CN207062200U - A kind of biomass conventional pyrolysis device - Google Patents
A kind of biomass conventional pyrolysis device Download PDFInfo
- Publication number
- CN207062200U CN207062200U CN201720721362.9U CN201720721362U CN207062200U CN 207062200 U CN207062200 U CN 207062200U CN 201720721362 U CN201720721362 U CN 201720721362U CN 207062200 U CN207062200 U CN 207062200U
- Authority
- CN
- China
- Prior art keywords
- ark
- sample
- heater
- corundum noah
- tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 24
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 21
- 239000010431 corundum Substances 0.000 claims abstract description 27
- 229910052593 corundum Inorganic materials 0.000 claims abstract description 27
- 239000007789 gas Substances 0.000 claims abstract description 24
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 16
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000012159 carrier gas Substances 0.000 claims abstract description 14
- 239000011449 brick Substances 0.000 claims abstract description 8
- 238000001035 drying Methods 0.000 claims abstract description 8
- 229910052742 iron Inorganic materials 0.000 claims abstract description 8
- 230000000505 pernicious effect Effects 0.000 claims abstract description 7
- 238000010521 absorption reaction Methods 0.000 claims abstract description 6
- 239000010977 jade Substances 0.000 claims 1
- 239000000047 product Substances 0.000 description 8
- 239000012075 bio-oil Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 210000000952 spleen Anatomy 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
A kind of biomass conventional pyrolysis device is the utility model is related to, belongs to biomass resource technical field of comprehensive utilization.The body of heater that heater and thermocouple are formed is provided with around the device alundum tube, heater and thermocouple are connected with temperature-controlling system, heater is located on iron stand with temperature-controlling system, insulating brick is additionally provided with alundum tube, sample corundum Noah's ark is provided with inside alundum tube one end, charge door is provided with the top of sample corundum Noah's ark, sample corundum Noah's ark side is provided with push rod, sample corundum Noah's ark side is additionally provided with carrier gas connector and is connected with carrier gas, sample corundum Noah's ark opposite side by rubber tube successively with condenser pipe, two-mouth bottle connects, the other end of two-mouth bottle successively with pernicious gas absorption bottle, U-shaped drying tube connects with gas collecting bag.The apparatus structure is simple, better performances.
Description
Technical field
A kind of biomass conventional pyrolysis device is the utility model is related to, belongs to biomass resource technical field of comprehensive utilization.
Background technology
Biomass be primarily referred to as the lignocellulosics such as stalk in agriculture and forestry production process in addition to grain, fruit, trees,
The materials such as fowl and animal excrement during heel, agriculture and forestry organic waste material and Animal husbandry production and discarded object under farming industry.It
There is recyclability, low stain and widely distributed property.Biomass resource can be converted into using pyrolytic technique by storage
Fortune is convenient, the liquid fuel of high value(Bio oil), be advantageous to the higher value application of biomass resource, have to alleviating energy crisis
It is significant.
Biomass pyrolysis liquefaction refers to the heating biological matter under conditions of anoxic, brings it about cracking and obtains charcoal and heat
Vent one's spleen, then pyrolysis gas is condensed rapidly, wherein condensable gases is converted into the process of liquid bio-oil.Pyrolytic process
It is the core of biomass pyrolysis liquefaction technology, determines the yield and quality of bio oil.
During conventional pyrolysis liquefaction process, body of heater is heated rapidly to predetermined temperature, then by charge door by material
It is added in Noah's ark, the corundum Noah's ark for filling material push-in soak zones is heated rapidly by pyrolysis, the gas of generation by push rod
Product and solid product are rapidly separated, and gaseous product carries through carrier gas and excludes body of heater, are obtained by condensing wherein condensable part
Bio oil.The shorter residence time reduces the second pyrolysis of gaseous product in body of heater, is advantageous to improve the quality of bio oil.
Currently without the preferable biomass conventional pyrolysis device of structural behaviour.
The content of the invention
For the above-mentioned problems of the prior art and deficiency, the utility model provides a kind of biomass conventional pyrolysis dress
Put.The apparatus structure is simple, better performances, and the utility model is achieved through the following technical solutions.
A kind of biomass conventional pyrolysis device, including carrier gas 1, push rod 2, sample corundum Noah's ark 3, charge door 4, thermocouple 5,
Insulating brick 6, alundum tube 7, body of heater 8, temperature-controlling system 9, rubber tube 10, iron stand 11, condenser pipe 12, two-mouth bottle 13, pernicious gas
Absorption bottle 14, U-shaped drying tube 15 and gas collecting bag 16, the body of heater that heater and thermocouple 5 are formed is provided with around alundum tube 7
8, heater and thermocouple 5 are connected with temperature-controlling system 9, and heater is located on iron stand 11 with temperature-controlling system 9, alundum tube 7
On be additionally provided with insulating brick 6, sample corundum Noah's ark 3 is provided with inside the one end of alundum tube 7, charge door is provided with the top of sample corundum Noah's ark 3
4, the side of sample corundum Noah's ark 3 is provided with push rod 2, and the side of sample corundum Noah's ark 3 is additionally provided with carrier gas connector and is connected with carrier gas 1, sample
The opposite side of product corundum Noah's ark 3 is connected with condenser pipe 12, two-mouth bottle 13 successively by rubber tube 10, the other end of two-mouth bottle 13 successively with
Pernicious gas absorption bottle 14, U-shaped drying tube 15 and gas collecting bag 16 connect.
The condenser pipe 12, two-mouth bottle 13 can be arranged to n groups according to actual conditions.
The operation principle of the biomass conventional pyrolysis device is:
(1)Biomass is crushed and screened, particle diameter between 60-120 mesh, then dried biomass to its moisture 10% with
Under, it is standby.
(2)The temperature of alundum tube 7 is increased to 400 DEG C by heater, it is by charge door 4 that biomass addition sample is firm
In beautiful Noah's ark 3, sample corundum Noah's ark 3 is then pushed into by the pyrolysis zone of alundum tube 7 by push rod 2, reacts the regular hour.
(3)Biomass pyrolytic reaction generation solid coke and pyrolysis gas, solid product are collected after gas all discharge,
Gaseous product is carried by carrier gas 1 and excludes body of heater.
(4)Gaseous product is cooled down after being discharged into body of heater 8 by condenser pipe 12, and bio oil is formed after condensation and is received in two-mouth bottle 13
Collection, non-condensable gas enter exhaust treatment system, and innocuous gas is ultimately discharged into air, can also be collected by gas pouch.
The beneficial effects of the utility model are:The present apparatus is simple in construction, better performances;Using the present apparatus realize solid with
The quick separating of gaseous product, and gaseous product is discharged body of heater rapidly, improve the yield of bio oil and improve biology
The quality of oil.
Brief description of the drawings
Fig. 1 is the utility model structure diagram;
Fig. 2 is the utility model furnace binding schematic diagram.
In figure:1- carrier gas, 2- push rods, 3- sample corundum Noah's arks, 4- charge doors, 5- thermocouples, 6- insulating bricks, 7- corundum
Pipe, 8- bodies of heater, 9- temperature-controlling systems, 10- rubber tubes, 11- iron stands, 12- condenser pipes, 13- two-mouth bottles, 14- pernicious gases absorb
Bottle, 15-U shape drying tubes, 16- gas collection bags.
Embodiment
With reference to the accompanying drawings and detailed description, the utility model is described in further detail.
Embodiment 1
The biomass conventional pyrolysis device, including carrier gas 1, push rod 2, sample corundum Noah's ark 3, charge door 4, thermocouple 5, guarantor
Warm brick 6, alundum tube 7, body of heater 8, temperature-controlling system 9, rubber tube 10, iron stand 11, condenser pipe 12, two-mouth bottle 13, pernicious gas are inhaled
Bottle 14, U-shaped drying tube 15 and gas collecting bag 16 are received, the body of heater 8 that heater and thermocouple 5 are formed is provided with around alundum tube 7,
Heater and thermocouple 5 are connected with temperature-controlling system 9, and heater is located on iron stand 11 with temperature-controlling system 9, on alundum tube 7
Insulating brick 6 is additionally provided with, sample corundum Noah's ark 3 is provided with inside the one end of alundum tube 7, the top of sample corundum Noah's ark 3 is provided with charge door 4,
The side of sample corundum Noah's ark 3 is provided with push rod 2, and the side of sample corundum Noah's ark 3 is additionally provided with carrier gas connector and is connected with carrier gas 1, sample
The opposite side of corundum Noah's ark 3 is connected with condenser pipe 12, two-mouth bottle 13 successively by rubber tube 10, and the other end of two-mouth bottle 13 is successively with having
Evil gas absorption bottle 14, U-shaped drying tube 15 and gas collecting bag 16 connect.
Embodiment 2
As illustrated in fig. 1 and 2, the biomass conventional pyrolysis device, structure is consistent with embodiment 1 with annexation, distinguishes
It can be arranged to two groups according to actual conditions in condenser pipe 12, two-mouth bottle 13.
Embodiment 3
As illustrated in fig. 1 and 2, the biomass conventional pyrolysis device, structure is consistent with embodiment 1 with annexation, distinguishes
It can be arranged to ten groups according to actual conditions in condenser pipe 12, two-mouth bottle 13.
Specific embodiment of the present utility model is explained in detail above in association with accompanying drawing, but the utility model is not
It is limited to above-mentioned embodiment, in those of ordinary skill in the art's possessed knowledge, this practicality can also be not being departed from
Various changes can be made on the premise of new objective.
Claims (2)
- A kind of 1. biomass conventional pyrolysis device, it is characterised in that:Including carrier gas(1), push rod(2), sample corundum Noah's ark(3)、 Charge door(4), thermocouple(5), insulating brick(6), alundum tube(7), body of heater(8), temperature-controlling system(9), rubber tube(10), iron stand (11), condenser pipe(12), two-mouth bottle(13), pernicious gas absorption bottle(14), U-shaped drying tube(15)With gas collecting bag(16), Alundum tube(7)Surrounding is provided with heater and thermocouple(5)The body of heater of composition(8), heater and thermocouple(5)With temperature control system System(9)Connection, heater and temperature-controlling system(9)Positioned at iron stand(11)On, alundum tube(7)On be additionally provided with insulating brick(6), just Jade pipe(7)Sample corundum Noah's ark is provided with inside one end(3), sample corundum Noah's ark(3)Top is provided with charge door(4), sample corundum Noah's ark(3)Side is provided with push rod(2), sample corundum Noah's ark(3)Side is additionally provided with carrier gas connector and carrier gas(1)Connection, sample Corundum Noah's ark(3)Opposite side passes through rubber tube(10)Successively with condenser pipe(12), two-mouth bottle(13)Connection, two-mouth bottle(13)It is another End successively with pernicious gas absorption bottle(14), U-shaped drying tube(15)With gas collecting bag(16)Connection.
- 2. biomass conventional pyrolysis device according to claim 1, it is characterised in that:The condenser pipe(12), two-mouth bottle (13)It can be arranged to n groups according to actual conditions.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720721362.9U CN207062200U (en) | 2017-06-21 | 2017-06-21 | A kind of biomass conventional pyrolysis device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720721362.9U CN207062200U (en) | 2017-06-21 | 2017-06-21 | A kind of biomass conventional pyrolysis device |
Publications (1)
Publication Number | Publication Date |
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CN207062200U true CN207062200U (en) | 2018-03-02 |
Family
ID=61509058
Family Applications (1)
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CN201720721362.9U Expired - Fee Related CN207062200U (en) | 2017-06-21 | 2017-06-21 | A kind of biomass conventional pyrolysis device |
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CN (1) | CN207062200U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111019679A (en) * | 2019-12-13 | 2020-04-17 | 中山大学 | Device for recovering energy substances from hyper-enriched plants and application thereof |
-
2017
- 2017-06-21 CN CN201720721362.9U patent/CN207062200U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111019679A (en) * | 2019-12-13 | 2020-04-17 | 中山大学 | Device for recovering energy substances from hyper-enriched plants and application thereof |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180302 |