CN205473575U - Continuous retort of bamboo material - Google Patents
Continuous retort of bamboo material Download PDFInfo
- Publication number
- CN205473575U CN205473575U CN201620010530.9U CN201620010530U CN205473575U CN 205473575 U CN205473575 U CN 205473575U CN 201620010530 U CN201620010530 U CN 201620010530U CN 205473575 U CN205473575 U CN 205473575U
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- China
- Prior art keywords
- coal gas
- pipeline
- platform
- endless tube
- regenerative heat
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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 utility model discloses a continuous retort of bamboo material, including heating system, carbomorphism system and air water recovery system. Heating system links to each other through the furnace body of hot -blast ring canal with the carbomorphism system, and the coal gas storage cabinet that the water ring formula adds press and air water recovery system links to each other, and the furnace body of carbomorphism system is collected the ring canal through the coal gas that lies in the furnace roof platform and is linked to each other with air water recovery system, the coal gas storage cabinet that pipeline and air water recovery system are passed through to the cooling chamber of carbomorphism system links to each other, and air water recovery system is located the right -hand member of bottom plate. This application dry distillation is fast, charcoal formation rate high, heat utilization efficiency is high, the height is rateed to comprehensive use of resources, and the in -process does not have the discarded object production simultaneously, can not cause the pollution to the environment.
Description
Technical field
This utility model relates to a kind of bamboo material continuous carbonization furnace, particularly a kind of bamboo material quantity-produced retort.
Background technology
China is Linesless charcoal big producing country, and annual char yield is up to ten million ton, along with the fast development of national economy, Linesless charcoal
Demand rise the most year by year.Owing to the main raw material(s) of Linesless charcoal is natural timber, the most also increase the need to natural timber
Ask.China's bamboo resource enriches, and produces the products such as substantial amounts of bamboo bits during bamboo utilizes, in order to be effectively protected forestry money
Source, has the most used bamboo charcoal to substitute Linesless charcoal, thus can be substantially reduced the demand to natural timber, thus be widely used
Every aspect to life staying idle at home.Biomass carbonated utilize thermal chemical reaction principle exactly, using bamboo bits the like waste as material
Green recyclable fuel prepared by raw material, and in carbonization process, moisture and volatile matter content unnecessary in raw material of substance is removed, biological
Cellulose in raw material, hemicellulose, lignin etc. are partially exploded, and finally give bamboo charcoal, bamboo tar, Bamboo vinegar solution etc. and produce
Thing.But process equipment of making charcoal falls behind, and there are problems, is in particular in:
One, reacting gas is at furnace interior combustion heating, and in causing body of heater, material is heated uneven, owing to the charcoal generated produces
Product natural cooling or directly by water-cooled, cause part charcoal product spontaneous combustion or and water react, charcoal production rate reduces, if
It is water-cooled, cooling water can cause environmental pollution containing organic compound directly discharges such as tar；
Two, the product char temperature got rid of is the highest, and the heat in course of reaction can not be utilized effectively, and causes heat wave
Take；
Three, course of reaction is had to charcoal product, the product such as the water gas of generation, Bamboo vinegar solution and bamboo tar can not get back
Receiving, cause the wasting of resources, being discharged in air again can be to environment.
Utility model content
For the problems referred to above, have developed a kind of char yield rate height, comprehensive utilization ratio bamboo high, free of contamination material continuously carbonizing
Stove.
For solving the problems referred to above, the technical solution of the utility model is:
A kind of bamboo material continuous carbonization furnace, including heating system, the gentle water reclamation system of carbonization system.It is characterized in that,
Heating system is positioned on the base of whole bamboo material continuous carbonization furnace bottom, by hot blast endless tube, cooled coal gas pipe and carbonization system
The body of heater of system is connected, and the liquid-ring type pressuring machine of crossing of heating system is connected with the coal gas preserver of air water recovery system by pipeline；
Carbonization system agent set is positioned at the centre position of base, and the body of heater of carbonization system and the one group of coal gas being positioned at throat platform are collected
Endless tube is connected；
Described heating system is by two regenerative heat-exchange stoves, three liquid-ring type pressuring machines, combustion fan, hot air rings
Pipe, cooled coal gas pipe, chimney, sealing hydraulic gate valve composition.Two regenerative heat-exchange stoves are placed side by side on base plate, to being passed through stove
Internal coal gas heats；Three liquid-ring type pressuring machines are positioned at the right side of regenerative heat-exchange stove, have two liquid-ring type pressuring machines
It is connected with regenerative heat-exchange stove by pipeline, for being passed through coal gas to regenerative heat-exchange stove；3rd liquid-ring type pressuring machine passes through
Cooled coal gas pipe is connected with the cooling chamber of body of heater lower end, for being passed through cooled coal gas to cooling chamber；Combustion fan is positioned at regenerative heat-exchange
The left side of stove, is connected with regenerative heat-exchange stove by pipeline, is passed through air when regenerative heat-exchange stove preheats；Regenerative heat-exchange stove
It is connected with chimney by pipeline, the gas discharge generated after preheating is completed；Regenerative heat-exchange stove is by pipeline and hot blast endless tube
Being connected, hot blast endless tube communicates with the annular distance on body of heater, is passed through heating gas to body of heater.
Described carbonization system by semi-underground blow tank, chapelet, intermediate bunker, conveying worm, throat platform,
Body of heater, hot blast endless tube platform, furnace foundation platform and base composition.The most semi-underground blow tank and chapelet are arranged on body of heater
Left side, chapelet is for feeding the material lifting in semi-underground blow tank in intermediate bunker to certain altitude；Middle material
Storehouse is arranged on above throat platform, is used for storing material；Intermediate bunker lower end is provided with conveying worm, for by intermediate bunker
In material feed in body of heater；Body of heater, below conveying worm, is fixed on furnace foundation platform, and furnace interior is the most successively
For preheating cavity, dewatering cavity, carbonization chamber and cooling chamber.
Described air water recovery system is collected endless tube, gravity type cleaner unit, conveying worm, Venturi tube dedusting by coal gas
Device, moisture trap, coal gas preserver, separation pond composition.Wherein gravity type cleaner unit, venturi scrubber, gas-water separation
Device is mounted side by side on the right side of body of heater, and coal gas is collected endless tube and is connected with gravity type cleaner unit by pipeline.Conveying worm is arranged on
The lower end of gravity type cleaner unit, is used for discharging product；Gravity type cleaner unit upper end is connected with venturi scrubber by pipeline, weight
Power formula cleaner unit, venturi scrubber are mainly used in removing the impurity that coal gas brings out；Venturi scrubber and moisture trap
Being connected, moisture trap is mainly used in separating gas with liquid；Coal gas preserver passes through pipeline and moisture trap upper end phase
Even, it is mainly used in the storage of coal gas；Separate pond and be arranged on the lower section of coal gas preserver, separate pond and divided with air water by pipeline
It is connected from device lower end, is mainly used in by different components product separately.
Beneficial effect
1, in using high-temperature medium, hot mode carries out bamboo wood dry distilling, improves more than 10 times than outer hot mode dry distillation rate；
2, heating medium is passed through furnace interior after being heated by outside regenerative heat-exchange stove again, and in can making body of heater, bamboo wood is heated
Uniformly, providing oxygen-free environment for dry distillation reactor, it is possible to more efficient carbonization, charcoal production rate is high, and produced calorific value of gas is high；
3, the high temperature bamboo charcoal that dry distilling generates uses cold medium cooling, had both reduced charcoal product temperature, and had improve charcoal recovery rate,
Can preheat to reacting gas again, effectively utilize heat；
4, this bamboo material continuous carbonization furnace has separating system for water, can be realized by coal gas collection endless tube, coal gas preserver
Recovery and storage to coal gas, effectively can isolate bamboo tar, bamboo by the separation pond of separating system for water from coal gas
The products such as vinegar liquid, improve resource utilization, simultaneously during without garbage generation, will not be to environment.
Accompanying drawing explanation
Fig. 1 is the front view of a kind of bamboo material continuous carbonization furnace structural representation；
Fig. 2 is the left view of a kind of bamboo material continuous carbonization furnace structural representation；
Fig. 3 is the top view of a kind of bamboo material continuous carbonization furnace structural representation；
Wherein, the semi-underground blow tank of 1-；2-chapelet；3-intermediate bunker；4-conveying worm；5-coal gas collects ring
Pipe；6-throat platform；7-body of heater；8-hot blast endless tube；9-hot blast endless tube platform；10-regenerative heat-exchange stove；11-regenerative heat-exchange
Stove；12-combustion fan；13-liquid-ring type pressuring machine；14-liquid-ring type pressuring machine；15-liquid-ring type pressuring machine；16-cooled coal gas pipe；
17-chimney；18-sealing hydraulic gate valve；19-sealing hydraulic gate valve；20-sealing hydraulic gate valve；21-sealing hydraulic lock
Valve；22-sealing hydraulic gate valve；23-sealing hydraulic gate valve；24-sealing hydraulic gate valve；25-sealing hydraulic gate valve；
The sealed liquid of 26-；Pressure gate valve；27-sealing hydraulic gate valve；28-base；29-furnace foundation platform；30-gravity type cleaner unit；31-
Conveying worm；32-venturi scrubber；33-moisture trap；34-separates pond；35-separates pond；36-coal gas is stored
Cabinet.
Detailed description of the invention
In conjunction with accompanying drawing, describe this utility model in detail:
A kind of bamboo material continuous carbonization furnace, including heating system, the gentle water reclamation system of carbonization system.
Described heating system by regenerative heat-exchange stove 10,11, liquid-ring type pressuring machine 13,14,15, combustion fan 12, heat
Vane pipe 8, cooled coal gas pipe 16, sealing hydraulic gate valve 18,19,20,21,22,23,24,25,26,27, chimney 17 forms.Water
Ring type pressuring machine 13 is connected with regenerative heat-exchange stove 10,11 respectively by pipeline, between be provided with sealing hydraulic gate valve 24,
25, liquid-ring type pressuring machine 14 is connected with regenerative heat-exchange stove 10,11 respectively by pipeline, between sealing hydraulic gate valve is installed
20,21, combustion fan 12 is connected with regenerative heat-exchange stove 10,11 respectively by pipeline, between sealing hydraulic gate valve is installed
22,23, regenerative heat-exchange stove 10 is connected with hot blast endless tube 8 by pipeline, between sealing hydraulic gate valve 18, heat accumulating type are installed
Recuperative furnace 10 is connected with chimney 17 by pipeline, between sealing hydraulic gate valve 27 is installed, regenerative heat-exchange stove 11 is by managing
Road is connected with hot blast endless tube 8, between sealing hydraulic gate valve 19 is installed, regenerative heat-exchange stove 11 is by pipeline and chimney 17 phase
Even, between, sealing hydraulic gate valve 26 is installed.During heating system work, open sealing hydraulic gate valve 20,22,27, close
Sealing hydraulic gate valve 18,19,21,24,25,26, coal gas is fed regenerative heat-exchange stove by pipeline by liquid-ring type pressuring machine 14
In 10, air is fed in regenerative heat-exchange stove 10 by pipeline by combustion fan 12, and gas-fired adds to regenerative heat-exchange stove 10
Heat, the gas of generation is discharged through chimney 17.After regenerative heat-exchange stove 10 has heated, close sealing hydraulic gate valve 20,22,
27, open sealing hydraulic gate valve 18,24, liquid-ring type pressuring machine 13 is passed through coal gas and enters heat after regenerative heat-exchange stove 10 heats
Vane pipe 8, is passed through coal gas of high temperature to body of heater 7.Simultaneously open sealing hydraulic gate valve 21,23,26, liquid-ring type pressuring machine 14
Feeding in regenerative heat-exchange stove 11 by coal gas by pipeline, air is fed regenerative heat-exchange stove 11 by pipeline by combustion fan 12
In, gas-fired is heated to regenerative heat-exchange stove 11, and the gas of generation is discharged through chimney 17.Treat that regenerative heat-exchange stove 11 heats
After completing, closing sealing hydraulic gate valve 21,23,26, open sealing hydraulic gate valve 19,25, liquid-ring type pressuring machine 13 is passed through
Coal gas enters hot air ring pipe 8 after regenerative heat-exchange stove 11 heats, and is passed through coal gas of high temperature to body of heater 7.It is then shut off sealed liquid
Pressure gate valve 18,24, opens sealing hydraulic gate valve 20,22,27, heats again to regenerative heat-exchange stove 10.Regenerative heat-exchange stove
10,11 alternately operating, is passed through coal gas of high temperature constantly to body of heater 7.
Described carbonization system is by semi-underground blow tank 1, chapelet 2, intermediate bunker 3, conveying worm 4, furnace roof
Platform 6, body of heater 7, hot blast endless tube platform 9, base 28, furnace foundation platform 29 form.Semi-underground blow tank 1 is positioned at below base 28,
Chapelet 2 is positioned on base 28, and above semi-underground blow tank 1, intermediate bunker 3 is on the right side of chapelet 2 upper end
Position, intermediate bunker 3 lower end is provided with conveying worm 4, and conveying worm 4 is throat platform 6 below, throat platform 6 lower end
For body of heater 7, hot blast endless tube platform 9 is positioned at position at lower 1/3rd of body of heater, and body of heater 7 is arranged on furnace foundation platform 29, furnace foundation
Platform 29 is base 28 below.Material is fed by semi-underground blow tank 1, through chapelet 2 transport to intermediate bunker 3, middle
The material of feed bin 3 feeds body of heater 7 through conveying worm 4, reacts with the heating gas being passed through.Most of gas that reaction produces
Body is collected endless tube 5 by the annular distance of throat platform 6 through coal gas and is entered air water recovery system.The bamboo charcoal that reaction produces is by body of heater 7 times
End is discharged.
Described air water recovery system is collected endless tube 5, gravity type cleaner unit 30, conveying worm 31, Venturi tube by coal gas
Cleaner unit 32, moisture trap 33, coal gas preserver 36, separation pond 34, separation pond 35 form.Coal gas is collected endless tube 5 and is led to
Piping is connected with gravity type cleaner unit 30, and gravity type cleaner unit 30 lower end is provided with conveying worm 31, gravity type cleaner unit
30 are connected with venturi scrubber 32, and venturi scrubber 32 is connected with moisture trap 33, and moisture trap 33 upper end is passed through
Pipeline is connected with coal gas preserver 36, moisture trap 33 lower end by pipeline with separate pond 34, separate pond 35 and be connected.Coal
Gas is collected the coal gas of endless tube 5 collection and is entered gravity type cleaner unit 30 through pipeline, and the bamboo tar of condensation passes through gravity type cleaner unit 30
The conveying worm 31 of bottom is discharged, for bamboo tar product.Gas through gravity type cleaner unit 30 enters venturi scrubber
32, after remove impurity, enter moisture trap 33, the gas that moisture trap 33 produces is imported coal gas preserver 36, gas by pipeline
The liquid that water separator 33 produces is entered by pipeline and separates pond 34,35.
Last it is noted that obviously, above-described embodiment is only for clearly demonstrating the application example, and not
Restriction to embodiment.For those of ordinary skill in the field, can also make on the basis of the above description
The change of other multi-form or variation.Here without also cannot all of embodiment be given exhaustive.And thus amplified
Among the obvious change gone out or the variation protection domain still in the application type.
Claims (3)
1. a bamboo material continuous carbonization furnace, including heating system, the gentle water reclamation system of carbonization system, it is characterised in that: institute
The heating system stated is by regenerative heat-exchange stove, liquid-ring type pressuring machine, combustion fan, hot blast endless tube, cooled coal gas pipe, chimney and close
Envelope formula hydraulic sluice valve forms, and wherein part liquid-ring type pressuring machine is connected with regenerative heat-exchange stove, and part liquid-ring type pressuring machine is with cold
Gas pipe is connected, and combustion fan is connected with regenerative heat-exchange stove by pipeline, and regenerative heat-exchange stove is connected with chimney by pipeline,
Regenerative heat-exchange stove is connected with hot blast endless tube by pipeline, and hot blast endless tube is fixed on hot blast endless tube platform；Described carbonization system
System is by semi-underground blow tank, chapelet, intermediate bunker, conveying worm, throat platform, body of heater, hot blast endless tube platform, stove
Based platform and base composition, body of heater is made up of preheating cavity, dewatering cavity, carbonization chamber and cooling chamber, the most semi-underground blow tank and chain
Bucket elevator is connected and is fixed on base, and intermediate bunker is arranged on above throat platform, and intermediate bunker lower end is provided with
Conveying worm, body of heater, below conveying worm, is fixed on furnace foundation platform, and furnace interior is followed successively by preheating from the top down
Chamber, dewatering cavity, carbonization chamber and cooling chamber；Described air water recovery system is collected endless tube, gravity type cleaner unit, spiral transferring by coal gas
Sending machine, venturi scrubber, moisture trap, coal gas preserver, separate pond composition, wherein coal gas collection endless tube passes through pipeline
Being connected with gravity type cleaner unit, gravity type cleaner unit is arranged on furnace foundation platform, and gravity type cleaner unit lower end is provided with spiral transferring
Sending machine, gravity type cleaner unit is connected with venturi scrubber by pipeline, and venturi scrubber is connected with moisture trap, air water
Separator is arranged on furnace foundation platform, and moisture trap upper end is connected with coal gas preserver by pipeline, moisture trap lower end
It is connected with separating pond by pipeline；Described heating system is by hot blast endless tube, the body of heater phase of cooled coal gas pipe and carbonization system
Even, being connected with the coal gas preserver of air water recovery system by liquid-ring type pressuring machine, the body of heater of carbonization system is by being positioned at furnace roof
The coal gas of platform is collected endless tube and is connected with air water recovery system.
Retort the most according to claim 1, it is characterised in that: the regenerative heat-exchange stove minimum two of described heating system
Platform, can use with multiple stage exchange.
Retort the most according to claim 1, it is characterised in that: the separation pond minimum two of described air water recovery system
Individual, can multiple exchanges use.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620010530.9U CN205473575U (en) | 2016-01-07 | 2016-01-07 | Continuous retort of bamboo material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620010530.9U CN205473575U (en) | 2016-01-07 | 2016-01-07 | Continuous retort of bamboo material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205473575U true CN205473575U (en) | 2016-08-17 |
Family
ID=56665167
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620010530.9U Withdrawn - After Issue CN205473575U (en) | 2016-01-07 | 2016-01-07 | Continuous retort of bamboo material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205473575U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105482837A (en) * | 2016-01-07 | 2016-04-13 | 唐山希锐自动化设备有限公司 | Bamboo substance continuous carbonization furnace |
-
2016
- 2016-01-07 CN CN201620010530.9U patent/CN205473575U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105482837A (en) * | 2016-01-07 | 2016-04-13 | 唐山希锐自动化设备有限公司 | Bamboo substance continuous carbonization furnace |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160817 Effective date of abandoning: 20180202 |
|
| AV01 | Patent right actively abandoned |