CN108546556A - A kind of biomass pyrolysis system - Google Patents
A kind of biomass pyrolysis system Download PDFInfo
- Publication number
- CN108546556A CN108546556A CN201810328481.7A CN201810328481A CN108546556A CN 108546556 A CN108546556 A CN 108546556A CN 201810328481 A CN201810328481 A CN 201810328481A CN 108546556 A CN108546556 A CN 108546556A
- Authority
- CN
- China
- Prior art keywords
- combustion furnace
- pyrolysis
- connect
- hot
- input terminal
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/12—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating using gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
-
- 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
Abstract
The invention discloses a kind of biomass pyrolysis systems, including circulating-heating part, pyrolysis section and post-processing part；The circulating-heating part includes combustion chamber, hotair chamber and fuel addition room；The combustion chamber includes the components such as combustion furnace, insulating brick, natural gas spraying gun, burning bed and feed device；The hotair chamber includes the components such as swing bucket, heating room, gitter brick, left conduit, right conduit, left wind turbine, right wind turbine, gyration gear ring, turning motor and swiveling gear；The pyrolysis section includes the components such as pedestal, bearing block, shaft, support ring, pyrolysis oven, reamer, pyrolysis chamber, hot-air input terminal, solid output end, hot-air output end and driving motor.The heat that high heating value incineration firing is generated is used for the drying and pyrolysis of waste of low heating value, can effectively improve the utilization rate of heat and the economic benefit of processing plant.
Description
Technical field
The present invention relates to biomass processes fields, and in particular to a kind of biomass pyrolysis system.
Background technology
Biomass refers to the various organisms formed by photosynthesis, including all animals and plants and microorganism.It is raw
Substance can be then the form of energy that solar energy is stored in the form of chemical energy in biomass, it is always for the survival of mankind heavy
One of energy is wanted, is to be only second to the fourth largest source after coal, oil, natural gas, occupies in entire energy resource system important
Status.
Biomass includes all plant, microorganism and useless as the animal of food and its production using plant, microorganism
Gurry.Representational biomass such as crops, agricultural waste material, timber, timber waste and animal wastes.Narrow sense is general
It reads：Biomass is primarily referred to as the lignocellulosics such as stalk, trees in agriculture and forestry production process in addition to grain, fruit (referred to as
Lignin), farming industry leftover bits and pieces, the objects such as the fowl and animal excrement during agriculture and forestry organic waste material and Animal husbandry production and waste
Matter.
Directly burning is a kind of most common, extraction energy in the direct and slave biomass of commericially feasible mode.This
Kind mode cost is minimum, obtains energy also the most directly, but capacity usage ratio is relatively low.With the reduction of biomass energy,
It is also more and more to the diversification research of energy resource structure.House refuse, the agricultural waste etc. given it up before especially are also opened
Beginning progresses into research range.
But the calorific value of these rubbish is low, deals with more difficulty, so also only being tried out in a small range.With
The diversification of rubbish type, the sharp increase of quantity, the progress of technology and increasingly harsh ecological requirements, these low heat values,
The processing cost and economic benefit of difficult rubbish improve there has also been apparent.Treatment technology is towards integrated, Composite and comprehensive
The direction of combination is developed.
Invention content
The present invention is intended to provide a kind of processing classification diversification, low energy consumption for processing, environmentally protective biomass pyrolysis system.
The present invention adopts the following technical scheme that：
A kind of biomass pyrolysis system, it is characterised in that：Including circulating-heating part, pyrolysis section and post-processing part；
The circulating-heating part includes combustion chamber, hotair chamber and fuel addition room；
Insulating brick, the gas spraying in combustion furnace that the combustion chamber includes combustion furnace, is distributed on combustion furnace inner wall
Rifle, the burning bed and feed device being fixed on combustion furnace inner wall；
The hotair chamber includes swing bucket, four heating rooms being fixed in swing bucket, is deposited in the indoor accumulation of heat of heating
Brick, the right conduit being fixed on swing bucket top surface, is connect with left conduit free end the left conduit being fixed on swing bucket top surface
Left wind turbine, the gyration gear ring being fixed on swing bucket side wall, is mounted on burning furnace roof at the right wind turbine being connect with right conduit free end
Turning motor on face and the swiveling gear on turning motor output shaft；
The swiveling gear is engaged with gyration gear ring；
The swing bucket is mounted on burning furnace top surface；
It is the pyrolysis section includes pedestal, is symmetrically mounted on pedestal bearing block, the shaft being located on bearing block, symmetrical fixed
The pyrolysis oven of support ring and support ring rotation connection in shaft, is located on pyrolysis furnace outer wall the reamer being fixed in shaft
Pyrolysis chamber, be located at pyrolysis chamber on hot-air input terminal, be located on pyrolysis oven solid output end, be located at pyrolysis chamber on heat
Air output end and it is connected with the rotating shaft driving motor.
As further solution：The burning bed is obliquely installed；The burning bed is in combustion furnace two opposite
It is arranged alternately on side wall.
As further solution：The combustion furnace is equipped with discharge system；The discharge system includes being opened in combustion
It burns rectangular aperture on furnace bottom face, the slideway for being fixed on rectangular aperture both sides, the baffle being located on slideway and is connect with baffle
Pushing meanss.
As further solution：The feed device includes the barrel being rotatablely connected with combustion furnace, circular array
Baffle in barrel, with the exhaust pipe of barrel rotation connection, the rotary electric machine being fixedly mounted on combustion furnace and mounted on turning
Driving wheel on dynamic motor output shaft；
The driving wheel is contacted with barrel；
The junction of the barrel and combustion furnace is provided with stomata；It is fixed with steel wire on the stomata；It is provided on the steel wire
Feed opening；
Barrel is divided into multiple fan sections by the baffle；The shape of the feed opening is identical as the shape in fan section.
As further solution：It is fixed with flow distribution plate on the top surface of the combustion furnace.
As further solution：The free end of the exhaust pipe is connect with hot-air input terminal.
As further solution：The post-processing section point includes spray column and pulverizer；
The input terminal of the spray column is connect with hot-air output end；
The input terminal of the pulverizer is connect with solid output end.
As further solution：Further include scavenging air valve A, scavenging air valve B and hot air duct；
The scavenging air valve A and scavenging air valve B is all provided with there are three connecting pin；
The hot air duct is set there are two input terminal and an output end；
First connecting pin of the scavenging air valve A and first input terminal of hot air duct connect, second connecting pin and a left side
Wind turbine connects, and third connecting pin is open end；
First connecting pin of the scavenging air valve B and second input terminal of hot air duct connect, second connecting pin and the right side
Wind turbine connects, and third connecting pin is open end；
The output end of the hot air duct is connect with hot-air input terminal.
The good effect that the present invention generates is as follows：
The process range of the present invention is wide, comprehensive benefit higher.The present invention is carried out for agricultural stalk, leaf and daily life rubbish
Processing, rubbish source is more extensive, can effectively expand rubbish source, reduces the dependence to rubbish type.It can effectively solve the problem that
Single treatment source is the unstable problem for the treatment of capacity.For processing plant, daily fixation operation cost is constant,
Stable rubbish source can make factory be in oepration at full load state always, ensure that daily processing benefit is runed higher than fixed
Cost improves the hematopoietic potential of processing plant, ensures that the operation that it can stablize down.
The present invention can effectively cut operating costs, and improve the utilization ratio of energy.Agricultural waste calorific value is higher, handles
It is relatively easy to, is mainly used for combustion heat supplying；House refuse complicated component, washiness cannot directly burn, be dried
Dry, the calorific value of especially most of house refuse is very low, is more suitable for being pyrolyzed.The heat generated using high heating value agricultural waste
Amount low heat value house refuse is dried and is pyrolyzed, not only solve the source problem that comes of heat, also effectively reduce coal, electricity and
The consumption of the energy such as natural gas does not need outside energy input and is just able to maintain that stable fortune after processing procedure stable operation
Row, operating cost are very low.
Description of the drawings
Fig. 1 is the layout of the present invention；
Fig. 2 is the structural schematic diagram of combustion furnace；
Fig. 3 is the sectional view of swing bucket；
Fig. 4 is the structural schematic diagram of pyrolysis section；
Fig. 5 is the sectional view of combustion furnace；
Fig. 6 is the sectional view of barrel；
Fig. 7 is the vertical view of steel wire；
Fig. 8 is the sectional view of scavenging air valve A；
Fig. 9 is the operating diagram of scavenging air valve A；
Wherein：11 combustion furnaces, 12 insulating bricks, 13 natural gas spraying guns, 14 burning beds, 21 swing buckets, 22 heating rooms, 23 gitter bricks,
24 left conduits, 25 right conduits, 26 left wind turbines, 27 right wind turbines, 28 gyration gear rings, 29 turning motors, 210 swiveling gears, 31 pedestals,
32 bearing blocks, 33 shafts, 34 support rings, 35 pyrolysis ovens, 36 reamers, 37 pyrolysis chambers, 38 hot-air input terminals, the output of 39 solids
End, 310 hot-air output ends, 311 driving motors, 41 rectangular apertures, 42 slideways, 43 baffles, 51 barrels, 52 baffles, 53 exhausts
Pipe, 54 rotary electric machines, 55 driving wheels, 56 stomatas, 57 steel wires, 58 feed openings, 6 flow distribution plates, 7 spray columns, 8 pulverizers, 91 are changed
Air valve A, 92 scavenging air valve B, 93 hot air ducts.
Specific implementation mode
With reference to Fig. 1-9, invention is further explained.
The present invention adopts the following technical scheme that：
A kind of biomass pyrolysis system, it is characterised in that：Including circulating-heating part, pyrolysis section and post-processing part；
The circulating-heating part includes combustion chamber, hotair chamber and fuel addition room；
The combustion chamber includes combustion furnace 11, is distributed on 11 inner wall of combustion furnace insulating brick 12, in combustion furnace 11
Natural gas spraying gun 13, the burning bed 14 and feed device being fixed on 11 inner wall of combustion furnace；
The hotair chamber includes 21, four heating rooms 22 being fixed in swing bucket 21 of swing bucket, is deposited in heating room 22
Interior gitter brick 23, the left conduit 24 being fixed on 21 top surface of swing bucket, the right conduit 25 being fixed on 21 top surface of swing bucket, with
The left wind turbine 26 of 24 free end of left conduit connection, is fixed on 21 side of swing bucket at the right wind turbine 27 being connect with 25 free end of right conduit
Gyration gear ring 28 on wall, the turning motor 29 on 11 top surface of combustion furnace and on 29 output shaft of turning motor
Swiveling gear 210；
The swiveling gear 210 is engaged with gyration gear ring 28；
The swing bucket 21 is mounted on 11 top surface of combustion furnace；
The pyrolysis section includes pedestal 31, is symmetrically mounted on pedestal 31 bearing block 32 sets shaft on bearing blocks 32
33, the pyrolysis oven 35 for support ring 34 and support ring 34 rotation connection being symmetrically fixed in shaft 33 is fixed in shaft 33
Reamer 36, the hot-air input terminal 38 being located on pyrolysis chamber 37, is located at pyrolysis oven at the pyrolysis chamber 37 being located on 35 outer wall of pyrolysis oven
Solid output end 39, the hot-air output end 310 being located on pyrolysis chamber 37 on 35 and the driving motor being connect with shaft 33
311。
As further solution：The burning bed 14 is obliquely installed；The burning bed 14 is in combustion furnace 11 two
It is arranged alternately on opposite side wall.
As further solution：The combustion furnace 11 is equipped with discharge system；The discharge system includes being opened in
Rectangular aperture 41, the slideway 42 for being fixed on 41 both sides of rectangular aperture on 11 bottom surface of combustion furnace, the baffle 43 being located on slideway 42
With the pushing meanss being connect with baffle 43.
As further solution：The feed device includes the barrel 51 being rotatablely connected with combustion furnace 11, circle
The exhaust pipe 53 of baffle 52 and barrel 51 rotation connection of the array in barrel 51, the rotation being fixedly mounted on combustion furnace 11
Motor 54 and the driving wheel 55 on 54 output shaft of rotary electric machine；
The driving wheel 55 is contacted with barrel 51；
The barrel 51 and the junction of combustion furnace 11 are provided with stomata 56；Steel wire 57 is fixed on the stomata 56；The steel
Feed opening 58 is provided on silk screen 57；
Barrel 51 is divided into multiple fan sections by the baffle 52；The shape of the feed opening 58 is identical as the shape in fan section.
As further solution：Flow distribution plate 6 is fixed on the top surface of the combustion furnace 11.
As further solution：The free end of the exhaust pipe 53 is connect with hot-air input terminal 37.
As further solution：The post-processing section point includes spray column 7 and pulverizer 8；
The input terminal of the spray column 7 is connect with hot-air output end 39；
The input terminal of the pulverizer 8 is connect with solid output end 38.
As further solution：Further include scavenging air valve A91, scavenging air valve B92 and hot air duct 93；
The scavenging air valve A91 and scavenging air valve B92 is all provided with there are three connecting pin；
The hot air duct 93 is set there are two input terminal and an output end；
First connecting pin of the scavenging air valve A91 is connect with first input terminal of hot air duct 93, second connecting pin
It is connect with left wind turbine 26, third connecting pin is open end；
First connecting pin of the scavenging air valve B92 is connect with second input terminal of hot air duct 93, second connecting pin
It is connect with right wind turbine 27, third connecting pin is open end；
The output end of the hot air duct 93 is connect with hot-air input terminal 37.
With reference to specific processing procedure, invention is further explained.
It includes stalk, wheat husk and stick that, which there are agricultural waste and house refuse two large divisions, agricultural waste in the processing source of the present invention,
Core etc. can burn, the relatively high substance of calorific value；House refuse includes the object that fruit peel, food and leaf etc. can burn
Matter.
The structure of feed device and operational process are introduced first.Feed device is by barrel 51, baffle 52, exhaust pipe
53, the components such as rotary electric machine 54, driving wheel 55, stomata 56, steel wire 57 and feed opening 58 form.Baffle 52 divides barrel 51
At multiple fan sections, fan section is independently arranged.The effect of steel wire 57 is to stop that the agricultural waste in fan section falls to combustion
The hot-air in combustion furnace 11 can be imported into fan section while burning stove 11, pre-add is carried out to the agricultural waste of its inside
Heat.58 shape of feed opening on steel wire 57 is identical as the shape in fan section, is driven and is expected by driving wheel 55 in rotary electric machine 54
When cylinder 51 rotates, the sequence of the agricultural waste in each fan section is made to fall in combustion furnace 11.The diameter and material of exhaust pipe 53
Cylinder 51 is identical, but reserves a filling hole in the joint of the two, can at any time be supplemented during barrel 51 rotates.
Working site can also make an end cap to match with filling hole as needed, and when charging takes away, and is put after the completion of filling
It returns on filling hole.
When first filling, the velocity of rotation of barrel 51 is fast, needs to fill in each fan section, after stable, barrel
51 uniform speed slows rotate, at this point, it is sky fan section to be located at filling hole, it is only necessary to load at this.Fan section is according to suitable
Sequence arranges, and is located at first that the fan section at filling hole is located at sequence, is located at the fan section at feed opening 58 and is located at last position, this
The preheating time of sample agricultural waste is longer, can effectively improve the temperature into agricultural waste in combustion furnace 11, avoid combustion furnace
Temperature fluctuation is frequent in 11.Because of the calorific value of agricultural waste or relatively low, it is therefore desirable to ensure the stabilization of temperature in combustion furnace 11
Property, it avoids stopping working.
The air that combustion furnace 11 needs is injected by hotair chamber.There are two connecting pin, the two alternatings for hotair chamber
Undertake the effect of air input and tail gas output end.Motor steering in left wind turbine 26 and right wind turbine 27 changes, and ensures the work(
The realization of energy.The top surface for heating room 22 is connect with heating 22 body rotation of room, by swiveling gear 210 and is returned in turning motor 29
During turning the drive heating rotation of room 22 of gear ring 28, heating 22 top surface of room is motionless.
It is opened on the top surface of combustion furnace 11 there are two air hole, makees air input and tail gas output uses.Flow distribution plate 6 is vertical
Between the two air holes, air and tail gas hypotelorism is avoided to lead to air turbulence.Think that the two distance compares
When close, it is very easy to extract out the air of input when taking out tail gas, 11 temperature of combustion furnace is caused to decline and for hypoxgia.
When left conduit 24 undertakes the effect of tail gas output end, high-temperature tail gas will be in the heating room 22 that connect with left conduit 24
Gitter brick 23 heat, exhaust temperature reduce；Right conduit 25 undertakes the effect of air input at this time, is connect with right conduit 25
Gitter brick 23 in hot cell 22 is heated the Cryogenic air in combustion furnace 11 is inputted, and can effectively avoid the temperature in combustion furnace 11
Fluctuation.
When swing bucket 21 rotates, heating room 22 also rotates therewith.By above description it is recognised that heating room 22 is also handed over
For carry heating air and accumulation of heat effect.Four heating rooms 22 can effectively reduce the hot and cold alternation frequency of gitter brick 23,
Improve its service life.When the treating capacity of the present invention increases, the quantity of heating room 22 is also required to increase therewith, is stored to reduce
The replacement frequency of hot brick 23.
Agricultural waste is fallen on the burning bed 14 in combustion furnace 11.Inclined burning bed 14 is alternately arranged at combustion furnace 11
On two opposite inner walls, agricultural waste slides on inclined burning bed 14, sequentially passes through each burning bed 14, Neng Gouzeng
Add its residence time in combustion furnace 11, can realize during especially moving and fall and to be come into full contact with air, fires
Burn more abundant, the flame-out phenomenon in bottom when avoiding accumulation burning.When natural gas spraying gun 13 is as heat source and low temperature is started
Heat supplement source, insulating brick 12 can effectively completely cut off heat loss, play good heat insulation effect.
House refuse is directly poured into pyrolysis oven 35.Filler on pyrolysis oven 35 may be used open flange soon after, beat
Evolution just, good airproof performance.After the completion of filling, driving motor 311 acts, and 36 turns of reamer is driven by shaft 33 and support ring 34
It is dynamic.Reamer 36 crushes house refuse when rotating, and is carried out at the same time and stirs, and enables fully dry and pyrolysis.
The high-temperature tail gas and scavenging air valve A91, scavenging air valve are passed through to the hot-air after agricultural waste preheating that combustion furnace 11 generates
B92, hot air duct 93 and hot-air input terminal 38 are injected into pyrolysis chamber 37, and the heat of high-temperature tail gas and hot-air passes through heat
Solution stove 35 passes to house refuse, and pyrolysis oven 35 is in closed state at this time, and house refuse is pyrolyzed under oxygen-free environment.
House refuse after the completion of pyrolysis is exported by solid output end 39, is transported to progress separating twice at pulverizer 8,
House refuse after the completion of processing can carry out fermentation and make organic fertilizer or be backfilling into soil.It needs simultaneously in pyrolysis oven 35
Increase a connecting tube between spray column 7 to need at it because will produce a large amount of gaseous contaminations in pyrolytic process
Reason.
The high-temperature tail gas and hot-air one-way flow being pyrolyzed in chamber 37, by hot empty after the outflow of hot-air output end 310
Airway 93 equally imported into spray column 7 and is handled.
The effect of scavenging air valve A91 and scavenging air valve B92 are to ensure the positive production work of combustion furnace 11.Detailed process is：Scavenging air valve
It is equipped with the rotatable spool with air flue in A91, scavenging air valve A91 is as intake valve in use, spool will be connected with extraneous air
Connecting pin and the connecting pin being connect with left wind turbine 26 are connected, and air enters combustion furnace 11；When scavenging air valve A91 is used as air bleeding valve
When, spool connects the connecting pin being connect with hot air duct 93 and the connecting pin being connect with left wind turbine 26,11 tail gas of combustion furnace
Spray column 7 is imported by hot air duct 93.Scavenging air valve B92 is identical with the structure of scavenging air valve A91, and the course of work is on the contrary, herein
It repeats no more.
Finally it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations, although
Present invention has been described in detail with reference to the aforementioned embodiments, it will be understood by those of ordinary skill in the art that, still may be used
To modify to the technical solution recorded in previous embodiment or equivalent replacement of some of the technical features, and
These modifications or replacements, the spirit and model of technical solution of the embodiment of the present invention that it does not separate the essence of the corresponding technical solution
It encloses.
Claims (8)
1. a kind of biomass pyrolysis system, it is characterised in that：Including circulating-heating part, pyrolysis section and post-processing part；
The circulating-heating part includes combustion chamber, hotair chamber and fuel addition room；
The combustion chamber includes combustion furnace (11), is distributed on combustion furnace (11) inner wall insulating brick (12) is mounted on combustion furnace
(11) natural gas spraying gun (13) in, the burning bed (14) and feed device being fixed on combustion furnace (11) inner wall；
The hotair chamber includes swing bucket (21), four heating rooms (22) being fixed in swing bucket (21), be deposited in plus
Gitter brick (23) in hot cell (22), the left conduit (24) being fixed on swing bucket (21) top surface are fixed on swing bucket (21) top
Right conduit (25) on face, the left wind turbine (26) being connect with left conduit (24) free end are connect with right conduit (25) free end
Right wind turbine (27), the gyration gear ring (28) being fixed on swing bucket (21) side wall, the revolution being mounted on combustion furnace (11) top surface
Motor (29) and the swiveling gear (210) on turning motor (29) output shaft；
The swiveling gear (210) is engaged with gyration gear ring (28)；
The swing bucket (21) is mounted on combustion furnace (11) top surface；
The pyrolysis section includes pedestal (31), is symmetrically mounted on pedestal (31) bearing block (32) is located at bearing block (32)
On shaft (33), be symmetrically fixed in shaft (33) support ring (34), with support ring (34) rotation connection pyrolysis oven
(35), the reamer (36) that is fixed in shaft (33), is located at pyrolysis chamber at the pyrolysis chamber (37) being located on pyrolysis oven (35) outer wall
(37) hot-air input terminal (38) on, is located on pyrolysis chamber (37) the solid output end (39) being located on pyrolysis oven (35)
Hot-air output end (310) and the driving motor (311) being connect with shaft (33).
2. a kind of biomass pyrolysis system according to claim 1, it is characterised in that：The burning bed (14) tilts and sets
It sets；The burning bed (14) is arranged alternately on (11) two opposite side walls of combustion furnace.
3. a kind of biomass pyrolysis system according to claim 1, it is characterised in that：The combustion furnace (11) is equipped with row
Material system；The discharge system includes the rectangular aperture (41) being opened on combustion furnace (11) bottom surface, is fixed on rectangular aperture (41)
The slideway (42) of both sides, the baffle (43) being located on slideway (42) and the pushing meanss being connect with baffle (43).
4. a kind of biomass pyrolysis system according to claim 1, it is characterised in that：The feed device includes and burning
Baffle (52) and barrel (51) rotation connection of the barrel (51), circular array of stove (11) rotation connection in barrel (51)
Exhaust pipe (53), the rotary electric machine (54) being fixedly mounted on combustion furnace (11) and on rotary electric machine (54) output shaft
Driving wheel (55)；
The driving wheel (55) contacts with barrel (51)；
The barrel (51) and the junction of combustion furnace (11) are provided with stomata (56)；It is fixed with steel wire on the stomata (56)
(57)；It is provided with feed opening (58) on the steel wire (57)；
Barrel (51) is divided into multiple fan sections by the baffle (52)；The shape phase of the shape and fan section of the feed opening (58)
Together.
5. a kind of biomass pyrolysis system according to claim 1, it is characterised in that：On the top surface of the combustion furnace (11)
It is fixed with flow distribution plate (6).
6. a kind of biomass pyrolysis system according to claim 4, it is characterised in that：The free end of the exhaust pipe (53)
It is connect with hot-air input terminal (38).
7. a kind of biomass pyrolysis system according to claim 1, it is characterised in that：The post-processing section point includes spray
Tower (7) and pulverizer (8)；
The input terminal of the spray column (7) is connect with hot-air output end (310)；
The input terminal of the pulverizer (8) is connect with solid output end (39).
8. a kind of biomass pyrolysis system according to claim 1, it is characterised in that：Further include scavenging air valve A (91), ventilation
Valve B (92) and hot air duct (93)；
The scavenging air valve A (91) and scavenging air valve B (92) are all provided with there are three connecting pin；
The hot air duct (93) sets there are two input terminal and an output end；
First connecting pin of the scavenging air valve A (91) is connect with first input terminal of hot air duct (93), second company
It connects end to connect with left wind turbine (26), third connecting pin is open end；
First connecting pin of the scavenging air valve B (92) is connect with second input terminal of hot air duct (93), second company
It connects end to connect with right wind turbine (27), third connecting pin is open end；
The output end of the hot air duct (93) is connect with hot-air input terminal (37).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810328481.7A CN108546556B (en) | 2018-04-08 | 2018-04-08 | Biomass pyrolysis system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810328481.7A CN108546556B (en) | 2018-04-08 | 2018-04-08 | Biomass pyrolysis system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108546556A true CN108546556A (en) | 2018-09-18 |
| CN108546556B CN108546556B (en) | 2020-10-02 |
Family
ID=63514932
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810328481.7A Expired - Fee Related CN108546556B (en) | 2018-04-08 | 2018-04-08 | Biomass pyrolysis system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108546556B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4204728A1 (en) * | 1992-02-17 | 1993-08-19 | Siemens Ag | Self contained plant drum heating for prodn. of low temp. gas - by using heating gas obtd. from carbonisation gas, for economy and simple gas prepn. |
| CN1077266A (en) * | 1992-04-06 | 1993-10-13 | 吴正新·亚瑟 | Thermal conversion pyrolysis reactor system |
| CN1132521A (en) * | 1993-08-19 | 1996-10-02 | 西门子公司 | Thermal waste disposal plant and process for operating the same |
| EP1277825A1 (en) * | 2001-07-18 | 2003-01-22 | Institut Francais Du Petrole | Process and installation for the production of combustible gas from gas derived from the thermal conversion of a solid charge |
| CN101735839A (en) * | 2009-12-10 | 2010-06-16 | 胜利油田胜利动力机械集团有限公司 | Process and device for environmentally-friendly and energy-saving biomass carbonization |
| CN102250633A (en) * | 2011-06-16 | 2011-11-23 | 西安三瑞实业有限公司 | Method for improving quality of brown coal with externally heated rotary furnace |
| CN103045273A (en) * | 2012-10-31 | 2013-04-17 | 周鼎力 | Method and equipment for preparing fuel from household garbage for suppressing dioxin |
| US20160339488A1 (en) * | 2013-09-29 | 2016-11-24 | Pte. Ltd. | Method and device for anaerobic pyrolysis treatment of dead-of-disease livestock and municipal organic refuse |
-
2018
- 2018-04-08 CN CN201810328481.7A patent/CN108546556B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4204728A1 (en) * | 1992-02-17 | 1993-08-19 | Siemens Ag | Self contained plant drum heating for prodn. of low temp. gas - by using heating gas obtd. from carbonisation gas, for economy and simple gas prepn. |
| CN1077266A (en) * | 1992-04-06 | 1993-10-13 | 吴正新·亚瑟 | Thermal conversion pyrolysis reactor system |
| CN1132521A (en) * | 1993-08-19 | 1996-10-02 | 西门子公司 | Thermal waste disposal plant and process for operating the same |
| EP1277825A1 (en) * | 2001-07-18 | 2003-01-22 | Institut Francais Du Petrole | Process and installation for the production of combustible gas from gas derived from the thermal conversion of a solid charge |
| CN101735839A (en) * | 2009-12-10 | 2010-06-16 | 胜利油田胜利动力机械集团有限公司 | Process and device for environmentally-friendly and energy-saving biomass carbonization |
| CN102250633A (en) * | 2011-06-16 | 2011-11-23 | 西安三瑞实业有限公司 | Method for improving quality of brown coal with externally heated rotary furnace |
| CN103045273A (en) * | 2012-10-31 | 2013-04-17 | 周鼎力 | Method and equipment for preparing fuel from household garbage for suppressing dioxin |
| US20160339488A1 (en) * | 2013-09-29 | 2016-11-24 | Pte. Ltd. | Method and device for anaerobic pyrolysis treatment of dead-of-disease livestock and municipal organic refuse |
Non-Patent Citations (1)
| Title |
|---|
| 金湓等: "生物质与污水污泥共热解特性研究", 《可再生能源》 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108546556B (en) | 2020-10-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN200988831Y (en) | Biomass continuous pyrolytic furnace and continuous pyrolytic system | |
| CN102032553B (en) | Continuous rotary biomass pyrolytic charring and boiler heat supply integrated equipment | |
| CN204986974U (en) | Automatic rotatory deashing fires burning furnace | |
| CN109022005A (en) | A kind of continuous biomass charing device and production method | |
| CN201892206U (en) | Continuous rotary device integrating biomass pyrolysis and carbonization and boiler heating | |
| CN201626934U (en) | Laying type straw carbonization device | |
| CN110295063A (en) | A kind of hot charcoal co-generation system of biomass external heating and method | |
| CN203586190U (en) | Biomass burning device used for butt joint with boiler, heat exchanger and heat supply system | |
| CN103602340A (en) | Stirring type biomass carbonization furnace | |
| CN103773404A (en) | Combined-type poly-generation biomass rapid carbonization equipment and carbon making method thereof | |
| CN108546556A (en) | A kind of biomass pyrolysis system | |
| CN201890859U (en) | Rotary type continuous pyrolysis carbonizing furnace with inner heat pipe | |
| CN207958249U (en) | A kind of decoration garbage carbonization disposal system in parallel with sludge | |
| CN110257093A (en) | The control method of carbonization system in a kind of hot charcoal co-generation system of biomass external heating | |
| CN203602551U (en) | Stirring biomass carbonizing furnace | |
| CN206843398U (en) | A kind of sludge cooperates with innocuity disposal system with stalk | |
| CN202116507U (en) | Production system for double activated carbon | |
| CN108611108A (en) | A kind of biomass pyrolysis furnace and biomass pyrolysis system | |
| CN205619252U (en) | Biomass burning machine | |
| CN102627387A (en) | Sludge carbonization furnace | |
| CN114772596A (en) | Biochar pyrolysis activation device for repairing heavy metal agricultural land | |
| CN205026934U (en) | Wind -force ration pay -off type organic heat transfer material heater | |
| CN102358852A (en) | Production method for preparing agriculture and forestry plant wastes into biomass fuel lumps used for gas supply system through gasification | |
| CN207649323U (en) | A kind of drying system using biomass fuel | |
| CN102269511B (en) | Manioc waste residue drying device and device for manufacturing firewood bar and charcoal |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20201002 |