CN109825319A - A kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments - Google Patents
A kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments Download PDFInfo
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- CN109825319A CN109825319A CN201910096157.1A CN201910096157A CN109825319A CN 109825319 A CN109825319 A CN 109825319A CN 201910096157 A CN201910096157 A CN 201910096157A CN 109825319 A CN109825319 A CN 109825319A
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- 241000208125 Nicotiana Species 0.000 title claims abstract description 72
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 72
- 239000002028 Biomass Substances 0.000 title claims abstract description 43
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 75
- 239000000463 material Substances 0.000 claims abstract description 34
- 238000004519 manufacturing process Methods 0.000 claims abstract description 26
- 238000002485 combustion reaction Methods 0.000 claims abstract description 21
- 230000001413 cellular effect Effects 0.000 claims abstract description 16
- 238000001035 drying Methods 0.000 claims abstract description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000003546 flue gas Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 10
- 239000000567 combustion gas Substances 0.000 claims abstract description 8
- 238000007599 discharging Methods 0.000 claims abstract description 3
- 238000010438 heat treatment Methods 0.000 claims description 14
- 238000000926 separation method Methods 0.000 claims description 14
- 239000003610 charcoal Substances 0.000 claims description 11
- 239000002737 fuel gas Substances 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 241000196324 Embryophyta Species 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 3
- 238000013461 design Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 230000002459 sustained effect Effects 0.000 claims description 3
- 235000021419 vinegar Nutrition 0.000 claims description 3
- 239000000052 vinegar Substances 0.000 claims description 3
- 239000002023 wood Substances 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 2
- 238000000746 purification Methods 0.000 abstract description 4
- 230000006641 stabilisation Effects 0.000 abstract 1
- 238000011105 stabilization Methods 0.000 abstract 1
- 235000019504 cigarettes Nutrition 0.000 description 11
- 230000007613 environmental effect Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 238000004939 coking Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000010815 organic waste Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 244000144985 peep Species 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 206010044565 Tremor Diseases 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- -1 stalk Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002918 waste heat Substances 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
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
A kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments, it is provided with multiple dedicated retorts of biomass flue-cured tobacco, the feed inlet of the discharging connection retort of dryer, retort is provided with cellular burner, the flue gas that the charing of retort material generates enters level-one, second level oil, gas separating device by flue, the gas outlet connection shell and tube condenser of oil, gas separating device, the output end of shell and tube condenser connects air accumulator, combustion gas a part in air accumulator is sent to burner, and it is hothouse baking tobacco leaf that the flame generated after lighting, which enters intensive baking room special hot air stove,；Another part is sent to direct combustion hotblast stove, provides heat source for drying machine drying material.The burning capacity density of carbonated gas is greatly improved by processes such as specific purification, purifications in the present invention, has ensured continuous, the stabilization of hot wind during flue-cured tobacco.Production cost is greatly reduced, remarkable benefit improves.
Description
Technical field
The present invention relates to a kind of flue-cured tobacco complete set of equipments, especially a kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments.
Background technique
China generates the agricultural abandoned biomass such as a large amount of stalk, shell class, core class, branch class every year, however due to lacking
Simple and effective comprehensive treatment equipment and measure, these flood tide agriculture and forestry organic waste materials mostly " are committed to the flames " or " wilderness lost ", no
The serious wasting of resources is only caused, and produces serious environmental pollution.Agricultural abandoned biomass circulation, environmentally friendly, efficient benefit
With being always China's agricultural and severe challenge and major issue that environment sustainable development faces.
Tobacco is one of most important industrial crops in China, and cultivated area and yield occupy first place in the world.China tobacco money
Source distribution is extensive, and Yunnan, Henan, Shandong, Gansu, Guizhou, Hunan are the important flue-cured tobacco places of production in China.Wherein, Yunnan, Guizhou,
Cultivated area maximum, the yield highest in Henan, Hunan Province, tobacco planting area and total output have accounted for 60% or so of the whole nation.So
And since tobacco planting administrative skill and production structure adjustment for a long time are more extensive, complete picking and purchase tobacco leaf is appointed
After business, a large amount of remaining cigarette straw wastes of generation are largely burned or are abandoned in field, and on the one hand a large amount of cigarette stalk resources are wasted,
On the other hand serious environmental pollution is also resulted in.Since the content of lignin of cigarette stalk is high, poor fluidity, especially in charing or
The problems such as tar content that gasification generates is high, a large amount of cigarette stalk resource becomes restriction still without being utilized effectively so far
An important factor for sustainable production of tobacco and tobacco grower's increasing both production and income.
Tobacco Leaf Curing is one of most important link of tobacco leaf production, directly determines tobacco leaf finished product quality and quantity.
Traditional tobacco flue-curing is mostly based on fire coal, tobacco flue-curing house in the form of coal-fired, according to incompletely statistics ten thousand more than 400, these
Tobacco flue-curing house energy consumption is high, system thermal efficiency is low, generates a large amount of carbon emissions in process of production, causes serious atmospheric pollution, and close
Coal price goes up over year, directly increases leaf tobacco production cost, and the small coal mine for not meeting environmental regulations is then taken by country completely
It forms.It uses using electric power as heat source, production cost is higher, especially in case of exceptional circumstances, has a power failure easily in high-temperature baking
A large amount of tobacco leaves are caused to rot, extreme influence quality of tobacco.And using biomass as heat source, in processing, production process
Electric power energy consumption is big, and high production cost, tobacco grower is often beyond affordability, especially easily generates coking problem during processing, is difficult
Be effectively addressed, equipment can not continuous, stable operation, lead to that the production cost increases, production efficiency reduces.
Combustion gas and charcoal flue-cured tobacco of the present invention using the generation of biomass carbonated process, completely instead of traditional energy flue-cured tobacco
Mode solves the generally existing carbon emission increase of traditional flue-cured tobacco, smoke pollution, pipeline coking and gas outlet amount is small, heat source
The technical problems such as shakiness change traditional flue-cured tobacco mode.The equipment is not necessarily to extra power heat supply, realizes self-produced confession, substantially
Degree improves production efficiency, reduces production cost, breaches technical problem associated with biomass carbon, gas, by agricultural such as cigarette stalks
Waste is turned waste into wealth, and " low-carbon, environmental protection, green " flue-cured tobacco is realized, and solves agricultural abandoned biomass circulation, efficient, synthesis benefit
With problem, promote tobacco leaf production low-carbon, environmental protection, low-cost high-efficiency.
Summary of the invention
To solve the above problems, the present invention proposes a kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments, it is roasting to change tradition
Cigarette mode reduces carbon emission amount, smoke pollution, reduces pipeline coking, improves gas outlet amount and heat source stability, significantly mentions
High efficiency reduces production cost, the agriculture and forestry organic waste materials such as cigarette stalk is turned waste into wealth, and realizes " low-carbon, environmental protection, green " flue-cured tobacco,
Agricultural abandoned biomass circulation, efficient, problem of complex utilization are solved, tobacco leaf production low-carbon, environmental protection, low-cost high-efficiency are promoted.
The purpose of the present invention is what is be achieved through the following technical solutions: including charging and discharging conveyer, dryer, deduster,
The dedicated retort of biomass flue-cured tobacco, gas and oil separating plant, shell and tube condenser, moisture separator, air accumulator, special hot air stove,
Tobacco dense type barn, direct-fired fuel gas hot-blast stove；It is characterized in that: the dedicated retort of more than two biomass flue-cured tobaccos is arranged, dry
The feed inlet of the outfeed belt conveyor tail end connection dedicated retort of biomass flue-cured tobacco of dry machine, the dedicated charing furnace bottom of biomass flue-cured tobacco
Carbon outleting port is set；A cellular burner, the charing of retort material is arranged in biomass flue-cured tobacco dedicated retort material char zone
The flue gas of generation enters burner internal by the way that cellular burner surface is porous, then passes through connection below cellular burner
Flue exports outside retort, primary oil, gas separating device into gas and oil separating plant；The level-one of oil, air separation
Oil, gas separating device gas outlet by flue connect second level oil, gas separating device air inlet, second level oil, gas separating device out
Port connects shell and tube condenser by sharing flue gas pipeline, and the output end of shell and tube condenser connects gas storage by air-introduced machine
Tank, the combustion gas in air accumulator are sent to burner through gas pipeline by control valve a part, the flame generated after lighting into
Entering intensive baking room special hot air stove is hothouse baking tobacco leaf；Another part connects direct-fired heat through gas pipeline by control valve
Wind furnace, direct combustion hotblast stove air outlet connect dryer air inlet, provide heat source for drying machine drying material.
A cellular burner is respectively set in the furnace body of the above-mentioned dedicated retort of biomass flue-cured tobacco, the burner is specific
Structure is cage enclosed construction, is made of heat-resistance stainless steel plate；The flue gas that the charing of retort material generates passes through cellular combustion
The design of burner porous surface enters burner internal.
Above-mentioned primary oil, gas separating device are common apparatus.
The interior setting of cabinet of above-mentioned second level oil, gas separating device is constituted detour and is led to by two upper feature boards and a lower feature board
The level-one on road is to level Four process chamber；At the top of the box body, swivel nozzle is set positioned at the top of second level to tertiary treatment room, is used for
It sprays wood vinegar and hot water mixing carries out secondary, oily, gas separation three times；Oil sump tank is set in the bottom of box, oil sump tank bottom is set
Put oilhole.
Above-mentioned intensive baking room special hot air stove specific structure be box sealing structure, hot-blast stove be arranged fuel gas inlet and
Burner is arranged in hot-blast outlet, fuel gas inlet, and multiple pipe heater outsides are arranged inside hot-blast stove, and the combustion space connection of burner is outer
Multiple interior heating tubes are arranged with pipe heater outside vertical direction in heating tube, connect side combusion chamber, side burning at the both ends of interior heating tube
Room is connected to end combustion chamber.The hot-blast stove uses sustained combustion mode, firstly, gas pipeline is delivered to burning below hot-blast stove
The combustible gas of device is lighted, the flame after lighting enter hot-blast stove pipe heater outside region heating, flame pass through again external heat region into
Enter interior heating region and heat interior heating tube, last flame enters hot-blast stove two sides and end combustion chamber.To realize and improve thermal energy
Stability meets the technical requirements of flue-cured tobacco.
The positive effect of the present invention:
1, the burning capacity density of carbonated gas, combustible gas is greatly improved by processes such as specific purification, purifications in this equipment
In nitrogen gas component reduce by 90% or more.
2, the present invention needs to design according to intensive flue-cured tobacco production, and carbon yield and fuel gases calorific value are high, and gas supply is continuous, stablizes,
Ensured hot wind during flue-cured tobacco it is continuous, stablize.
3, oil, gas separating device use multistep treatment room tar collector, thoroughly solve it is biomass carbonated during
Charing production efficiency is greatly improved in the coking problem of generation.
4, using part biological matter carbonated gas, the drying self-produced confession of heat source is realized, instead of traditional coal-fired heat source material
Drying mode, realizing biomass material water content can normally be carbonized below 40%, and other biological matter gas or charcoal
Change mostly 16% hereinafter, production cost is greatly reduced, remarkable benefit improves.
5, the equipment is widely used in the different types agricultural abandoned biomass such as stalk, shell class, core class, branch class, improves
Biomass Energy Utilization efficiency is suitable for discarded cigarette stalk processing, turns waste into wealth, it can be achieved that cigarette stalk resource " environmentally friendly, efficient " circulation benefit
With raw material production cost is greatly reduced, and comprehensive productivity effect significantly improves.Low-carbon, environmental protection, green flue-cured tobacco are realized, agriculture is solved
Woods abandoned biomass circulation, efficient, problem of complex utilization.
6, flue-cured tobacco and raw material stoving efficiently are solved the problems, such as using charing waste heat, is not necessarily to external heat source, realized and originate from certainly
For breaching technical problem associated with biomass carbon, gas.
7, the complete special equipment is simple, easy, at low cost, can large-scale promotion application, breach traditional flue-cured tobacco equipment,
Technology, technique bottleneck, low-carbon, cleaning, environmental protection, production cost is effectively reduced, production efficiency increases substantially, increase income for tobacco grower and
Low-carbon, green flue-cured tobacco open a new way.
Detailed description of the invention
Fig. 1: complete set of equipments schematic diagram of the invention.
Fig. 2: the dedicated retort schematic diagram of biomass flue-cured tobacco.
Fig. 3: cellular burner schematic diagram.
Fig. 4: I and II oil, gas separating device schematic diagram.
Fig. 5: intensive baking room special hot air stove schematic diagram.
Fig. 6: Fig. 5 A-A cross-sectional view.
Specific embodiment
See that Fig. 1, particular content of the invention are as follows: charing material be cigarette stalk and agriculture and forestry organic waste material, 3-5 centimeters of specification.It dries
Dry machine 21 uses J16 dryer, and feeding conveyor 16 uses 50 belt conveyors, and material is delivered to drying by feeding conveyor 16
The feeding inlet of machine, the discharge outlet connection XLG type cyclone dust collector 19 and air-introduced machine 20 of dryer；During drying materials
Grit carries out dust processing through XLG type cyclone dust collector by air-introduced machine.Outfeed belt conveyor 18 is arranged in the discharge port of dryer,
Outfeed belt conveyor 18 uses 50 belt conveyors；See Fig. 1,2, the dedicated retort 2 of two biomass flue-cured tobaccos is set, dryer goes out
Material conveyer tail end connects the feed inlet 2-1 of the dedicated retort 2 of two biomass flue-cured tobaccos, two dedicated retorts of biomass flue-cured tobacco
Furnace wall 2-2 on 11 peep hole 2-6, fire hole 2-7 and flue 2-4, two dedicated retorts of biomass flue-cured tobacco are set
The carbon outleting port 2-5 and pedestal 2-9 of charcoal is respectively set out in bottom；Screw conveyor 2-8 is set in carbon outleting port 2-5, through spiral transferring
It send machine to go out charcoal by carbon outleting port, flood dragon type conveyer 17 is set outside carbon outleting port, with this outside transporting biological charcoal；Two biomass flue-cured tobaccos
A cellular burner 2-3 is respectively set in dedicated retort material char zone, sees Fig. 3, which is cage
Enclosed construction is made of heat-resistance stainless steel plate, is fixed in retort by fixed frame 25；Material after drying passes through pan feeding
Mouth enters in retort, lights material by material fire hole 2-7, passes through cellular burner 2-3 and supplies oxygen；Each biomass is roasting
The dedicated retort of cigarette is respectively equipped with 14 temperature monitoring points, connects external control room, material in real-time monitoring furnace by data line
Charing situation.Simultaneously by peep hole 2-6, for observing material charing situation in retort and adjusting.
The flue gas that the charing of retort material generates enters burner internal by the way that cellular burner surface is porous.Pass through again
Outside the flue 2-4 output retort connected below cellular burner, sees Fig. 4, oil gas point is entered by air inlet 3-2
Primary oil, gas separating device 3 from device；Primary oil, gas separating device use existing common apparatus, in primary oil, gas separating device 3
Assemble umbrella-type purifying processor 3-1；Primary oil, 3 gas outlet of gas separating device connect second level oil, gas separating device 15 by flue
Air inlet；
See Fig. 4, the interior setting of cabinet of second level oil, gas separating device 15 is by two upper feature board 15-2 and a lower feature board 15-3 structure
At the level-one of alternate path to level Four process chamber A, B, C, D, each feature board is fixed in cabinet by support rod 15-1；In second level
The bottom of box setting oil sump tank 15-4 of oil, gas separating device 15, for collecting oil liquid 15-5；Drain oil is arranged in oil sump tank bottom
Overflow valve 15-10 is arranged on side wall by 15-6；Pass through connection pin shaft 15-7 and connection bolt 15-8 and nut on the side wall of oil sump tank
It is assembled on the connecting plate 15-9 of second level oil, 15 cabinet of gas separating device.One is fixed on cabinet.In second level oil, gas separating device
Swivel nozzle 16 is arranged positioned at the top of second level to tertiary treatment room B, C, for spraying wood vinegar and 70 DEG C in 15 top of the box
The above hot water mixing carries out secondary, oily, gas separation three times.
See Fig. 1, two second level oil, gas separating device 15 gas outlet pass through and share flue gas pipeline 14 and connect shell and tube condenser
12 use the prior art with water tank 13, shell and tube condenser 12；The output end of shell and tube condenser 12 concatenates an aqueous vapor separation
Device 4, secondary moisture separator 5 and air-introduced machine 11, moisture separator use WSD80 moisture separator.Realize the combustion of aqueous vapor separation
Gas connects air accumulator 7 by air-introduced machine, and a part is sent to by the combustion gas in air accumulator 7 by control valve through gas pipeline 8
The burner of hot-blast stove 9, the flame generated after lighting enter special hot air stove 9, so for intensive baking room 10 provide hot wind into
Row baking tobacco leaves；
See that Fig. 5-6, the specific structure of special hot air stove 9 are box sealing structure, hot-blast stove setting fuel gas inlet 9-1 and hot wind go out
Burner 9-2 is arranged in mouth 9-5, fuel gas inlet, and multiple pipe heater outside 9-6 are arranged inside hot-blast stove, and the combustion space of burner connects
Multiple interior heating tube 9-7 are arranged with pipe heater outside 9-6 vertical direction in logical pipe heater outside 9-6, connect at the both ends of interior heating tube 9-7
Side combusion chamber 9-3 is met, side combusion chamber 9-3 is connected to end combustion chamber 9-4.The hot-blast stove uses sustained combustion mode, firstly, will combustion
Feed channel is delivered to 9 lower section burner of hot-blast stove, and combustion gas is lighted, and the flame after lighting enters hot-blast stove pipe heater outside region and adds
Heat, flame pass through external heat region again and heat interior heating tube into interior heating region, and last flame enters hot-blast stove two sides and end
End burning room.To realize that improving thermal energy stablizes；Another part connects the direct-fired heat of DC-Q through gas pipeline 1 by control valve
Wind furnace 23(is shown in Fig. 1), 23 air outlet of direct combustion hotblast stove connects 21 air inlet of dryer, provides heat for 21 material drying of dryer
Wind.
The course of work:
1, drying materials
Shove charge material requirement water content is 16% hereinafter, its laggard furnace material moisture can be lower than 40% for the first time, and material is through conveying
Machine is sent to the feeding inlet of dryer, inputs hot wind from direct combustion hotblast stove to dryer, dries to material.
2, multistage oil-gas separation is carbonized
Material after drying is transmitted to biomass carbonizing furnace through conveyer and is carbonized after dust removal machine dedusting.This process is main
Output charcoal and flue gas, wherein the charcoal of output goes out charcoal through carbon outleting port；The flue gas of generation then by flue be delivered to oil,
Air separation, carries out firsts and seconds oil, gas separation, and the flue gas after separation enters shell and tube condenser through flue, passes through
Shell and tube condenser carry out three-level oil, gas separation, oil, gas separation after combustion gas after water, gas separating device are purified, are purified,
Air accumulator is delivered to by air-introduced machine guidance.
3, biological fuel gas heat supply-intensive baking room carries out tobacco flue-curing
Into the biological fuel gas of air accumulator, the dedicated heat of intensive baking room is sent to through gas pipeline by control valve a part
Wind furnace is respectively that intensive baking room provides hot wind progress tobacco flue-curing after lighting.Another part is by control valve through gas pipeline
It is sent to direct combustion hotblast stove, persistently provides drying heat source for retort shove charge material.
4, charcoal a part after going out charcoal is used for biomass carbon base system column production, and another part can be used for substituting combustion
Coal carries out traditional intensive baking room tobacco flue-curing, realizes circulation, efficiently utilizes.
Claims (4)
1. a kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments, including charging and discharging conveyer, dryer, deduster, biology
The dedicated retort of matter flue-cured tobacco, gas and oil separating plant, shell and tube condenser, moisture separator, air accumulator, special hot air stove, tobacco
Intensive baking room, direct-fired fuel gas hot-blast stove；It is characterized in that: the dedicated retort of more than two biomass flue-cured tobaccos, dryer is arranged
The outfeed belt conveyor tail end connection dedicated retort of biomass flue-cured tobacco feed inlet, the dedicated charing furnace bottom of biomass flue-cured tobacco distinguishes
Setting carbon outleting port goes out charcoal；A cellular burner, retort is respectively set in biomass flue-cured tobacco dedicated retort material char zone
The flue gas that material charing generates enters burner internal by the way that cellular burner surface is porous, then by under cellular burner
Outside the flue output retort just connected, primary oil, gas separating device into gas and oil separating plant；
The air inlet that oil, the primary oil of air separation, gas separating device gas outlet pass through flue connection second level oil, gas separating device
Mouthful, second level oil, gas separating device gas outlet pass through share flue gas pipeline connect shell and tube condenser, the output of shell and tube condenser
End connects air accumulator by air-introduced machine, and the combustion gas in air accumulator is sent to burning through gas pipeline by control valve a part
Device, it is hothouse baking tobacco leaf that the flame generated after lighting, which enters intensive baking room special hot air stove,；Another part passes through control valve
Direct combustion hotblast stove is connected through gas pipeline, direct combustion hotblast stove air outlet connects dryer air inlet, is drying machine drying object
Material provides heat source.
2. biomass carbon according to claim 1, gas intensive flue-cured tobacco complete set of equipments, it is characterized in that: biomass flue-cured tobacco is special
With a cellular burner is arranged in the furnace body of retort, which is cage enclosed construction, and use is heat-resisting
Stainless steel plate production；The flue gas that the charing of retort material generates is entered in burner by the porous design of cellular burner surface
Portion.
3. biomass carbon according to claim 1, gas intensive flue-cured tobacco complete set of equipments, it is characterized in that: second level is oily, gas separation
Setting is made of the level-one of alternate path two upper feature boards and a lower feature board to level Four process chamber in the cabinet of device；In case
Swivel nozzle is arranged positioned at the top of second level to tertiary treatment room in the top of body, carries out for spraying wood vinegar and hot water mixing
Secondary, oily, gas separation three times；Oil sump tank is set in the bottom of box, drain oil is arranged in oil sump tank bottom.
4. biomass carbon according to claim 1, gas intensive flue-cured tobacco complete set of equipments, it is characterized in that: intensive baking room is special
With hot-blast stove, fuel gas inlet and hot-blast outlet are set, fuel gas inlet is arranged burner, multiple pipe heater outsides is arranged inside hot-blast stove,
The combustion space of burner is connected to pipe heater outside, multiple interior heating tubes is arranged with pipe heater outside vertical direction, in interior heating tube
Both ends connect side combusion chamber, and side combusion chamber is connected to end combustion chamber；The hot-blast stove uses sustained combustion mode, firstly, by combustion gas
The combustible gas of burner is lighted below pipeline to hot-blast stove, and the flame after lighting enters hot-blast stove pipe heater outside region and adds
Heat, flame pass through external heat region again and heat interior heating tube into interior heating region, and last flame enters hot-blast stove two sides and end
End burning room.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910096157.1A CN109825319A (en) | 2019-01-31 | 2019-01-31 | A kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201910096157.1A CN109825319A (en) | 2019-01-31 | 2019-01-31 | A kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments |
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ID=66861967
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| CN209722036U (en) * | 2019-01-31 | 2019-12-03 | 辽宁金和福农业科技股份有限公司 | A kind of biomass carbon, gas intensive flue-cured tobacco complete set of equipments |
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Application publication date: 20190531 |