CN205528594U - Continuous retort of multilayer - Google Patents

Continuous retort of multilayer Download PDF

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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
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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
Application number
CN201620113107.1U
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Chinese (zh)
Inventor
吴海霞
郝建设
郝强柱
郝小柱
黄康
郝英合
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xinji Yuan Xiang Green Energy Technology Co Ltd
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Xinji Yuan Xiang Green Energy Technology Co Ltd
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Priority to CN201620113107.1U priority Critical patent/CN205528594U/en
Application granted granted Critical
Publication of CN205528594U publication Critical patent/CN205528594U/en
Expired - Fee Related legal-status Critical Current
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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

A kind of multilamellar continuous carbonization furnace
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).
CN201620113107.1U 2016-02-04 2016-02-04 Continuous retort of multilayer Expired - Fee Related CN205528594U (en)

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

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Cited By (5)

* Cited by examiner, † Cited by third party
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 kind of the grid pyrolysis reactor and method of suitable coals rapid cleavage
CN111732961A (en) * 2020-06-28 2020-10-02 南京林业大学 Continuous cleaning and carbonizing device for straws

Cited By (5)

* Cited by examiner, † Cited by third party
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 kind of the grid pyrolysis reactor and method of suitable coals rapid cleavage
CN111732961A (en) * 2020-06-28 2020-10-02 南京林业大学 Continuous cleaning and carbonizing device for straws

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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