CN101671570A - Miniature movable type agricultural and forest biomass fast pyrolysis device - Google Patents
Miniature movable type agricultural and forest biomass fast pyrolysis device Download PDFInfo
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- CN101671570A CN101671570A CN200910170228A CN200910170228A CN101671570A CN 101671570 A CN101671570 A CN 101671570A CN 200910170228 A CN200910170228 A CN 200910170228A CN 200910170228 A CN200910170228 A CN 200910170228A CN 101671570 A CN101671570 A CN 101671570A
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
The invention discloses a miniature movable type agricultural and forest biomass fast pyrolysis device. The device comprises a traveling mechanism (25), a combustion furnace (18), a feeder (21), a fast pyrolysis reactor (22), a gas solid separator (23), a gas condenser (11), a non-condensable gas purifier (24), a fan (16), a gas buffer tank (17) and a gas preheater (19); the height of the fast pyrolysis reactor (22) can be adjusted, the device can be suitable for various agricultural and forest biomass raw materials, and the fluidization quality in the reactor is better due to the arrangementof an inverted-cone-shaped gas flow stabilizer in a top cover of the reactor; the non-condensable gas is taken as gas sources of spouting gas and fluidized gas and heat supply fuel, the entire deviceis simple in structure, small in volume and stable in running, can be hauled to the agricultural and forest biomass for production intensively and has lower production cost; the small-scale movable type operating mode also avoids the problem that the industrial enlargement of a fluid bed reactor is not easy; and the industrial production of agricultural and forest biomass fast pyrolysis is realized in a disguised form.
Description
Technical field
The present invention relates to a kind of miniature movable type agricultural and forest biomass fast pyrolysis device, belong to the agricultural-forestry biomass utilization, especially the recovery energy field.
Background technology
Agricultural and forest biomass fast pyrolysis is meant under the anoxybiotic condition, with the agricultural-forestry biomass Pintsch process is gas and solid carbon, the cracked gas that to remove solid carbon afterwards again cools off the process that obtains bio oil and non-condensable gases rapidly, its principal product is a bio oil, and by product is solid carbon and non-condensable gases.Agricultural and forest biomass fast pyrolysis must satisfy three primary conditions: medium thermo-cracking temperature (450～650
℃), higher biological particles temperature rise rate (10
2～10
4K/s) and short gas residence time (0.2～3s).
The agricultural-forestry biomass resource distribution relatively disperses, need carry out thermo-cracking from collecting and transport to factory vegetatively, and agricultural-forestry biomass---especially agricultural wastes (as stalk, rice husk etc.) energy density is low, therefore need to collect, transport, store the raw material supply of a large amount of raw materials when satisfying continuous production, and plant size is big more, it is big more that raw material is collected radius, and raw material is collected, trucking costs is high more.WIPO PCT patent (WO2006/117006A1) discloses a kind of mobile biomass pyrolysis installation, this device comprises biomass through pyrolysis unit and travel mechanism, can haul scattered biomass concentration point by tow tractor and carry out the thermo-cracking processing, having reduced raw material collects and transportation cost, but the pyrolysis reactor that this pyrolysis plant adopts is a kind of centrifugal ablation reactor, belong to the direct contact reactor of mechanical movement formula, be characterized in to use the raw material (2～6mm) of greater particle size, need not use heat-transfer medium and assist gas, but in its reactor moving parts is arranged, structure is relatively complicated, the moving parts of equipment breaks down easily under thermo-cracking high temperature, and working reliability and operation life are difficult to be guaranteed.Chinese invention patent (CN200510137.7) discloses a kind of mobile biomass liquefaction system, its equipment all can be delivered by transportation means such as automobiles, carry out biomass liquefying than being easier to transport scattered biomass concentration point to, can reduce raw material equally collects and trucking costs, but the reactor that this system adopts is the normal flow fluidized bed reactor, and need to dismantle, transport and reinstall debugging in new grown place when changeing factory, therefore changeing factory's cycle can be long.
Prior biological matter rapid pyrolysis reactor mainly contains fluidized bed reactor (mainly comprising fluidized-bed, spouted bed, circulating fluidized bed, spouted fluidized bed etc.) and mechanical movement formula reactor (mainly comprising rotation awl, moving-bed, vacuum bed, ablation reactor etc.), and wherein fluidized bed reactor is the main both at home and abroad at present agricultural and forest biomass fast pyrolysis reactor that adopts.Yet up to the present yet there are some problems in fluidized bed reactor, has the bed material problem that horizontal mixed effect is undesirable, heat transfer efficiency is not high such as the normal flow fluidized bed reactor; Spouted bed bioreactor is prone to problems such as dead band, fluctuation of service; Circulating fluidized bed needs the fluidal texture of additional designs bed material and the volume that seems is bigger, and its thermo-efficiency is lower when using on a large scale; Though spouted fluidized bed combines the advantage of spouted bed and fluidized-bed, but still need design spouted gas and fluidized gas air flue respectively, still need the spouted gas and the fluidized gas source of the gas that provide extra respectively, therefore also have device structure complexity, working cost problem of higher.Therefore we have applied for utility model patent (ZL 2007201519336), a kind of spouted fluidized bed bioreactor is disclosed, by the design of tabular air distribution plate, will be divided into spouted gas and fluidized gas by the gas of same source of the gas supply, structure of reactor is simplified; Simultaneously, this system uses the not condensable gases that produces behind the biomass through pyrolysis as described spouted gas and fluidized gas, has avoided using extra spouted gas and fluidized gas source of the gas, has reduced running cost.But yet there are some imperfection parts in this utility model, at first, owing to comprise impurity such as tar, powdered carbon in the not condensable gases that biomass through pyrolysis produces, so use the not condensable gases circulation after the cracking to cause the pipeline (comprising blower fan, valve, under meter etc.) of its process to stop up through regular meeting because of the alluvial of tar and powdered carbon as source of the gas, equipment continous-stable service ability is not good enough; Secondly, the extra source of the gas that not condensable gases after the use cracking replaces stability of flow causes the fluctuation of air-flow in the reactor easily as spouted gas and fluidized gas, and reactor fluidised form difficult quality is guaranteed, carry out to such an extent as to influence the continous-stable of heat scission reaction, the bio oil productive rate is lower.
In addition, the problem that prior art is amplified difficulty for the fluidized bed reactor industrialization also is not well solved, the production of difficult realization large-scale industrialization.
In the agricultural and forestry biomass fast pyrogenation process,, generally need regulate processing parameter (mainly comprising inlet amount, fluidizing gas velocity, bed material amount and thermo-cracking temperature etc.) according to feedstock property and reactor size in order to satisfy three primary conditions.Because the agricultural-forestry biomass resource is of a great variety, character is different, for raw material of different nature, same reactor is difficult to satisfy simultaneously by the adjusting processing parameter these three primary conditions of fast pyrolysis, and the bigger change of processing parameter also can influence the serviceability of other link of complete assembly, and therefore same set of fast pyrolysis device is difficult to be applicable to the fast pyrolysis of multiple different properties agricultural-forestry biomass raw material.If the reactor that adopts size to regulate at raw material of different nature, by conditioned reaction device size, be aided with the adjusting of processing parameter again, will be easy to satisfy three primary conditions of fast pyrolysis, thereby make complete assembly be applicable to plurality of raw materials.
Summary of the invention
At above-mentioned the deficiencies in the prior art, technical problem to be solved by this invention provides a kind of miniature movable type agricultural and forest biomass fast pyrolysis device, this device go for multiple agricultural-forestry biomass raw material, simple for structure, volume is little, stablely, convenient move, can the collecting and distributing kobold of various agricultural-forestry biomass resources live carry out fast pyrolysis production, production cost is lower.
For solving the problems of the technologies described above, technical scheme of the present invention is for being made of walking mechanism, roasting kiln and the feeder, rapid pyrolysis reactor, gas-solid separator, gas condenser, non-condensable gases refining plant, blower fan, gas buffer jar and the gas preheater that link to each other successively by pipeline:
The air outlet of described gas preheater links to each other with the inlet mouth of described rapid pyrolysis reactor bottom, described gas preheater heat transferring medium inlet links to each other with the exhanst gas outlet of described roasting kiln, and the combustion gases inlet of described roasting kiln links to each other with described gas buffer jar;
Described rapid pyrolysis reactor is small-sized spouted fluidized bed bioreactor, its internal diameter is between 0.1m～0.3m, total height is between 1.6m～2m, this rapid pyrolysis reactor is by the back taper inlet plenum, the middle part can change the straight tubular conversion zone and the reactor head of height and the tabular air distribution plate that is installed between back taper inlet plenum and the conversion zone is formed, back taper inlet plenum bottom is provided with inlet mouth, the middle part can change the straight tubular conversion zone of height and be made up of the straight tubular reaction tubes that is no less than a section, it is identical to select that as required one or more diameters are installed, highly different reaction tubess is to change the height of described rapid pyrolysis reactor; Reactor head central authorities are provided with pneumatic outlet, inside be provided with one with the co-axial back taper gas of this pneumatic outlet current stabilizer, cone angle is 90 °, cone bottom diameter and this pneumatic outlet diameter ratio are (1.2～1.5): 1, and the awl baseplane is (0.2～0.3) to the ratio of the distance of pneumatic outlet and rapid pyrolysis reactor total height: 1.Except that the described miscellaneous equipment that carries out the mechanism is installed on the described walking mechanism.
Advantage of the present invention and technique effect are:
1. the height of rapid pyrolysis reactor of the present invention can be regulated, be aided with the adjusting of processing parameter, this device goes for the fast pyrolysis of multiple different properties agricultural-forestry biomass raw material, and raw material can be various timber, bark, stalk, corn cob, rice husk and discarded wood-based plate etc.
2. reactor head of the present invention inside be provided with one with the co-axial back taper gas of pneumatic outlet current stabilizer, this gas current stabilizer can alleviate effectively in the rapid pyrolysis reactor that causes as spouted gas and fluidized gas owing to the extra source of the gas that uses not condensable gases after the cracking to replace stability of flow that airflow fluctuation is big, fluidization quality is difficult to guaranteed problem, help the continous-stable of fast pyrolysis reaction to carry out, improve the bio oil productive rate.
3. rapid pyrolysis reactor of the present invention is small-sized spouted fluidized bed bioreactor, and its internal diameter is between 0.1m～0.3m, and total height is between 1.6m～2m; Described tabular air distribution plate is made up of circular flat board and woven wire placed on it, this flat board is provided with spouted hole and fluidisation hole, spouted hole is positioned at dull and stereotyped center, its diameter is (0.3～0.5) with the ratio of the internal diameter of rapid pyrolysis reactor: 1, the fluidisation hole is along circumferentially being distributed in periphery, spouted hole, its diameter is (0.05～0.1) with the ratio of spouted bore dia: 1, total percentage of open area in spouted hole and fluidisation hole is (35%～55%), this steel wire mesh number is between 100 orders～180 orders, spouted hole of designing on the air distribution plate and fluidisation hole can be divided into the gas from same source of the gas spouted gas and fluidized gas, avoid being provided with respectively spouted gas and fluidizing agent passage, make this rapid pyrolysis reactor simple for structure, volume is little, there is not scale effect, but continuous and stable production.
4. feeder of the present invention is made up of hopper, air sealer and tremie pipe, air sealer is connected with a buncher, make feeder of the present invention when realizing the continous-stable charging, can also enter rapid pyrolysis reactor by feeder by secluding air, improve reaction stability, helped system's continuous and stable production.
5. gas-solid separator of the present invention is the two stage cyclone separator, and the bottom of every grade of cyclonic separator all is connected with collection charcoal case, can realize that hot pyrolysis gas and the effective of solid carbon separate.
6. gas condenser of the present invention top is provided with the liquid inlet, the bottom is provided with liquid exit, this liquid exit links to each other with this liquid inlet with hot tube heat exchanger by recycle pump successively, this hot tube heat exchanger is used for the bio oil cooling to condenser, as improvement of the present invention, this hot tube heat exchanger can link to each other with the raw material drying unit, with the heat in the recycle heat transferring medium, reduce system energy consumption, reduce production costs.
7. the present invention uses not the condensable gases refining plant that condensable gases is not purified, this device is become with the gas filter set by gas-liquid separator, this gas-liquid separator is centrifugal suspension separator, this gas filter is an electrostatic detarrer, by the not condensable gases that recycles is carried out purifying treatment, avoided the pipeline (comprising blower fan, valve, under meter etc.) of its process to stop up, guaranteed system's continuous and stable production because of the alluvial of tar and powdered carbon.
8. roasting kiln of the present invention is can mixed firing coal, the combination burner of combustion gas, the not condensable gases or the solid carbon of meat or all using system generations, not only realized the recycle of fast pyrolysis by product, and avoid using expensive thermals source such as microwave, electric energy, further reduce system energy consumption, reduce production costs.
9. gas preheater heat transferring medium outlet of the present invention links to each other with a smoke eliminator, to purify the flue gas of discharging, the flue gas compliance with environmental protection requirements that makes the discharge of this device on the one hand, on the other hand as improvement of the present invention, can reclaim the waste heat of discharging flue gas by described smoke eliminator, be used for links such as raw material drying, further reduce system energy consumption, reduce production costs.
10. the present invention has walking mechanism, this walking mechanism is by frame, haulage gear, wheel and leg are formed, haulage gear is fixed on the frame front end, wheel is fixed on the downside at frame front and rear portion, before each wheel, the frame downside of back both sides is separately installed with a leg, described leg is height-adjustable leg, described wheel all has drift stop, whole device can conveniently be hauled agricultural-forestry biomass resource concentration point and be carried out fast pyrolysis production, conservation is collected and trucking costs, reduce production costs, in addition, this small-scale mobile operation mode has also been avoided the fluidized bed reactor industrialization and has been amplified difficult problem, has in a disguised form realized the production of agricultural-forestry biomass resource fast pyrolysis large-scale industrialization.
Description of drawings
Fig. 1 is the schematic flow sheet of one embodiment of the present invention.
Fig. 2 is a certain section reaction tubes sectional view of rapid pyrolysis reactor of the present invention.
Fig. 3 is a rapid pyrolysis reactor top cover stereographic map-1 of the present invention.
Fig. 4 is a rapid pyrolysis reactor top cover stereographic map-2 of the present invention.
Fig. 5 is a structural arrangement vertical view of the present invention.
Fig. 6 is a structural arrangement front view of the present invention.
Among Fig. 1～Fig. 6, (1) is hopper, and (2) are air sealers, (3) be tremie pipe, (4) are bunchers, and (5) are the back taper inlet plenums, (6) be air distribution plate, (7) are conversion zones, and (8) are reactor heads, (9) be first step cyclonic separator, (10) are second stage cyclonic separators, and (11) are gas condensers, (12) be recycle pump, (13) be hot tube heat exchanger, (14) are centrifugal suspension separators, and (15) are electrostatic detarrers, (16) be blower fan, (17) be the gas buffer jar, (18) are roasting kilns, and (19) are gas preheaters, (20) be smoke eliminator, (21) be feeder, (22) be rapid pyrolysis reactor, (23) are gas-solid separators, and (24) are condensable gases refining plants not, (25) be walking mechanism, (26) be frame, (27) are legs, and (28) are wheels, (29) be haulage gear, (30) be collection charcoal case 1, (31) are collection charcoal casees 2, and (32) are back taper gas current stabilizers.
Embodiment
Below in conjunction with accompanying drawing, the present invention and working process thereof are described in further detail:
Shown in Fig. 1～4, feeder (21) is by hopper (1), air sealer (2) and tremie pipe (3) are formed, tremie pipe (3) lower end links to each other with the opening for feed of rapid pyrolysis reactor (22) bottom, the agricultural-forestry biomass raw material is sent into rapid pyrolysis reactor (22) thus and is carried out the fast pyrolysis reaction, air sealer (2) links to each other with a buncher (4), in order to regulate inlet amount, rapid pyrolysis reactor (22) is by bottom back taper inlet plenum (5), the middle part can change conversion zone (7) and the reactor head (8) of height and be installed in back taper inlet plenum (5) and conversion zone (7) between tabular air distribution plate (6) composition, its internal diameter is between 0.1m～0.3m, total height is between 1.6m～2m, back taper inlet plenum (5) bottom is provided with inlet mouth, the middle part can change the straight tubular conversion zone (7) of height and be made up of the straight tubular reaction tubes that is no less than a section, it is identical to select that as required one or more diameters are installed, highly different reaction tubess, to change the height of described rapid pyrolysis reactor (22), reactor head (8) central authorities are provided with pneumatic outlet, inside is provided with one and the co-axial back taper gas of this pneumatic outlet current stabilizer (32), cone angle is 90 °, cone bottom diameter and this pneumatic outlet diameter (1.2～1.5): 1, the awl baseplane is (0.2～0.3) to the ratio of the distance of pneumatic outlet and rapid pyrolysis reactor (22) total height: 1, tabular air distribution plate (6) is made up of circular flat board and woven wire placed on it, this flat board is provided with spouted hole and fluidisation hole, spouted hole is positioned at dull and stereotyped center, the ratio of the internal diameter of its diameter and rapid pyrolysis reactor (22) is (0.3～0.5): 1, the fluidisation hole is along circumferentially being distributed in periphery, spouted hole, its diameter is (0.05～0.1) with the ratio of spouted bore dia: 1, total percentage of open area in spouted hole and fluidisation hole is (35%～55%), this steel wire mesh number is between 100 orders～180 orders, agricultural-forestry biomass raw material fast pyrolysis in temperature is 500～650 ℃ rapid pyrolysis reactor (22) is gas and solid carbon, the air outlet of reactor head (8) links to each other with first step cyclonic separator (9) gas inlet, first step cyclonic separator (9) pneumatic outlet links to each other with second stage cyclonic separator (10) gas inlet, two stage cyclone separator bottom links to each other with collection charcoal case 2 (31) with collection charcoal case 1 (30) respectively, the solid carbon overwhelming majority that fast pyrolysis produces is separated collection charcoal case 1 (30) and the collection charcoal case 2 (31) of entering in this two stage cyclone separator, second stage cyclonic separator (10) pneumatic outlet links to each other with gas condenser (11) gas inlet, gas after the separate solid charcoal enters in the gas condenser (11) by rapid condensation, obtain bio oil and non-condensable gases, the outlet of gas condenser (11) lower liquid links to each other with hot tube heat exchanger (13) liquid inlet by recycle pump (12), hot tube heat exchanger (13) liquid exit links to each other with gas condenser (11) liquid inlet, top, bio oil is being lowered the temperature by this recycle pump (12) and this hot tube heat exchanger (13) circulation time, gas condenser (11) pneumatic outlet links to each other with the gas inlet of centrifugal suspension separator (14), the liquid exit of centrifugal suspension separator (14) links to each other with gas condenser (11) lower liquid inlet, centrifugal suspension separator (14) pneumatic outlet is caught the device inlet with static tar and is linked to each other, condensable gases is not taken off contained liquid through centrifugal suspension separator (14), the liquid return of deviating from is in gas condenser (11), entering static tar through the not condensable gases of suspension separator (14) catches in the device and filters, electrostatic detarrer (15) outlet links to each other with blower fan (16) inlet, blower fan (16) outlet links to each other with gas buffer jar (17) inlet, gas buffer jar (17) outlet 1 links to each other with gas preheater (19) inlet, gas preheater (19) outlet links to each other with the inlet mouth of back taper inlet plenum (5) bottom, gas buffer jar (17) outlet 2 links to each other with the mixed combustion furnace gas fuel inlet, the mixed combustion furnace exhanst gas outlet links to each other with gas preheater (19) heat transferring medium inlet, the outlet of gas preheater (19) heat transferring medium links to each other with flue gas cleaner (20), condensable gases does not enter gas buffer jar (17) afterwards through blower fan (16), entering rapid pyrolysis reactor (22) after partly condensable gases heats up by gas preheater (19) afterwards circulates as spouted gas and fluidized gas, all the other not solid fuel such as condensable gases and other subsidiary product of thermal cracking solid carbon and coal enter roasting kiln (18) burning, the high-temperature flue gas that burning produces enters gas preheater (19) as thermal medium and carries out heat exchange, and the weary flue gas of eluting gas preheater (19) enters emptying after flue gas cleaner (20) purifying treatment.
As Fig. 5～shown in Figure 6, the miscellaneous equipment of the present invention except that carrying out mechanism (25) is installed on the described walking mechanism (25), this walking mechanism (25) is by frame (26), haulage gear (29), wheel (28) and leg (27) are formed, haulage gear (29) is fixed on frame (26) front end, wheel (28) is fixed on the downside of frame (26) front and rear, preceding at each wheel (28), the frame of back both sides (26) downside is separately installed with a leg (27), described leg (27) is height-adjustable leg (27), described wheel (28) all has drift stop, and whole device can conveniently be hauled agricultural-forestry biomass resource concentration point and be carried out fast pyrolysis production
Embodiment:
With the larchwood is raw material, utilizes treatment capacity to carry out fast pyrolysis production for the miniature movable type agricultural and forest biomass fast pyrolysis device of 30Kg/h:
This device structure is by feeder (21), rapid pyrolysis reactor (22), gas-solid separator (23), gas condenser (11), condensable gases refining plant (24) not, blower fan (16), gas buffer jar (17), gas preheater (19), roasting kiln (18) and walking mechanism (25) constitute, rapid pyrolysis reactor (22) internal diameter 0.16m wherein, total height 1.6m, the conversion zone (7) of rapid pyrolysis reactor (22) is made up of the two-stage reaction pipe that highly is respectively 0.4m and 0.6m, reactor head (8) pneumatic outlet diameter 32mm, the cone bottom diameter 40mm of inner set back taper gas current stabilizer (32), cone angle is 90 °, the awl baseplane is 0.32m to the distance of this pneumatic outlet, air distribution plate (6) is gone up spouted bore dia 56mm, fluidisation bore dia 3mm, total percentage of open area is 35%, and the steel wire mesh number on the air distribution plate (6) is 120 orders.
When the device operation is produced, at first open roasting kiln (18), open blower fan (16) operation gas-circulating system, setting Heating temperature is 560 ℃, and spouted gas and fluidizing agent total flux are 25m
3/ h; ON cycle pump (12) operation condenser system; Open feeder buncher (4) when rapid pyrolysis reactor (22) temperature is 500 ℃ of left and right sides and begin slow charging, and strengthen inlet amount gradually according to reactor intensification situation, treat that temperature-stable back about 560 ℃ adjusts buncher (4) rotating speed and make inlet amount be stabilized in 30Kg/h; Valve on adjustments of gas surge tank (17) outlet 1 pipeline makes the not condensable gases stability of flow that enters rapid pyrolysis reactor (22) at 25m
3/ h, all the other not condensable gases enter roasting kiln (18) burning; Solid carbon in timely collection collection charcoal case 1 (30), the collection charcoal case 2 (31) and the bio oil in the gas condenser (11); Viewing system temperature, flow, pressure and other parameters, the good operation of assurance device; Reaction is closed roasting kiln (18) after finishing, and blower fan (16) and gas condenser (11) work on, and after rapid pyrolysis reactor (22) temperature drops to 150 ℃, close blower fan (16) and recycle pump (12), end-of-job.
Claims (10)
1. miniature movable type agricultural and forest biomass fast pyrolysis device is characterized in that this device is by walking mechanism (25), roasting kiln (18) and the feeder (21) that links to each other successively by pipeline, rapid pyrolysis reactor (22), gas-solid separator (23), gas condenser (11), condensable gases refining plant (24), blower fan (16), gas buffer jar (17) and gas preheater (19) formation:
The air outlet of described gas preheater (19) links to each other with the inlet mouth of described rapid pyrolysis reactor (22) bottom, described gas preheater (19) heat transferring medium inlet links to each other with the exhanst gas outlet of described roasting kiln (18), and the combustion gases inlet of described roasting kiln (18) links to each other with described gas buffer jar (17);
Described rapid pyrolysis reactor (22) is small-sized spouted fluidized bed bioreactor, its internal diameter is between 0.1m～0.3m, total height is between 1.6m～2m, this rapid pyrolysis reactor (22) is by bottom back taper inlet plenum (5), the middle part can change straight tubular conversion zone (7) and the reactor head (8) of height and be installed in back taper inlet plenum (5) and conversion zone (7) between tabular air distribution plate (6) composition, back taper inlet plenum (5) bottom is provided with inlet mouth, the middle part can change the straight tubular conversion zone (7) of height and be made up of the straight tubular reaction tubes that is no less than a section, it is identical to select that as required one or more diameters are installed, highly different reaction tubess is to change the height of described rapid pyrolysis reactor (22);
Described reactor head (8) central authorities are provided with pneumatic outlet, inside be provided with one with the co-axial back taper gas of this pneumatic outlet current stabilizer (32), cone angle is 90 °, cone bottom diameter and this pneumatic outlet diameter ratio are (1.2～1.5): 1, and the awl baseplane is (0.2～0.3) to the ratio of the distance of pneumatic outlet and rapid pyrolysis reactor (22) total height: 1.
Except that the described miscellaneous equipment that carries out the mechanism (25) is installed on the described walking mechanism (25).
2. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1, it is characterized in that described tabular air distribution plate (6) is made up of circular dull and stereotyped and woven wire placed on it, this flat board is provided with spouted hole and fluidisation hole, spouted hole is positioned at dull and stereotyped center, its diameter is (0.3～0.5) with the ratio of the internal diameter of thermo-cracking rapid pyrolysis reactor: 1, the fluidisation hole is along circumferentially being distributed on the flat board, its diameter is (0.05～0.1) with the ratio of spouted bore dia: 1, total percentage of open area in spouted hole and fluidisation hole is (35%～55%), and this steel wire mesh number is between 100 orders～180 orders.
3. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1 is characterized in that described feeder (21) is made up of hopper (1), air sealer (2) and tremie pipe (3), and air sealer (2) is connected with a buncher (4).
4. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1 is characterized in that described gas-solid separator (23) is a two-stage level cyclonic separator, and the bottom of every grade of cyclonic separator all is connected with collection charcoal case.
5. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1, it is characterized in that described gas condenser (11) top is provided with the liquid inlet, the bottom is provided with liquid exit, this liquid exit links to each other with this liquid inlet with hot tube heat exchanger (13) by recycle pump (12) successively.
6. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1, it is characterized in that described not condensable gases refining plant (24) is become with the gas filter set by gas-liquid separator, this gas-liquid separator is a centrifugal suspension separator (14), and this gas filter is electrostatic detarrer (15).
7. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1, it is characterized in that described roasting kiln (18) for can mixed firing coal, the combination burner of combustion gas, meat or whole not condensable gases or solid carbon of producing of using system.
8. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1 is characterized in that described gas preheater (19) links to each other with a smoke eliminator (20) in the heat transferring medium outlet, to purify the flue gas of discharging.
9. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 1, it is characterized in that described walking mechanism (25) is made up of frame (26), haulage gear (29), wheel (28) and leg (27), haulage gear (29) is fixed on frame (26) front end, wheel (28) is fixed on the downside of frame (26) front and rear, and frame (26) downside in the forward and backward both sides of each wheel (28) is separately installed with a leg (27).
10. miniature movable type agricultural and forest biomass fast pyrolysis device as claimed in claim 9 is characterized in that described leg (27) is height-adjustable leg, and described wheel (28) all has drift stop.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101702284A CN101671570B (en) | 2009-09-08 | 2009-09-08 | Miniature movable type agricultural and forest biomass fast pyrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101702284A CN101671570B (en) | 2009-09-08 | 2009-09-08 | Miniature movable type agricultural and forest biomass fast pyrolysis device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101671570A true CN101671570A (en) | 2010-03-17 |
| CN101671570B CN101671570B (en) | 2012-08-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2009101702284A Expired - Fee Related CN101671570B (en) | 2009-09-08 | 2009-09-08 | Miniature movable type agricultural and forest biomass fast pyrolysis device |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101955786A (en) * | 2010-09-17 | 2011-01-26 | 北京林业大学 | Device for preparing bio-oil from waste manmade boards by thermochemical clean conversion |
| CN102719265A (en) * | 2012-06-18 | 2012-10-10 | 天津大学 | Solid waste or biomass high-efficiency pyrolysis oil-producing system |
| CN103031136A (en) * | 2012-12-27 | 2013-04-10 | 北京林业大学 | Pyrolysis poly-generation comprehensive utilization method for waste artificial board |
| CN103666514A (en) * | 2013-11-22 | 2014-03-26 | 胥利先 | Method for on-line catalytic cracking of biomass through gushing bed-revolving bed two-step method |
| CN104560074A (en) * | 2013-10-22 | 2015-04-29 | 中国石油化工股份有限公司 | System for preparing bio-oil and activated carbon by microwave pyrolysis |
| CN106244179A (en) * | 2016-08-29 | 2016-12-21 | 上海交通大学 | Packaged type biomass catalyzing pyrolysis reaction device |
| CN106590706A (en) * | 2016-12-21 | 2017-04-26 | 北京林业大学 | Vehicle-mounted biomass pyrolysis liquefaction system |
| CN110332531A (en) * | 2019-06-01 | 2019-10-15 | 中山市思源电器有限公司 | A kind of gas burner that auxiliary air air ducting is set |
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| CN1215146C (en) * | 2002-11-08 | 2005-08-17 | 华东理工大学 | Fast biomass-cracking process of preparing liquid fuel |
| CN100340637C (en) * | 2005-12-31 | 2007-10-03 | 华中科技大学 | Mobile biomass liquefaction system |
| CN101486918A (en) * | 2009-02-17 | 2009-07-22 | 北京海润川投资咨询有限公司 | Novel spouted circulating fluid bed timber rapid pyrolysis apparatus and technological process |
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2009
- 2009-09-08 CN CN2009101702284A patent/CN101671570B/en not_active Expired - Fee Related
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101955786A (en) * | 2010-09-17 | 2011-01-26 | 北京林业大学 | Device for preparing bio-oil from waste manmade boards by thermochemical clean conversion |
| CN101955786B (en) * | 2010-09-17 | 2013-02-27 | 北京林业大学 | Device for preparing bio-oil from waste manmade boards by thermochemical clean conversion |
| CN102719265A (en) * | 2012-06-18 | 2012-10-10 | 天津大学 | Solid waste or biomass high-efficiency pyrolysis oil-producing system |
| CN102719265B (en) * | 2012-06-18 | 2014-06-25 | 天津大学 | Solid waste or biomass high-efficiency pyrolysis oil-producing system |
| CN103031136A (en) * | 2012-12-27 | 2013-04-10 | 北京林业大学 | Pyrolysis poly-generation comprehensive utilization method for waste artificial board |
| CN104560074A (en) * | 2013-10-22 | 2015-04-29 | 中国石油化工股份有限公司 | System for preparing bio-oil and activated carbon by microwave pyrolysis |
| CN104560074B (en) * | 2013-10-22 | 2017-03-01 | 中国石油化工股份有限公司 | A kind of microwave-heating bio oil and the system of activated carbon |
| CN103666514A (en) * | 2013-11-22 | 2014-03-26 | 胥利先 | Method for on-line catalytic cracking of biomass through gushing bed-revolving bed two-step method |
| CN106244179A (en) * | 2016-08-29 | 2016-12-21 | 上海交通大学 | Packaged type biomass catalyzing pyrolysis reaction device |
| CN106590706A (en) * | 2016-12-21 | 2017-04-26 | 北京林业大学 | Vehicle-mounted biomass pyrolysis liquefaction system |
| CN110332531A (en) * | 2019-06-01 | 2019-10-15 | 中山市思源电器有限公司 | A kind of gas burner that auxiliary air air ducting is set |
| CN110332531B (en) * | 2019-06-01 | 2021-02-02 | 中山市思源电器有限公司 | Gas burner with secondary air guide device |
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