CN207076464U - Equipment for continuously preparing charcoal - Google Patents

Equipment for continuously preparing charcoal Download PDF

Info

Publication number
CN207076464U
CN207076464U CN201720065030.XU CN201720065030U CN207076464U CN 207076464 U CN207076464 U CN 207076464U CN 201720065030 U CN201720065030 U CN 201720065030U CN 207076464 U CN207076464 U CN 207076464U
Authority
CN
China
Prior art keywords
heater
pyrolysis gas
annular body
continuously preparing
annular
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.)
Active
Application number
CN201720065030.XU
Other languages
Chinese (zh)
Inventor
金成国
王莉均
邵菊香
黄多辉
王藩侯
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.)
Yibin University
Original Assignee
Yibin University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Yibin University filed Critical Yibin University
Priority to CN201720065030.XU priority Critical patent/CN207076464U/en
Application granted granted Critical
Publication of CN207076464U publication Critical patent/CN207076464U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

The utility model discloses a kind of equipment for being used to continuously prepare charcoal, is related to agriculture and forestry organic waste material comprehensive utilization of resources field, including hollow annular body of heater, and the external side of annular furnace is provided with and communicated with material disengaging room;The annular body of heater and material disengaging interior are provided with material transmission track jointly, and the in-out end of material transmission track passes in and out room to outer parallel across material;Body feed tank is fixedly installed on the material transmission track.The utility model can continuous production, without flame-out, production efficiency is high, reduces charing energy consumption;In production process raw material be heated evenly, pyrolysis time it is controllable, the charcoal property of preparation is homogeneous.

Description

Equipment for continuously preparing charcoal
Technical field
Agriculture and forestry organic waste material comprehensive utilization of resources field is the utility model is related to, is used to continuously make in particular to one kind The equipment of standby charcoal.
Background technology
Charcoal be as biological material under conditions of complete or partial anoxic through pyrolysis charring caused by a kind of height Aromatization infusibility solid matter, surface porosity characteristic remarkable, there is larger specific surface area and higher surface energy.Biology Carbon surface polar functional group is less, and essential groups include carboxyl, phenolic hydroxyl group, carbonyl, lactone, pyranone, acid anhydrides etc., constitute life The good characterization of adsorption of thing charcoal.
China produces about 1,400,000,000 tons of agriculture and forestry discarded object per year, wherein the only stalk yield of the staple crop such as corn, rice, wheat Just reach 6.5 hundred million tons, but wherein crop-residue incorporation accounting is less than 20%, and the stock number being wasted is more than 50%.China crops Stalk is arbitrarily thrown aside, and the face source COD total amount maximum being likely to form every year is about 4,880,000 tons.
Consider from industrialization angle, it is that only the agriculture and forestry organic waste materials such as stalk are unified, efficiently process, it could realize Its maximum value.The agriculture and forestry discarded object of substantial amounts is exactly the ideal source of charcoal, and charcoal technology is just agreed with The efficient needs for utilizing stalk resource, reducing pollution of area source.
At present, charcoal is prepared as raw material using agriculture and forestry discarded object both at home and abroad and generally uses cracking process, i.e., in anaerobic or lacked The biomass such as agriculture and forestry discarded object is heated under conditions of oxygen makes its produce cracking reaction, so as to produce charcoal, bio oil and can Combustion gas.But these equipment are produced using batch more, it is impossible to the carbonization of biomass is carried out continuously, the problem of charing high energy consumption be present, And tail gas recycle is using there is also weak point.
Utility model content
The purpose of this utility model is to provide a kind of equipment for continuously preparing charcoal, to solve the above problems.
To realize the utility model purpose, the technical scheme used for:A kind of equipment for continuously preparing charcoal, bag Annular body of heater is included, toroidal cavity is provided with the furnace body wall of annular body of heater, and the external side of annular furnace is provided with and communicated with material disengaging Room;The annular body of heater is provided with material transmission track jointly with material disengaging interior, and the in-out end of material transmission track is worn It is outdoor to go out material disengaging;Body feed tank is fixedly installed on material transmission track.
Further, pyrolysis gas escape orifice is provided with the body feed tank.
Further, the body feed tank includes casing and case lid, and pyrolysis gas escape orifice is located on case lid, and pyrolysis gas escapes Hole is at least one.
Further, the bottom half is provided with engaging tooth, and engaging tooth is fastened on material transmission track;The thing Material disengaging outdoor is additionally provided with the drive device of driving material transmission track operation, and drive device is equipped with governing box.
Further, in the annular furnace body and material disengaging interior is provided with air inlet main pipeline, on admission line It is provided with volume damper;Multiple air inlet subtubes are provided with the air inlet main pipeline, and are passed in and out in annular furnace body with material Indoor air inlet main pipeline inlet end is connected with air blower.
Further, pyrolysis gas outlet is further opened with the annular body of heater, and pyrolysis gas outlet is connected by conveyance conduit Connect and be provided with clarifier.
Further, the pyrolysis gas outlet is multiple that multiple pyrolysis gas outlets are respectively positioned on the top surface of annular body of heater, and more Individual pyrolysis gas outlet is connected with clarifier jointly by conveyance conduit.
Further, the mode of heating of the annular body of heater is external heating mode, and external heating mode heats for flame.
Further, the mode of heating of the annular body of heater is interior mode of heating, and interior mode of heating is electrical heating.
Further, thermometer is additionally provided with the annular body of heater, and thermocouple, thermocouple are provided with annular furnace body It is connected with thermometer.
The beneficial effects of the utility model are,
1. the utility model can continuous production, without flame-out, production efficiency is high, reduces charing energy consumption;In production process Raw material is heated evenly, pyrolysis time is controllable, and the charcoal property of preparation is homogeneous.
2. the utility model makes the body feed tank on material transmission track with material transmission by the advance of material transmission track Track is driven together, realizes the fully-automatic production of charcoal, and does not need hand feed and discharging, and production is more convenient.
3. the utility model can be carried out pyrolysis gas by the way that caused pyrolysis gas in annular furnace body is sent in clarifier Effectively it is discharged into after purification in air, reduces the pollution of air, more energy-conserving and environment-protective;Simultaneously can be by evolution device by pyrolysis gas Wood tar, pyrolkigneous liquid and combustion gas isolate, the material for making to separate is reused, realize the energy secondary recovery profit With.The utility model improves resource utilization, has good in economic efficiency and free of contamination feature.
4. the utility model can use multiple heating mode, mode of heating is simple, and heat utilization rate is high, can be effectively to annular Temperature in body of heater is monitored, while the air quantity that indoor entrance is conveniently passed in and out to body of heater and material is adjusted.Pass through simultaneously Body feed tank waste heat after charing preheats to the agriculture and forestry organic waste material in the body feed tank that does not carbonize, improves energy utilization rate.
Brief description of the drawings
Fig. 1 is the structure chart provided by the utility model for being used to continuously prepare the equipment of charcoal;
Fig. 2 is the front view provided by the utility model for being used to continuously prepare the equipment of charcoal;
Fig. 3 is the annular furnace body section figure provided by the utility model for being used to continuously prepare in the equipment of charcoal;
Fig. 4 is the material disengaging room sectional view provided by the utility model being used to continuously prepare in the equipment of charcoal;
Mark and corresponding parts title in accompanying drawing:
1st, annular body of heater, 2, material disengaging room, 3, material transmission track, 4, body feed tank, 5, pyrolysis gas escape orifice, 6, case Lid, 7, casing, 8, engaging tooth, 9, air inlet main pipeline, 10, volume damper, 11, air inlet subtube, 12, air blower, 13, heat Vent one's spleen outlet, 14, conveyance conduit, 15, clarifier, 16, thermometer, 17, thermocouple, 18, drive device, 19, governing box, 20, Toroidal cavity.
Embodiment
The utility model is described in further detail below by specific examples of the implementation and with reference to accompanying drawing.
Fig. 1-Fig. 4 shows a kind of equipment for continuously preparing charcoal provided by the utility model, including annular furnace Body 1, toroidal cavity 20 is provided with the furnace body wall of annular body of heater 1, and the outside of annular body of heater 1 is provided with and connected with toroidal cavity 20 Material disengaging room 2, radial direction arrangement of the material disengaging room 2 along annular body of heater 1, annular body of heater 1 is passed in and out with material Room 2 collectively forms " racket " shape, and " face " of " racket " is annular body of heater, and " handle " is that material passes in and out room 2, facilitates material to enter Into annular body of heater 1, while facilitate the installation of material transmission track 3;The annular body of heater 1 with setting jointly in material disengaging room 2 Material transmission track 3 is equipped with, and the in-out end of material transmission track 3 is passed outside material disengaging room 2, and material transmission track 3 Middle part bends along toroidal cavity 20 and arranged, and the in-out end of material transmission track 3 passes in and out the axis direction parallel of room 2 along material Cloth.
Body feed tank 4 is fixedly installed on the material transmission track 3, material transmission track 3 is track car-type, i.e. material Case 4 is fixed on material transmission track 3, and material transmission track 3 is driven by drive device 18, passes through material transmission track 3 Advance, the body feed tank 4 on material transmission track 3 is driven with material transmission track 3.It is used to place farming in body feed tank 4 Thing stalk, bamboo and wood processing waste, branch, leaf, shell, pericarp, vinasse, bagasse, rice hulls, cotton seed hulls and discarded edible Agriculture and forestry organic waste material after the crushing such as bacterium culture medium;Pyrolysis gas escape orifice 5, the side of pyrolysis gas escape orifice 5 are provided with the body feed tank 4 Just the pyrolysis gas in body feed tank 4 is distributed to annular body of heater 1 during charing, improves the charing effect of agriculture and forestry organic waste material Rate, make the charing of agriculture and forestry organic waste material in body feed tank 4 more thorough.
The body feed tank 4 includes casing 7 and case lid 6, convenient that agriculture and forestry organic waste material is stored in body feed tank, while conveniently will Charcoal after charing takes out, and pyrolysis gas escape orifice is located on case lid 6, and pyrolysis gas escape orifice 5 is at least one, multiple pyrolysis gas Escape orifice 5 is evenly distributed on case lid 6, the pyrolysis gas in body feed tank 4 is quickly discharged.
The bottom of casing 7 is provided with engaging tooth 8, and engaging tooth 8 is fastened on material transmission track 3, can effectively be avoided Body feed tank 4 departs from material transmission track 3 in moving process, makes the movement of body feed tank 4 more steady.The material passes in and out room 2 The outer drive device 18 for being additionally provided with the track operation of driving material transmission, and drive device 18 is equipped with governing box 19, governing box 19 can regulate and control to the rotating speed of drive device 18, so as to the speed of service of Effective Regulation material transmission track 3, so as to control The translational speed of body feed tank 4, and then when playing in control material case 4 pyrolysis time of agriculture and forestry organic waste material and regulation charcoal unit Between yield effect.
Air inlet main pipeline 9 is provided with the annular body of heater 1 and in material disengaging room 2, is provided with admission line 9 Volume damper 10;It is provided with multiple air inlet subtubes 11 on the air inlet main pipeline 9, multiple air inlet subtubes 11 are along air inlet The axis direction uniform intervals arrangement of main pipeline 9, enable air to uniformly enter in annular body of heater 1 and material disengaging room 2, wind Adjustable valve 10 can adjust speed and the capacity that air is entered in annular body of heater 1 and material disengaging room 2, make in annular body of heater 1 Part anoxic or complete anoxic, and the inlet end of air inlet main pipeline 9 in annular body of heater 1 and in material disengaging room 2 is connected with Air blower 12, annular body of heater 1 and material are admitted air into by the effect of air blower 12 and pass in and out the air flow of room 2 faster.
Pyrolysis gas outlet 13 is further opened with the annular body of heater 1, and pyrolysis gas outlet 13 is connected by conveyance conduit 14 Clarifier 15 is provided with, caused gas in annular body of heater 1 effectively can be transported to by pyrolysis gas outlet 13 by conveyance conduit 14 Purified in clarifier 15, wood tar caused by purification, pyrolkigneous liquid and combustion gas is recycled and is utilized, while after purification Gas can be directly discharged in air, can effectively be prevented the pollution of air, be reasonably utilized resource.The pyrolysis gas goes out Mouthfuls 13 be multiple, and multiple pyrolysis gas outlets 13 are respectively positioned on the top surface of annular body of heater 1, and multiple pyrolysis gas outlets 13 are along annular body of heater 1 Circumferential uniformly arrangement, makes the spacing between two neighboring pyrolysis gas outlet 13 equal, and multiple pyrolysis gas outlets 13 pass through conveying Pipeline 14 is connected with clarifier 15 jointly, the pyrolysis gas in annular body of heater 1 is uniformly discharged.
The mode of heating of the annular body of heater 1 is external heating mode, and external heating mode heats for flame, and flame heats Raw material can be coal dust, heavy oil or gas, and flame is located at the lower section of annular body of heater.The mode of heating of the annular body of heater 1 Can also be interior mode of heating, and interior mode of heating is electrical heating, it is electrically heated using electric furnace heating wire, Elema or Si-Mo rod conduct Heater element, and electric heating element is arranged on the inner bottom surface of annular body of heater 1.
Thermometer 16 is additionally provided with the annular body of heater 1, and thermocouple 17 is provided with annular body of heater 1, thermocouple 17 It is connected with thermometer 16, the temperature in annular body of heater 1 can be quickly understood by thermometer 16, facilitate agricultural in body feed tank 4 to give up The charing of gurry.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, for this For the technical staff in field, the utility model can have various modifications and variations.It is all in the spirit and principles of the utility model Within, any modification, equivalent substitution and improvements made etc., it should be included within the scope of protection of the utility model.

Claims (10)

1. the equipment for continuously preparing charcoal, it is characterised in that:Including annular body of heater, set in the furnace body wall of annular body of heater There is toroidal cavity, and the external side of annular furnace is provided with the material disengaging room connected with toroidal cavity;The annular body of heater and material Disengaging interior is provided with material transmission track jointly, and the in-out end of material transmission track passes material disengaging outdoor;The thing Body feed tank is fixedly installed on material transmission track.
2. the equipment according to claim 1 for continuously preparing charcoal, it is characterised in that set on the body feed tank There is pyrolysis gas escape orifice.
3. the equipment according to claim 2 for continuously preparing charcoal, it is characterised in that the body feed tank includes case Body and case lid, pyrolysis gas escape orifice is located on case lid, and pyrolysis gas escape orifice is at least one.
4. the equipment according to claim 3 for continuously preparing charcoal, it is characterised in that the bottom half is set There is engaging tooth, and engaging tooth is fastened on material transmission track;The material disengaging outdoor is additionally provided with driving material transmission rail The drive device of road operation, and drive device is equipped with governing box.
5. the equipment according to claim 1 for continuously preparing charcoal, it is characterised in that in the annular furnace body and Material disengaging interior is provided with air inlet main pipeline, and volume damper is provided with admission line;On the air inlet main pipeline Multiple air inlet subtubes are provided with, and the air inlet main pipeline inlet end of in annular furnace body and material disengaging interior is connected with drum Blower fan.
6. the equipment according to claim 1 for continuously preparing charcoal, it is characterised in that on the annular body of heater also Pyrolysis gas outlet is offered, and pyrolysis gas outlet is connected with clarifier by conveyance conduit.
7. the equipment according to claim 6 for continuously preparing charcoal, it is characterised in that the pyrolysis gas outlet is Multiple, multiple pyrolysis gas outlets are respectively positioned on the top surface of annular body of heater, and multiple pyrolysis gas outlets by conveyance conduit jointly with only Change device connection.
8. the equipment according to claim 1 for continuously preparing charcoal, it is characterised in that the annular body of heater adds Hot mode is external heating mode, and external heating mode heats for flame.
9. the equipment according to claim 1 for continuously preparing charcoal, it is characterised in that the annular body of heater adds Hot mode is interior mode of heating, and interior mode of heating is electrical heating.
10. the equipment according to claim 1 for continuously preparing charcoal, it is characterised in that on the annular body of heater Thermometer is additionally provided with, and thermocouple is provided with annular furnace body, thermocouple is connected with thermometer.
CN201720065030.XU 2017-01-19 2017-01-19 Equipment for continuously preparing charcoal Active CN207076464U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720065030.XU CN207076464U (en) 2017-01-19 2017-01-19 Equipment for continuously preparing charcoal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720065030.XU CN207076464U (en) 2017-01-19 2017-01-19 Equipment for continuously preparing charcoal

Publications (1)

Publication Number Publication Date
CN207076464U true CN207076464U (en) 2018-03-09

Family

ID=61435491

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720065030.XU Active CN207076464U (en) 2017-01-19 2017-01-19 Equipment for continuously preparing charcoal

Country Status (1)

Country Link
CN (1) CN207076464U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106675599A (en) * 2017-01-19 2017-05-17 宜宾学院 Device and method for continuously preparing charcoal

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106675599A (en) * 2017-01-19 2017-05-17 宜宾学院 Device and method for continuously preparing charcoal
CN106675599B (en) * 2017-01-19 2019-11-26 宜宾学院 For continuously preparing the device and method of charcoal

Similar Documents

Publication Publication Date Title
CN202530040U (en) Continuous biomass dry-distillation carbonization apparatus
CN102701814A (en) Roller organic fertilizer fermentation machine and fermentation process
CN103980921B (en) Industrial production method of fuel oil by thermal cracking of biomass
CN201896159U (en) Biomass fuel gas and biomass charcoal preparation system with accurate control
CN104861996B (en) A kind of technique for biomass pyrolysis carbon gas oil polygenerations systeme
CN102643657A (en) Continuous biomass carbonization process
CN102559220A (en) Precisely controlled biomass gas and biomass carbon preparation system
CN101595951B (en) Drying device with combination of wheat bran on-line microwave and air current and method
CN106281397B (en) Field biomass through pyrolysis oil refining apparatus based on solar energy heating and from heat supply
CN106675599B (en) For continuously preparing the device and method of charcoal
CN104312602A (en) Continuous carbonization furnace for waste wood chips
CN207076464U (en) Equipment for continuously preparing charcoal
CN104861997A (en) Biomass pyrolysis reaction system and pyrolysis method
CN104861993A (en) Tower-type continuous carbonization furnace for biomass
CN109456781A (en) A kind of integrated apparatus and method of charcoal/oil/gas coproduction
CN110006033B (en) Biomass burner and pig manure low-cost treatment system
CN210035473U (en) Biomass burner and low-cost pig manure treatment system
CN204689938U (en) Tower biological matter continuous carbonization furnace
CN104446733A (en) Environment-friendly energy-saving bio-organic fertilizer fermentation equipment
CN110257093A (en) The control method of carbonization system in a kind of hot charcoal co-generation system of biomass external heating
CN106631222A (en) Composite heating fast fermentation device of organic fertilizer
CN104342174B (en) A kind of shell-and-tube classification biomass carbonizing furnace
CN210030576U (en) Biomass pyrolysis reaction device and pyrolysis system
CN202968479U (en) Continuous biomass carbonizing apparatus
CN204125423U (en) A kind of waste wood continuous carbonization furnace

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant