is provided with many
Individual carbonization bed 8, described carbonization bed 8 is two or more, and described carbonization bed 8 is semi-circular structure, the semicircle of described carbonization bed 8
Circumference is connected inside carbonization chamber 1, and described carbonization bed 8 is crisscross arranged in carbonization chamber 1 from top to bottom, sets in described carbonization chamber 8
Having central rotating shaft 14, described central rotating shaft 14 to be located at the axle center of carbonization chamber 1, described central rotating shaft 14 is from carbonization chamber 1 top one
Directly extending to bottom carbonization chamber 1, described central rotating shaft 14 self can rotate around center, and described central rotating shaft 14 is welded with
Unload claw 9, described in unload claw 9 and be located at and be close to bed surface on carbonization bed 8, described in unload claw 9 and be provided with rake teeth 15, described carbonization chamber 1
Outside disc center, top is provided with motor 3, and the rotary shaft of described motor 3 is connected with central rotating shaft 14, and described carbonization chamber 1 has
Combustor 2, described combustor 2 is provided with heat sink 11 with carbonization chamber 1 junction, and described combustor 2 is provided with hot gas conduit 12, institute
Stating steam to lead 12 pipes and extend to bottom in carbonization chamber 1, described hot gas conduit 12 is provided with pore 13, and described carbonization chamber 1 upper end sets
There is retort gas outlet 10.
This utility model is so work: first light combustor 2, starts motor 3, feeding screw 4 and spiral discharging
Device 5, the wood material such as timber, shell is added continuously to carbonization chamber 1 by charging aperture 6 from feeding screw 4, passes through combustor
The 2 pairs of carbonization chambers 1 heat makes the raw material carbonization in carbonization chamber 1 produce Linesless charcoal, is rotarily driven by motor 3 and unload in carbonization chamber 1
Claw 9 rotates raw material from top carbonization bed 8 successively discharging, until the raw material entrance discharging opening 7 that carbonization is good, then from spiral
Discharger 5 outlet is discharged, and reaches continuous prodution, and the by-product flue gas produced in production is discharged to by retort gas outlet
In tail gas treatment device.
This utility model simple in construction, each parts combine linking closely, easy to operate, safety and stability, and efficiency is high, produces
Journey is totally-enclosed, will not produce environment and pollute.
Claims (1)
1. a multilamellar continuous carbonization furnace, it is characterised in that: it is by feeding screw (4), carbonization chamber (1), combustor (2) and spiral shell
Screwing out glassware (5) composition, described carbonization chamber (1) is provided with charging aperture (6), discharging opening (7), the charging aperture of described carbonization chamber (1)
(6) outlet with feeding screw (4) is connected, the discharging opening (7) of described carbonization chamber (1) and the import of spiral discharging device (5)
Being connected, described carbonization chamber (1) is provided with multiple carbonization bed (8), and described carbonization bed (8) is two or more, described charcoal
Changing bed (8) is semi-circular structure, and the semicircle circumference of described carbonization bed (8) is connected with carbonization chamber (1) inner side, and described carbonization bed (8) exists
Carbonization chamber is crisscross arranged in (1) from top to bottom, is provided with central rotating shaft (14), described central rotating shaft (14) in described carbonization chamber (1)
Being located at the axle center of carbonization chamber (1), described central rotating shaft (14) extends to carbonization chamber (1) bottom from carbonization chamber (1) top,
Described central rotating shaft (14) can around center self rotate, described central rotating shaft (14) is welded with and unloads claw (9), described in unload
Claw (9) is located at is close to the upper bed surface of carbonization bed (8), described in unload claw (9) and be provided with rake teeth (15), outside described carbonization chamber (1) top
Disc center, portion is provided with motor (3), and the rotary shaft of described motor (3) is connected with central rotating shaft (14), under described carbonization chamber (1)
Being provided with combustor (2), described combustor (2) and carbonization chamber (1) junction are provided with heat sink (11), and described combustor sets on (2)
Having hot gas conduit (12), described steam is led (12) pipe and is extended to carbonization chamber (1) interior bottom, and described hot gas conduit (12) is provided with gas
Hole (13), described carbonization chamber (1) upper end is provided with retort gas outlet (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620113107.1U CN205528594U (en) | 2016-02-04 | 2016-02-04 | Continuous retort of multilayer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620113107.1U CN205528594U (en) | 2016-02-04 | 2016-02-04 | Continuous retort of multilayer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205528594U true CN205528594U (en) | 2016-08-31 |
Family
ID=56776944
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620113107.1U Expired - Fee Related CN205528594U (en) | 2016-02-04 | 2016-02-04 | Continuous retort of multilayer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205528594U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105524633A (en) * | 2016-02-04 | 2016-04-27 | 辛集市远翔环保能源科技有限公司 | Multilayer continuous carbonization furnace |
| CN108624361A (en) * | 2017-03-19 | 2018-10-09 | 李佳纯 | Multiple-effect modular bio matter gasification furnace and combustion method |
| WO2018223320A1 (en) * | 2017-06-07 | 2018-12-13 | 东莞市裕证工业设备有限公司 | Continuous carbonization system |
| CN109957411A (en) * | 2019-04-01 | 2019-07-02 | 中国矿业大学 | A grid pyrolysis reactor and method suitable for rapid coal cracking |
| CN111732961A (en) * | 2020-06-28 | 2020-10-02 | 南京林业大学 | Continuous clean carbonization plant for straw |
-
2016
- 2016-02-04 CN CN201620113107.1U patent/CN205528594U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105524633A (en) * | 2016-02-04 | 2016-04-27 | 辛集市远翔环保能源科技有限公司 | Multilayer continuous carbonization furnace |
| CN108624361A (en) * | 2017-03-19 | 2018-10-09 | 李佳纯 | Multiple-effect modular bio matter gasification furnace and combustion method |
| WO2018223320A1 (en) * | 2017-06-07 | 2018-12-13 | 东莞市裕证工业设备有限公司 | Continuous carbonization system |
| CN109957411A (en) * | 2019-04-01 | 2019-07-02 | 中国矿业大学 | A grid pyrolysis reactor and method suitable for rapid coal cracking |
| CN111732961A (en) * | 2020-06-28 | 2020-10-02 | 南京林业大学 | Continuous clean carbonization plant for straw |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20200204 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |