CN104609418B - Biological material carbonization-activation integral device - Google Patents

Biological material carbonization-activation integral device Download PDF

Info

Publication number
CN104609418B
CN104609418B CN201410807455.4A CN201410807455A CN104609418B CN 104609418 B CN104609418 B CN 104609418B CN 201410807455 A CN201410807455 A CN 201410807455A CN 104609418 B CN104609418 B CN 104609418B
Authority
CN
China
Prior art keywords
activation
steam
furnace
retort
auger
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
CN201410807455.4A
Other languages
Chinese (zh)
Other versions
CN104609418A (en
Inventor
杨生茂
陈忠良
钟哲科
吕豪豪
刘玉学
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.)
Zhejiang Academy of Agricultural Sciences
Original Assignee
Zhejiang Academy of Agricultural Sciences
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 Zhejiang Academy of Agricultural Sciences filed Critical Zhejiang Academy of Agricultural Sciences
Priority to CN201410807455.4A priority Critical patent/CN104609418B/en
Publication of CN104609418A publication Critical patent/CN104609418A/en
Application granted granted Critical
Publication of CN104609418B publication Critical patent/CN104609418B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Carbon And Carbon Compounds (AREA)

Abstract

The present invention relates to a kind of biological material carbonization-activation integral device, the problem that solves that existing carbonization-activation unit efficiency is low, and activation process control is difficult, energy consumption is high.The present apparatus includes vertical retort and lateral activation furnace, vertical charing cylinder is equipped in retort, it is horizontally through activation furnace and is equipped with activation auger, the lower end for carbonizing cylinder is connected with the beginning of activation auger, be additionally provided on retort be connected to activation auger and to activation auger internal spray steam steam jet, steam jet passes through the furnace wall of retort, and the activation furnace and retort are equipped with air inlet and exhaust outlet, and the air inlet of activation furnace and retort is connected with combustion furnace.Steam activation of the present invention will not have an impact charing;Activation process sprays steam using steam jet, collaboration activation auger is controlled, steam consumption can effectively be controlled, and fully ensure that contact of the steam with layer of charcoal, guarantee activation effect, the heat for reducing steam consumption, and can use activation furnace itself, steam in steam jet is heated, the additional energy of heating steam is reduced.

Description

Biological material carbonization-activation integral device
Technical field
The present invention relates to a kind of biological material processing unit (plant), in particular to a kind of biological material carbonization-activation integral dress It sets.
Background technique
Biological material charcoal processing activation, can use traditional steam activation process.It traditional method charcoal processing and activated Journey be it is separated, centre needs manually to shift, large labor intensity, and carbonization-activation process carries out in batches, single batch processing Amount is big, and for steam activation process, the amount activated is needed to will lead to steam greatly for single and the difficulty of charcoal comprehensive engagement increases, processing Low efficiency.Furthermore it needs first to heat acquisition high-temperature steam in activation process, then pass in activation furnace, heat the energy consumption of steam Greatly.
CN103395782A patent disclosed in Chinese patent on November 20th, 2013, entitled removable carbonization-activation side Method.This method uses vertical conveying, from it is upper it is big under be successively arranged feeding warehouse, char zone, region of activation, discharge baffle, then pass through Auger discharging below discharge baffle is set.The first, above-mentioned carbonization-activation mode char zone and region of activation there is no carry out every From, the vapor volume control difficulty of region of activation is big, and quantity of steam crosses conference and spreads to char zone, carbonization process is impacted, and steam Vapour amount is too small, is unable to satisfy the demand activated completely;The second, above-mentioned carbonization-activation mode material accumulation consolidation, for charing Area, carbonization process are mainly the transmitting of heat, are influenced less on charred effect, and for region of activation, the material meeting of consolidation accumulation Cause steam that can not influence activation effect with the abundant comprehensive engagement of material.
Summary of the invention
It is an object of the invention to low for existing carbonization-activation unit efficiency, activation process control is difficult, energy consumption is high is asked Topic, provides a kind of biological material carbonization-activation integral device.
The technical solution adopted by the present invention to solve the technical problems is: a kind of biological material carbonization-activation integral dress It sets, including vertical retort and lateral activation furnace, is equipped with vertical charing cylinder in retort, is horizontally through activation furnace and is equipped with Auger is activated, the lower end of cylinder is carbonized and is connected with the beginning of activation auger, is additionally provided with to be connected on activation furnace and activates auger and to work Change the steam jet of auger internal spray steam, steam jet passes through the furnace wall of activation furnace, and the activation furnace and retort are all provided with There are an air inlet and exhaust outlet, the air inlet of activation furnace and retort is connected with combustion furnace.Retort and activation furnace separation, guarantee to live The steam for changing furnace will not have an impact the material not carbonized, and activation auger can pass through the adjusting of revolving speed, a controllable charing Cylinder blanking velocity, the two controllable thickness for activating layer of charcoal in augers, guarantees the comprehensive engagement of steam and charcoal, and in every section auger Charcoal amount it is controllable, the steam consumption of corresponding auger one section of every conveying can be controlled quantitatively, energy saving.Setting folder on the outside of retort Layer filling thermal insulation material, activation furnace can be built into using refractory brick.Retort, activation furnace side wall can be set and prevent internal pressure The excessively high venting of power.Detection mouth, monitoring temperature is arranged along each position of airflow direction in retort, activation furnace.
Preferably, the steam jet is pulse spray, during activation auger rotates one week, steam jet is at equal intervals Injection 1~5 time.Steam jet is sprayed using pulsed, can control steam consumption by the ratio between injecting times and auger revolving speed, can Control property is high.In addition, activation in-furnace temperature is up to 500 DEG C or more, steam jet under high temperature environment may be used using metal tubes such as copper pipes To carry out reheating to the steam in pipe, the temperature requirement of steam gas supply is reduced in this way, saves the cost of heating steam.It adopts With pulse spray, moreover it is possible to guarantee that the temperature of pulse spacing steam jet is stablized.
Preferably, steam jet connection activation after activation furnace inner part is using helix tube coiling several weeks twists Dragon.Increase stroke of the steam jet in activation furnace, when each the amount of injection of steam jet is less, can use in activation furnace originally The temperature of body heats the steam in pipe, it might even be possible to replace steam using hot water in steam jet import, hot water is made to exist Vaporization, which is brought rapidly up, in steam jet coiling process forms steam, additional energy needed for further reduced heating steam.
Preferably, the steam jet is equipped with several along activation auger conveying direction.It can choose a little or more Point injection steam, guarantees activation effect.
Preferably, the rear end of the activation furnace is successively arranged cooling water tank and discharging bin, activation auger sequentially passes through work Go out charcoal in discharging bin location after change furnace, cooling water tank.
Preferably, it is described charing cylinder outside be retort hot air chamber, charing furnace upper end be equipped with smoke chamber, smoke chamber and The isolation of retort hot air chamber, the top for carbonizing cylinder are equipped with lower hopper, and lower hopper bottom end is taper, in lower hopper bottom end and charing cylinder There is annulus gap, annulus gap connection charing cylinder and smoke chamber, smoke chamber is by returning smoke pipe connection burning between the inner wall of top The air inlet of furnace returns the air-introduced machine being additionally provided on smoke pipe as air flow power.In material carbonization process, the cracking gas of generation passes through Annulus gap, smoke chamber, time smoke pipe enter combustion furnace burn-up, flatulence in charing cylinder are not only prevented, but also reduce discharge, on time smoke pipe Condenser can be installed, the substances such as condensable tar are separated and recovered.
Preferably, being equipped with discharging bin below the end of the activation auger, cigarette is connected by smoke collection pipe at the top of discharging bin Gas chamber.The cracking gas finally to discharge is collected into smoke chamber processing also by smoke collection pipe.
Preferably, the space in retort, outside charing cylinder is separated using several pieces of horizontal baffles in the retort At upper and lower multilayer, horizontal baffle has venthole up and down, the air inlet of retort, the ventilation of neighbouring horizontal baffle Hole, retort exhaust outlet left and right is arranged alternately from top to bottom, form the snakelike air flue turned back.The snakelike air flue turned back increases The stroke of hot wind improves heat transfer effect.It is possible to further open up the connecting leg at left and right sides of connection on charing cylinder, make hot wind It can enter connecting leg to heat charing cylinder internal layer.
It is more using several pieces of vertical clapboards the space in activation furnace, outside activation auger to be separated into left and right in the activation furnace Room, vertical clapboard have the venthole of left and right perforation, the air inlet of activation furnace, the venthole of adjacent upright partition, activation furnace Exhaust outlet is arranged alternatively up and down along charing auger conveying direction, forms the air flue above and below snakelike.
Preferably, the exhaust outlet of the activation furnace is connected to the middle section of retort by muffler, and pass through retort Exhaust outlet is unified to be vented.Activation furnace material initial temperature is relatively high, therefore small by the hot wind heat loss of activation furnace, can pass through Muffler enters retort utilization, and uses same exhaust, is convenient for vent gas treatment.
For the present invention using vertical charing and horizontal activation combination, one of connecting completes biological material charing, activation Process, charing and activation process isolation again, have an impact steam activation will not to charing in series connection;Activation process is using steaming Vapour jet pipe sprays steam, and collaboration activation auger is controlled, and can effectively control steam consumption, and fully ensure that steam and layer of charcoal Contact, guarantee activation effect, the heat for reducing steam consumption, and can use activation furnace itself, in steam jet Steam is heated, and the additional energy of heating steam is reduced.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the invention.
Fig. 2 is structural schematic diagram at A in Fig. 1 of the present invention.
In figure: 1, feed inlet, 2, condenser, 3, time smoke pipe, 4, elevator, 5, lower hopper, 6, horizontal baffle, 7, retort Air inlet, 8, smoke chamber, 9, retort exhaust outlet, 10, retort, 11, charing cylinder, 12, muffler, 13, smoke collection pipe, 14, steaming Vapour jet pipe, 15, detection mouth, 16, connecting leg, 17, overflow pipe, 18, cooling water tank, 19, discharge outlet, 20, water inlet, 21, discharging bin, 22, vertical clapboard, 23, activation auger, 24, activation furnace, 25, activation furnace air inlet, 26, lower hopper tapered bottom end, 27, annular gas Gap.
Specific embodiment
Below by specific embodiment and in conjunction with attached drawing, the present invention is further described.
Embodiment: a kind of biological material carbonization-activation integral device, as shown in Figure 1, 2.The present apparatus includes vertical charcoal Change furnace 10 and horizontal activation furnace 24, vertical charing cylinder 11 is equipped in retort, activation auger 23 is horizontally through activation furnace two End, the bottom end for carbonizing cylinder are connected with the head end of activation auger.The outside for carbonizing cylinder is the gas chamber of retort, retort gas chamber it is outer Side is equipped with heat preservation sandwich layer, fills thermal insulation material in interlayer.Activation furnace is built into using refractory brick, is activation furnace on the outside of activation auger Gas chamber.Retort, activation furnace use combustion furnace hot wind supply.
As shown in Figure 1, retort air inlet 7 is located on the left of retort lower end, retort exhaust outlet 9 is located at charing furnace upper end Right side, retort 10 is interior, charing cylinder 11 is separated into upper, middle and lower-ranking using upper and lower two pieces of horizontal baffles 6 outside.The level of downside Partition opens up the venthole of connection or more on the right side;The horizontal baffle of upside opens up the venthole of connection or more by left side;In charcoal Change and is formed in furnace from top to bottom, the snakelike air flue turned back.Meanwhile it carbonizing cylinder and being respectively equipped in upper, middle and lower-ranking position and laterally being connected The connecting leg 16 of logical charing cylinder barrel.The middle layer side of retort is equipped with venting, and middle layer and upper sides are respectively equipped with detection mouth.
As shown in Figure 1, activation furnace air inlet 25 is located at activation furnace left end lower part, activation furnace exhaust outlet is located at activation furnace right end Top, activation furnace 24 is interior, activation auger 23 is separated into three Room of left, center, right using the two pieces of vertical clapboards 22 in left and right outside.Left side it is vertical Partition opens up the venthole of connection left and right by top;The vertical clapboard on right side opens up the venthole of connection left and right on the lower;In work Change and is formed in furnace from left to right, snakelike upper and lower air flue.Activation furnace exhaust outlet is connected to the middle layer of retort by muffler 12, Then it is vented by the way that retort exhaust pipe 9 is unified.The left room of activation furnace 24 is set there are two steam jet 14, and middle room is equipped with a steaming Vapour jet pipe 14, steam jet pass through activation furnace furnace wall and are connected to activation auger, and steam jet is the pulse spray of adjustable frequency.This Steam jet 14 uses straight tube in activation furnace in example, can also be by steam jet if to reduce steam initially for stripping temperature 14 change spiral coil into activation furnace inner part.Detection mouth 15 is respectively equipped in left room, the middle room of activation furnace.In activation furnace Room, right ventricle are respectively equipped with venting.
Smoke chamber 8, smoke chamber and the isolation of retort gas chamber are equipped with above retort 10.The top for carbonizing cylinder 11 is equipped with blanking Bucket 5, lower hopper are connect by elevator 4 with the feed inlet 1 of bottom.As shown in Fig. 2, lower hopper is the taper bucket, lower hopper taper There is annulus gap 27, annulus gap connection charing cylinder 11 and smoke chamber 8, flue gas between bottom end 26 and charing 11 top inner wall of cylinder The left side of room is connected to condenser 2 by returning smoke pipe 3, and tar collecting vessel is arranged below condenser, and it is logical to go out gas side above condenser Cross the inlet side that blower is connected into combustion furnace.
The right side of activation furnace is equipped with cooling water tank 18, and cooling water tank bottom left sets water inlet 20, top right side setting row The mouth of a river 19, top left side are additionally provided with overflow pipe 17.After activation auger 23 sequentially passes through activation furnace, cooling water tank, auger is activated Discharging bin 21 is set below end, and the top of discharging bin 21 is equipped with smoke collection pipe 13, and the smoke collection pipe other end is connected to smoke chamber.
Biological material is from throat-fed, moves down completion charing into charing cylinder, and in charing cylinder, carbonizes cylinder bottom For the charing material at end by activation auger horizontal feed, the revolving speed by activating auger controllably carbonizes the speed that material declines in cylinder And the carbon layer in activation auger.According to activation auger rotational speed regulation steam jet pulse frequency, guarantee steam with The comprehensive contact of layer of charcoal guarantees activation efficiency and effect, and reduces steam consumption.

Claims (8)

1. a kind of biological material carbonization-activation integral device, it is characterised in that: including vertical retort and lateral activation Furnace, retort is interior to be equipped with vertical charing cylinder, is horizontally through activation furnace and is equipped with activation auger, carbonizes the lower end of cylinder and activates auger Beginning be connected, be additionally provided on activation furnace be connected to activation auger and to activation auger internal spray steam steam jet, steam Vapour jet pipe passes through the furnace wall of activation furnace, and the activation furnace and retort are equipped with air inlet and exhaust outlet, activation furnace and retort Air inlet be connected with combustion furnace, the steam jet connects activation after activation furnace inner part is using helix tube coiling several weeks Auger increases stroke of the steam jet in activation furnace, when each the amount of injection of steam jet is less, can also reach and utilize work The heat of itself, heats the steam in pipe in change furnace, it might even be possible to steam is replaced using hot water in steam jet import, Making hot water, effectively heating vaporization forms steam rapidly in steam jet coiling process, further reduced needed for heating steam Additional energy, the activation furnace is interior to be separated into left and right for the space in activation furnace, outside activation auger using several pieces of vertical clapboards Multicell, vertical clapboard have the venthole of left and right perforation, the air inlet of activation furnace, the venthole of adjacent upright partition, activation furnace Exhaust outlet along charing auger conveying direction be staggered alternatively up and down, formed it is snakelike above and below air flue.
2. biological material carbonization-activation integral device according to claim 1, it is characterised in that: the steam jet is Pulse spray, during activation auger rotates one week, steam jet sprays 1~5 time at equal intervals.
3. biological material carbonization-activation integral device according to claim 1 or 2, it is characterised in that: the steam spray Pipe is equipped with several along activation auger conveying direction.
4. biological material carbonization-activation integral device according to claim 1 or 2, it is characterised in that: the activation furnace Rear end be successively arranged cooling water tank and discharging bin, activation auger sequentially passes through after activation furnace, cooling water tank in discharging bin location Charcoal out.
5. biological material carbonization-activation integral device according to claim 1 or 2, it is characterised in that: the charing cylinder Outside be retort hot air chamber, charing furnace upper end be equipped with smoke chamber, smoke chamber and retort hot air chamber isolation, carbonize the upper of cylinder Side is equipped with lower hopper, and lower hopper bottom end is bullet, has annulus gap between lower hopper bottom end and charing cylinder top inner wall, Annulus gap connection charing cylinder and smoke chamber, smoke chamber connect the air inlet of combustion furnace by returning smoke pipe, return on smoke pipe and are additionally provided with Air-introduced machine as air flow power.
6. biological material carbonization-activation integral device according to claim 5, it is characterised in that: the activation auger Discharging bin is equipped with below end, discharging bin top connects smoke chamber by smoke collection pipe.
7. biological material carbonization-activation integral device according to claim 1 or 2, it is characterised in that: the retort Interior that the space in retort, outside charing cylinder is separated into multilayer up and down using several pieces of horizontal baffles, horizontal baffle has up and down The venthole of perforation, the air inlet of retort, neighbouring horizontal baffle venthole, retort exhaust outlet from top to bottom left and right It is arranged alternately, forms the snakelike air flue turned back.
8. biological material carbonization-activation integral device according to claim 1, it is characterised in that: the row of the activation furnace Port is connected to the middle section of retort by muffler, and is vented by the way that retort exhaust outlet is unified.
CN201410807455.4A 2014-12-23 2014-12-23 Biological material carbonization-activation integral device Active CN104609418B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410807455.4A CN104609418B (en) 2014-12-23 2014-12-23 Biological material carbonization-activation integral device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410807455.4A CN104609418B (en) 2014-12-23 2014-12-23 Biological material carbonization-activation integral device

Publications (2)

Publication Number Publication Date
CN104609418A CN104609418A (en) 2015-05-13
CN104609418B true CN104609418B (en) 2019-05-24

Family

ID=53144119

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410807455.4A Active CN104609418B (en) 2014-12-23 2014-12-23 Biological material carbonization-activation integral device

Country Status (1)

Country Link
CN (1) CN104609418B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107344718B (en) * 2017-06-29 2023-07-25 安泰环境工程技术有限公司 Continuous high-temperature carbonization and activation integrated device and method
CN107500288A (en) * 2017-09-27 2017-12-22 黎城蓝天燃气开发有限公司 A kind of production method of activated coke
CN109280557B (en) * 2018-09-25 2020-12-15 福建省闽安机械制造有限公司 Heat exchange method for carbonization furnace
CN111675218A (en) * 2020-06-18 2020-09-18 石家庄启泰炭业科技有限公司 Active carbon production device
CN112174142B (en) * 2020-10-28 2022-02-01 闽江学院 Biomass material carbonization and activation integrated device
CN112250071A (en) * 2020-11-16 2021-01-22 山东科能环保科技有限公司 Carbonization and activation dual-function consubstantial furnace for producing active carbon and steam
CN113479883B (en) * 2021-08-05 2024-01-09 江苏森森炭业科技有限公司 Automatic charcoal equipment of receiving of active carbon semi-manufactured goods
CN115140738B (en) * 2022-06-17 2023-12-15 四川惊雷科技股份有限公司 Circulation energy-saving carbonization and activation integrated machine
CN116792773B (en) * 2023-08-28 2023-10-27 内蒙古蓝色火宴科技环保股份公司 Biomass charcoal burning waste gas treatment equipment

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101214956A (en) * 2008-01-15 2008-07-09 章水根 Method and device for producing inside and outside thermal combined two-stage continuous activated carbon
JP5185056B2 (en) * 2008-10-16 2013-04-17 ヤンマー株式会社 Engine speed control device
CN204369574U (en) * 2014-12-23 2015-06-03 浙江省农业科学院 Biological material carbonization-activation integral device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05185056A (en) * 1992-01-09 1993-07-27 Toshiba Mach Co Ltd Treatment of composite plastic waste material and equipment therefor
CN202829593U (en) * 2012-09-06 2013-03-27 重庆亿豪活性炭制造厂 Activated carbon producing device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101214956A (en) * 2008-01-15 2008-07-09 章水根 Method and device for producing inside and outside thermal combined two-stage continuous activated carbon
JP5185056B2 (en) * 2008-10-16 2013-04-17 ヤンマー株式会社 Engine speed control device
CN204369574U (en) * 2014-12-23 2015-06-03 浙江省农业科学院 Biological material carbonization-activation integral device

Also Published As

Publication number Publication date
CN104609418A (en) 2015-05-13

Similar Documents

Publication Publication Date Title
CN104609418B (en) Biological material carbonization-activation integral device
CN105062521B (en) A kind of swinging continuous pyrolysis stalk coke oven
CN106430191A (en) Active carbon activation furnace and active carbon production method
CN204237743U (en) A kind of New type coal gas retort
CN107990741A (en) A kind of retort UTILIZATION OF VESIDUAL HEAT IN temperature regulating device and its temperature control method
CN109761237A (en) A kind of efficient inside and outside dual-heating mode revolution retort
CN109468139A (en) A kind of biomass graded pyrolysis and combustion device
CN107384455A (en) Downdraft radiant tube biomass pyrolytic charcoal processing stove
CN110357101A (en) A kind of cleaning prepares the vertical integral type internal fired furnace of active carbon
CN109161389B (en) Self-weight spiral progressive biomass efficient energy-saving pyrolysis system
CN204939394U (en) Rotary type continuous pyrolysis stalk coke oven
CN204369574U (en) Biological material carbonization-activation integral device
CN209081807U (en) A kind of self weight spiral progressive biomass high-efficiency energy-saving pyrolysis system
CN105258500B (en) The hot air circulating system and its proportional controlling means of automatic fuel gas continuous tunnel furnace
CN109022001B (en) Dead weight spiral gradually-advancing type biomass high-efficiency energy-saving pyrolysis furnace device
CN106701128A (en) Regenerative pyrolytic reaction system and method for powdered coal
CN101157863B (en) Highly effective environment protection energy-saving retort
CN210528482U (en) Vertical integrated internal combustion furnace for cleanly preparing activated carbon
CN101638230A (en) Kiln for producing active carbon
CN108504369A (en) A kind of biomass carbonated destructive distillation purification recovery device and method
CN210528483U (en) Horizontal integrated internal combustion furnace for cleanly preparing activated carbon
CN209685691U (en) A kind of continuous biomass apparatus for thermal cleavage
CN109266370B (en) Progressive biomass high-efficiency energy-saving pyrolysis furnace
CN203194404U (en) Foot baking device
CN208748006U (en) A kind of biomass pyrolytic charing furnace

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant