Description of the drawings
Fig. 1 is the part-structure schematic diagram of baking equipment for preparatory treatment of tobacco (heating equipment),
Fig. 2 is furnace interior structure chart, and wherein Fig. 2 a are right side block diagram, and Fig. 2 b are main structure figure, and Fig. 2 c are
Left side block diagram,
Fig. 3 is converter nose and slag removal mechanism schematic diagram in combustion furnace, and wherein Fig. 3 a are front view, and Fig. 3 b are left side view,
Fig. 4 is the cooperation schematic diagram of interior converter nose and outer converter nose in right side view in Fig. 3 a,
Fig. 5 is the burning air supply system structural schematic diagram of combustion furnace,
Fig. 6 is combustion furnace and heat exchanger installation diagram, and wherein Fig. 6 a are front view, and Fig. 6 b are left side view, and Fig. 6 c are to overlook
Figure,
Fig. 7 is the structural schematic diagram of heat exchanger shown in Fig. 5, and wherein Fig. 7 a are its left view internal structure chart, and Fig. 7 b are thereafter
Depending on structural schematic diagram,
Fig. 8 is the deduster structural schematic diagram in heat exchanger, and wherein Fig. 8 a are its front view, and Fig. 8 b are that its left view is (right
Answer rearview shown in Fig. 7 b), Fig. 8 c are its vertical view,
Fig. 9 is the concentration feeding system schematic diagram of five disjunctor cured tobacco curing houses,
Figure 10 is the schematic diagram for concentrating single feeding device in feeding system.
In figure:1, combustion furnace, 11, hopper, 12, helical blade feeder, 13, burning feed pipe, 14, converter nose, 15, burning
Air supply system, 16, slag removal mechanism, 17, burning distribution plenum;
121, feeding motor;
141, interior converter nose, 142, outer converter nose, 1421, miner diameter end, 1422, bigger diameter end, 143, flame watch window, 144, temperature
Spend inductive probe, 145, igniter, 146, hollow ventilated area;
151, small wind turbine, 152, air blower, 153, matching air box, 154, main ajutage, 155, discharge nozzle anti-backfire ajutage,
156, other purposes ajutages;
161, remove the gred motor, and 162, slagging-off band tooth push rod, 163, slagging-off rod bush, 164, push rod directive wheel, 165, gear,
166, electronic induction limit switch, 167, mechanical trip limit switch;
181, fence, 182, lack material warning device, 183, support frame, 184, separated material lock, 185, electric box, 186, adjustable
Height castor;
2, heat exchanger, 21, secondary combustion chamber, 22, deduster, 23, radiator, 24, chimney, 25, breast hole, 26, deashing
Mouthful, 27, heat exchanger bracing frame;
221, flame kicker baffle, 222, cylindrical dedusting main body, 223, frustum structure, 224, flue gas rising passway,
225, heat exchanger flame spray entrance (fume inlet passage);
231, radiator bobbin carriage, 232, fin radiator, 233, heat dissipation light pipe;
3, feeding system is concentrated, 31, the Material sucking machine containing vacuum pump, 32, storage vat, 33, aspirating air pipe, 330, air entry,
34, charging line, 340, material sucking port, 35, auger feed mechanism, 36, solenoid valve, 37, vacuum hopper, 371, filter screen, 38, again
Power valve;
4, barn, 41, for hot cell, 42, hang smoke-box, 421, hang smoke-box gate, 43, insulated wall, 44, for hot cell return air inlet,
45, for hot cell air outlet, 46, high low speed circulating fan, 47, cold wind import.
Specific implementation mode
The present invention will be described in detail heating equipment and each component therein in conjunction with attached drawing, but the protection model of the present invention
It encloses and is not limited to that.
One, the combustion furnace in heating equipment:
1) biomass granule fuel
The biomass of the present invention being applicable in fuel mainly and include with sawdust, tabacco straw, soybean stalk, rice husk etc. for raw material
Particle.The biological particles are the cylindrical pellet that raw material crushes simultaneously extrusion molding (or compression forming), grain size (diameter)
For 3~20mm, preferably 5~10mm, particle length is generally less than 6cm, and preferably particle length is 2~5cm.The biological particles
The density of fuel is > 1g/cm3, preferably its density is 1.05~1.3g/cm3。
2) converter nose in combustion furnace
As shown in figures 1-4, present invention firstly provides the converter nose in a kind of biomass combustion furnace, the converter nose 14 includes sleeping
Converter nose 141 and the outer converter nose 142 of truncated cone-shaped, form hollow ventilated area 146 in the cylinder of formula setting between interior converter nose and outer converter nose,
The burner hearth of combustion furnace described in main composition inside the interior converter nose, the bottom of converter nose offers ventilation hole for being in Horizontal cylinder
Biomass granule fuel burning provides air;Interior converter nose axial direction one end is connect with the bottom of burning feed pipe 13, the axial other end
For being inserted into the heat exchanger 2 being connect with combustion furnace 1;Axial one end that outer converter nose is equally used for being inserted into the heat exchanger 2 is
Miner diameter end 1421, outer converter nose is its bigger diameter end 1422 close to axial one end of burning feed pipe, and outer converter nose miner diameter end 1421
The circumferential weld width d of inner wall to the radial distance between interior converter nose outer wall, that is, bocca periphery is 0.8~5mm.
In a kind of specific embodiment, the outer diameter of the interior converter nose is 159mm, and the outer diameter of outer converter nose bigger diameter end is
214mm.In a kind of specific embodiment, the circumferential weld width d is 1~3mm, preferably 1.5~2.5mm, for example, 2mm.
In a kind of specific embodiment, in nearly heat exchanger one end, interior converter nose is concordant with the axial length of outer converter nose, and
In closely burning feed pipe one end, the axial length of interior converter nose is more than the axial length of outer converter nose, and is longer than outer converter nose in interior converter nose
Axial one section of radial outside be provided with the burning distribution plenum 17 at the converter nose end in package.The burning distribution plenum is suitable first
In a buffer container, for accessing the fresh air come from air blower, and be distributed to combustion furnace burner hearth and
In secondary combustion chamber.
In a kind of specific embodiment, a diameter of 2~10mm of the ventilation hole of interior converter nose bottom, quantity be 20~
200.On the one hand the design of ventilation hole is to ensure that the fresh air to provide sufficient in burner hearth, while ensuring the biology in burner hearth
Matter particle do not fall out to hollow ventilated area or burning distribution plenum in, and can accurately design its size, quantity and distribution and
Design circumferential weld size makes the air-supply ratio of the second-time burning in primary combustion and heat exchanger in burner hearth suitable.A kind of specific
Embodiment in, a diameter of 3~7mm of the ventilation hole of interior converter nose bottom, quantity be 40~100;Specifically, the ventilation
Hole is, for example, the equal cloth hole that diameter 5mm quantity is 70.
Further include slag removal mechanism 16 in a kind of specific embodiment, in the converter nose, and the slag removal mechanism be with
The self-skimming mechanism of controller electrical connection, for the clinker in interior converter nose to be pushed into a small amount of not sufficiently combusted clout part
Second-time burning is carried out in heat exchanger 2.
Further include that the discharge nozzle being arranged in burning feed pipe is prevented back in a kind of specific embodiment, in the converter nose
The air supply direction of fiery ajutage 155, the discharge nozzle anti-backfire ajutage is consistent with the feed direction of biomass granule fuel, uses
In preventing the stove fire in burner hearth from burning in hopper, while to provide another way combustion-supporting fresh air in burner hearth.A kind of specific
Embodiment in, discharge nozzle anti-backfire ajutage be two, blowout wind fuel is blown into converter nose down.
Further include flame watch window 143 in a kind of specific embodiment, in the converter nose, the flame observation window
Mouth is cylindrical structure, and axial one end is goed deep into burner hearth, and the axial other end is arranged in outer converter nose radial outside;In the converter nose
Further include setting the temperature sense probe 144 of fire box temperature and for the igniter 145 of igniting for surveying;The flame observation window
Other purposes ajutages 156 are both provided with by mouth, temperature sense probe and igniter for preventing stove fire from damaging workpiece;And
The temperature sense probe, igniter, for for provided in burner hearth biomass granule fuel helical blade feeder 12 and
Burning air supply system 15 for providing combustion air for combustion furnace is electrically connected with the controller.In a kind of specific embodiment
In, the igniter is silicon nitride igniter.The setting of the flame watch window and temperature sense probe makes staff
It can be with whether there is or not flame-out in accurate judgement combustion furnace.
Converter nose advantageous effect:The hollow ventilated area 146 of converter nose provided by the invention and interior converter nose and outer converter nose miner diameter end
Between the setting of circumferential weld make:1) there is more stable air pressure in hollow ventilated area, more stable burning situation is provided for burner hearth, 2)
Burn again after air in hollow ventilated area is preheated, be conducive to improve efficiency of combustion, 3) it is provided in burning air supply system
Fresh air can enter through this approach in heat exchanger so that clinker obtained by biomass granule fuel or its primary combustion and a small amount of
Not sufficiently combusted clout is able to carry out sufficient second-time burning in heat exchanger, 4) size of circumferential weld width and burner hearth bottom are logical
The matched design of air holes size may make primary combustion of the biomass granule fuel in burner hearth and the secondary combustion in heat exchanger
It burns to adjust and arrives desirable level so that efficiency of combustion is maximum.
The processing of converter nose:Converter nose uses 310S high temperature resistant stainless steel materials in burning.310S high temperature resistant stainless steels are a kind of
Austenitic chromium nickel stainless steel, with good inoxidizability and corrosion resistance, because the chromium and nickel of higher percent, make it gather around
Have good more creep strengths, can continuous operation at high temperature, there is good heat-resisting quantity, heat safe temperature to be not less than
1150℃.When making converter nose in burning, the cutting of high-precision sawing machine is first passed through, then put face work on lathe, finally puts and add on drilling machine
The a certain number of ventilation holes of work.The design of converter nose has fully considered that the characteristic of biomass granule fuel, structure are set in combustion furnace
Meter is reasonable, ensures full combustion of fuel.The outer converter nose of burning is cast using high temperature spheroidal graphite cast-iron one-pass molding, the temperature tolerance of material
It can be not less than 1000 DEG C and with the indeformable characteristic under high-temperature medium.The converter nose of the present invention is using high temperature resistant, etch-proof
For the interior converter nose that 310S stainless steels make as burner hearth liner, service life is 10 times of other common materials or more.
3) slag removal mechanism in combustion furnace
See Fig. 3, the present invention provides the self-skimming mechanism in a kind of biomass combustion furnace, including horizontally disposed slagging-off band
Tooth push rod 162, for slagging-off with tooth push rod provide with the slagging-off motor 161 of passing power and gear 165, be set in slagging-off band tooth push away
The slagging-off rod bush 163 of bar radial outside, the push rod directive wheel 164 being oriented to tooth push rod for slagging-off, the slagging-off band tooth push rod
Axial one end be arranged in the burner hearth that converter nose 141 is formed in the cylinder by horizontal setting, slagging-off is axial another with tooth push rod
One end is arranged outside burner hearth and pushes away slag movement by the level of controller control push rod.In the present invention, the teeth portion on gear and slagging-off
With the teeth portion matching in tooth push rod so that gear rotation drives the push rod horizontal movement.
In a kind of specific embodiment, the self-skimming mechanism further includes electronic induction limit switch 166 and machine
Tool lead limit switch 167 is used to limit the start-stop position that slagging-off moves in the horizontal direction with tooth push rod.In the present invention, the electricity
Son induction limit switch 166 and mechanical trip limit switch 167 are arranged at slagging-off with the axial the same end of tooth push rod 162,
(duplicate protection) is limited when retracting for push rod moves damage to ensure that converter nose structure will not be retracted by push rod.
In a kind of specific embodiment, the push rod directive wheel 164 and gear 165 are separately positioned on slagging-off band tooth and push away
Corresponding position above and below bar.
Further include that setting is removing the gred with tooth push rod axial direction one end in a kind of specific embodiment, in the slag removal mechanism
And the dreg pushing board in burner hearth is set.Preferably, the horizontal maximum width of the dreg pushing board is the 1/20~1/ of interior converter nose internal diameter
3, the height of dreg pushing board is the 1/20~1/3 of interior converter nose internal diameter.It is highly preferred that the horizontal maximum width of the dreg pushing board is interior stove
The 1/10~1/4 of mouth internal diameter, the height of dreg pushing board are the 1/10~1/4 of interior converter nose internal diameter.
In a kind of specific embodiment, the dreg pushing board is arc plate or rectangular slab.The arc plate is for example in half
Circle, crescent, rectangle or square, the biological particles stove that the dreg pushing board so designed will appropriately can burn in burner hearth
In slag and a small amount of not sufficiently combusted clout push-in heat exchanger, and ensure that suitable biomass granule fuel stays in burner hearth simultaneously
In.
Advantageous effect:Self-skimming mechanism provided by the invention automatically controls regular slagging-off, anti-fuel coking caking, and institute
It states push rod and stirs burner hearth bottom in time to prevent ventilation hole from blocking, it is ensured that efficiency of combustion.In addition, releasing combustion furnace by push rod
Clinker and a small amount of not sufficiently combusted clout in heat exchanger can also second-time burning, further increase efficiency of combustion.The present invention carries
The self-skimming mechanism of confession is in slag removal, it is possible to part biological matter granular fuel is pushed into heat exchanger, because push-in is changed
Biomass granule fuel in hot device 2 can carry out second-time burning, thus self-skimming process will not detract efficiency of combustion completely.
Self-skimming mechanism uses material and processing:Slagging-off therein uses the 310S high temperature resistants of diameter 25mm not with tooth push rod
Become rusty round steel machine add-on type, has the characteristics that high intensity, high temperature resistant, corrosion-resistant, meets duty requirements.Using bipolar caging system control
System (mechanical and electronic type) push rod moves back and forth, and reaches ideal self-skimming effect.
4) the burning air supply system in combustion furnace
See Fig. 5 and Fig. 2, the present invention provides the burning air supply system in a kind of biomass combustion furnace, burning gas supply system
System 15 includes small wind turbine 151, air blower 152 and the matching air box 153 being sequentially connected in series, and the small wind turbine is charged pool power supply and wind turbine
For power in the wind turbine of 10~200w, the air blower 152 is power of fan more than small power of fan and for being provided for combustion furnace
The wind turbine of main fresh air, the matching air box 153 be used for distribute fresh air and it include multiple parallel connections outlet, it is described
The outlet of multiple parallel connections is connect with main ajutage 154, discharge nozzle anti-backfire ajutage 155 and other purposes ajutages 156 respectively.
The burning air supply system is the advantageous effect that combustion furnace is brought:The small wind turbine of charged pool is provided in the present invention
151, even if combustion furnace is in power failure work, small wind turbine may be that burning provides a certain amount of fresh air, more important
, when power failure, small wind turbine can be that discharge nozzle anti-backfire ajutage 155 and other purposes ajutages 156 provide enough skies
Gas will not damage such as igniter, the glass plate of flame observation window, temperature sense to ensure that stove fire will not burn into hopper
The workpieces such as should pop one's head in, and when having a power failure, can optionally open, close or adjust the valve on main ajutage 154.Institute of the present invention
It states burning air supply system and provides a kind of safe and efficient working environment for biomass combustion furnace.
In a kind of specific embodiment, the power of the small wind turbine is 15~100w, preferably 20~50w;The drum
The power of wind turbine is 150~800w, preferably 200~500w.Specifically, the power of the small wind turbine and air blower is for example distinguished
For 25w and 250w.In a kind of specific embodiment, the small wind turbine is centrifugal blower.In a kind of specific embodiment
In, air blower when lighting a fire that is switched on closes and only opens the small wind turbine, and keeps small wind turbine to continue after blower opening
Work can prevent from being tempered when having a power failure.The small wind turbine can be equipped with service message and battery dual power supply, in normal operation, with electricity
Net power supply, and storage battery power supply is enabled automatically when having a power failure.Independent anti-backfire is equipped in the burning air supply system of the present invention to fill
Set, it is any in special circumstances all be not in tempering detonation the phenomenon that.
In a kind of specific embodiment, other purposes ajutages include igniter ajutage 156a, temperature sense
Should pop one's head in ajutage 156b and flame watch window ajutage 156c.
In a kind of specific embodiment, the other end of the main ajutage 154 and the burning distribution plenum 17 of combustion furnace
Connection is burnt for being sent into fresh air power-assisted biomass granule fuel from interior converter nose bottom vents in burner hearth, and from ring
Fresh air is provided for heat exchanger carry out second-time burning at seam;The other end of the discharge nozzle anti-backfire ajutage 155 is passed through combustion
Burn prevents the stove fire in burner hearth from burning into hopper 11 into burner hearth inside feed pipe 13 while feeding fresh air.This field skill
What art personnel can understand, the other end of the discharge nozzle anti-backfire ajutage 155 can also not be passed directly into burning feed pipe
It inside 13, but is passed through in the pipe for being set up directly on and being installed with helical blade feeder 12, then which is passed through again
It burns in feed pipe and enters in burner hearth.
5) other structures in combustion furnace
As shown in Fig. 1~5, the combustion furnace 1 further include for be inserted into heat exchanger 2 and interfaced converter nose 14, use
Hopper 11 in storage biomass granule fuel, the helical blade feeder 12 for being sent into biomass granule fuel in converter nose
With burning feed pipe 13, for by the slag removal mechanism in the clinker and a small amount of not sufficiently combusted clout push-in heat exchanger in converter nose
16 and it is distributed to burning distribution plenum combustion-supporting in converter nose and heat exchanger for the fresh air that provides of air supply system 15 that will burn
17。
In the present invention, flame is sprayed from converter nose in the horizontal direction, and flame is laterally burnt into heat exchanger, and flame level sprays
The distance of converter nose end is usually 30~150cm.
In a kind of specific embodiment, the helical blade feeder 12 is drawn by feeding motor 121, and the combustion
It further includes the fence 181 being arranged above hopper 11 for auxiliary storage to burn stove, and the scarce material report at the top of burning feed pipe is arranged
The feed hopper bottom in combustion furnace is arranged for electrical in alarm device 182, the support frame 183 for being used to support each component in combustion furnace
The channel and play the separated material lock 184 of anti-backfire, be used for that physics blocks between feed hopper bottom and helical blade feeder when failure
The caster with adjustable height for showing and manipulating the electric box 185 of automatically controlled information and adjusted for combustion furnace movement and converter nose height
186。
Advantageous effect:Firepower size in combustion furnace of the present invention can be accurately controlled by control system, specific main
If controlling the start and stop of helical blade feeder 12 and controlling firepower size.Such as set-up of control system is friction feeding 8s and stops
It has a rest and continues periodical feeding after 5s, stove fire is more prosperous at this time, and friction feeding 5s and rests and continue stove fire when periodical feeding after 5s
It is smaller.During specific control, we can be of different sizes according to required firepower and be divided into multiple firepower gears, such as 10
Shelves, then its feeding rule is programmed and is controlled for each firepower gear;Meanwhile to the slagging-off frequency of each firepower gear
It is programmed and automatically controls.In a kind of specific embodiment, we are according to temperature feedback in the extension smoke-box of barn come automatic
Firepower size or firepower gear are controlled, and slagging-off frequency is automatically controlled according to firepower size or firepower gear.
Support frame 183 uses material and processing:40*40 square tube sections are selected, are first cut through high precision numerical control sawing machine, then put
It is welded in fixing mould, keeps the consistency of size.
Helical blade feeder uses material and processing:The core component of helical blade feeder is helical blade and spiral
Axis.Helical blade selects Q345 low-alloy steel, and material good under laser blanking machine is added in helical blade former and is rushed
Pressure.Helical axis selects 45# round steel quenched through high-temperature heat treatment, and hardness is up to 260~300HBS.
Two, the heat exchanger in heating equipment:
A kind of heat exchanger is provided in Fig. 6~8, the heat exchanger 2 is used to be connected to 14 one end of horizontal converter nose of combustion furnace 1,
The heat exchanger 2 includes the secondary combustion chamber 21 for being located at lower part, is arranged in second-time burning room and for flame and high temperature cigarette
The deduster 22 of gas dedusting carries out the radiator 23 of heat exchange with air for the high-temperature flue gas after dedusting and is handed over for heat
The chimney 24 of flue gas discharge heat exchanger after changing;The deduster 22 includes connecting the converter nose 14 and for will be in converter nose laterally
Fume inlet passage 225 that the flame and high-temperature flue gas of ejection introduce in heat exchanger, two axial directions for being connected to 225 end of fume inlet passage
It is arranged at the cylindrical dedusting main body 222 of vertical direction, is located at two intersubjective flame kicker baffles of cylindrical dedusting
221 and the top in each cylindrical dedusting main body and with the frustum structure of cylindrical dedusting main body coaxial arrangement
223, the flame kicker baffle 221 be vertically arranged and for by the flame and high-temperature flue gas from being introduced tangentially into two cylinders
In dedusting main body, in upper and miner diameter end under, bigger diameter end and cylindrical dedusting main body are close for the bigger diameter end of the frustum structure 223
Envelope connection so that flame and high-temperature flue gas are after fume inlet passage enters deduster, in the guiding role backspin of flame kicker baffle
It rotates into cylindrical dedusting main body, then is flowed out from the flue gas rising passway 224 that the center taper through-hole of frustum structure is formed
Deduster and enter the radiator 23.
Skilled artisans will appreciate that, the frustum structure is, for example, frustum cone structure, but for ease of mechanical processing, is led to
Often the frustum structure is set to polygonal frustum structure, such as the polygonal frustum structure at 10~30 angles, in a kind of specific reality
Apply in mode is 18 angles.When processing, sector structure material (one piece of fan-shaped strip sheet) good under laser is rolled over into 17 knives through bar folder
Form frustum mechanism.
In a kind of specific embodiment, the fume inlet passage 225 is set as rhs-structure, and fume inlet passage 225 to
Few one end connect in the longitudinal direction with converter nose 14 is provided with channel base plate notch, for slag removal mechanism 16 push away the clinker come with
A small amount of not sufficiently combusted clout is fallen to from there in the secondary combustion chamber 21 of heat exchanger 2.Skilled artisans will appreciate that
, bottom plate can not also be arranged in 225 rhs-structure of the fume inlet passage, this can't influence the efficiency of dust collection of deduster.
In a kind of specific embodiment, two cylindrical dedusting main bodys are tangent to be arranged and sets up separately in fume inlet passage high temperature
The left and right sides in flow of flue gas direction, the maximum width m that fume inlet passage projects in the horizontal plane are less than or equal to two frustum structures
The shortest distance n that projects in the horizontal plane of miner diameter end.
In a kind of specific embodiment, the heat exchanger 2 further includes the breast hole 25 for being located at exchanger base, is located at
The cleaning door 26 of the flue end of radiator 23 and the heat exchanger bracing frame 27 for being used to support each component of heat exchanger;It is described
Radiator 23 includes radiator bobbin carriage 231 and the fin radiator 232 being arranged in radiator bobbin carriage 231 and heat dissipation light pipe
233, the high-temperature flue gas after dedusting is introduced into lower layer's fin radiator, after middle level fin radiator and upper layer heat dissipation light pipe from cigarette
Chimney is discharged, and air enters radiator above radiator bobbin carriage 231, and is flowed from above to below outside heat-dissipating pipe, and absorption comes from
The high temperature air of heat is flowed out from 2 bottom of heat exchanger in high-temperature flue gas;Lower layer's fin radiator is five and is arranged in parallel
On sustained height, the middle level fin radiator is four and is arranged in parallel on sustained height, and radiate light pipe on the upper layer
The non-finned light pipe being arranged in parallel on sustained height for five.Skilled artisans will appreciate that, in every layer of heat-dissipating pipe
Flue gas in four or five heat-dissipating pipes co-flow simultaneously.Flue-gas temperature in the heat dissipation light pipe on upper layer is not high, thus
Without adding the fin for increasing heat exchange area to it, if necessary, naturally it is also possible to which fin is added to it.Alternatively, it is also possible to set
It sets more layers heat-dissipating pipe or every layer is arranged more roots or less root heat-dissipating pipe, this is all feasible.
In a kind of specific embodiment, in lower layer's fin radiator, middle level fin radiator and upper layer heat dissipation light pipe
In one end of every hot channel be both provided with cleaning door 26 and deashing lid.In every layer of hot channel in compared with the prior art
One end jointly setting one deashing lid for, mode provided by the invention can make the better tightness of heat-dissipating pipe, heat exchange
The heat exchange efficiency higher of device.
In a kind of specific embodiment, is built in 21 inner wall of secondary combustion chamber of the heat exchanger and be equipped with refractory brick, and
The heat exchanger is split settings, using flange by scarfing cinder pipeline, secondary combustion chamber 21, the radiator of split settings in heat exchanger
23 and chimney 24 be correspondingly connected with, and also using flange by the section and in upper nothing of laying bricks under of 21 split settings of the secondary combustion chamber
Brick section connects;Scarfing cinder drawer and matched scarfing cinder rake are additionally provided at the breast hole.In the present invention, heat exchanger
Second-time burning room in build set refractory brick make it have very strong heat insulating ability and mitigate steel plate degree of oxidation.Heat exchanger is group
Dress formula structure, installation operation is convenient, and flanged joint is convenient for maintenance and repair, and is not required to mechanical unloading installation, processing safety
By force.In addition, also flue is arranged in upper no brick section in secondary combustion chamber in the present invention, it is specifically located above deduster.
Those skilled in the art know that ground, cyclone separator are that the one kind detached for gas-solid system or liquid-solid system is set
It is standby, rotary motion is caused its working principle is that being introduced tangentially by air-flow, makes the solid particle or liquid with larger centrifugal inertial force
Drop is got rid of to outside wall surface and is separated.The advantages of deduster in the present invention draws cyclone separator, and further setting frustum structure 223
So that the deduster is more suitable for detaching the dust come from the flame and high-temperature flue gas laterally gone out in combustion furnace 1.
In a kind of specific embodiment, the ratio of the diameter and bigger diameter end diameter of the miner diameter end of the frustum structure is
1:1.5~5.In a kind of specific embodiment, the ratio of the diameter and bigger diameter end diameter of the miner diameter end of the frustum structure
It is 1:2~4, the deduster so designed can give the flame and high-temperature flue gas that are introduced in heat exchanger in the present invention to play best remove
Dirt effect.
The advantageous effect brought by present invention heat exchanger:The heat exchanger of the present invention uses the cyclone type dedusting of special structure
Device, for the dust generated when by burning after cyclone dust collectors sedimentation separation, purified high-temperature flue gas can reach national environmental protection row
Put standard (smokeless and dust free).
Secondary combustion chamber in present invention heat exchanger is divided into two sections.Setting adapts in it on four peripheral walls of lower intersegmental part
The refractory brick of wall size.The thickness of refractory brick is 30mm~50mm, is tiled using high temperature clay.Epimere is internally provided with rotation
Wind deduster can effectively prevent the finned tube that the dust generated in combustion process enters radiator.Secondary combustion chamber (specifically changes
Hot device flame entrance 225) it is docked tightly with the outer converter nose of combustion furnace.
Secondary combustion chamber 21 in present invention heat exchanger is made of the acid resisting steel of 4mm thickness, the flue gas in secondary combustion chamber
Pipeline is fastenedly connected with radiator 23 using combined type, it is ensured that sealing;Radiator 23 is made of acidproof steel or stainless steel, heat dissipation
Area >=9m2, heat exchange efficiency >=57.8%.
Chimney in present invention heat exchanger usesRound steel pipe make, one end is connect with radiator, another
End is stretched out for being connect with civil engineering chimney outside the wall of hot cell, and all junctions ensure to seal.
In the present invention, after combustion furnace is docked with heat exchanger, the height of secondary combustion chamber bottom of the converter nose apart from heat exchanger away from
From for 200~300mm, for example, 250mm so that secondary combustion chamber bottom can store waste residue and carry out secondary abundant combustion
It burns, moreover it is possible to buffer raising up for dust, reduce the deposition in heat-dissipating pipe, (each baking season cleaning one of deashing number can be reduced
It is secondary), labor intensity is reduced, heat utilization rate is improved.
Full-automatic control system in heating equipment provided by the invention has following features:
1) has one-key start function.
2) has the fully automatic operation pattern for bulk curing barn tobacco flue-curing flow.
3) operating status can be preserved by having a power failure extremely in operational process, can be connected operation after being re-energised automatically.
4) have (reserved) centralized control and internet of things functional.
5) has automatic firing function:Without manual intervention Full-automatic ignition, can judge in burner hearth whether it is flame-out and from
Dynamic rekindling.
6) operating status can be shown:It can show current firepower size, operating status, fire box temperature.
7) has self-skimming function:Self-skimming ensures combustion furnace normal operation.
8) have and lack material alarm:Sound-light alarm, SMS remind (optional).
9) have preceding scavenging, rear scavenging and flame-out security function, prevent tempering detonation.
Three, the concentration feeding system in heating equipment:
As shown in Figure 9 and Figure 10, the present invention provides a kind of biomass granule fuel concentration feeding system, the concentration feed
System 3 is used to provide biomass granule fuel for more than two concentrations of combustion furnace 1, and the concentration feeding system 3 includes containing vacuum
Material sucking machine 31, the storage vat 32, two of pump or more aspirating air pipe 33, two or more charging line 34, is sent auger feed mechanism 35
Expect distribution joint, more than two solenoid valves 36, more than two vacuum hoppers 37 and more than two weight valves 38;The storage vat 32
For leaving biomass granule fuel concentratedly, its bottom is provided with auger feed mechanism (35) and for granular fuel to be sent into
The feeding distribution joint of different charging lines 34, during the vacuum hopper 37 is arranged at the top of combustion furnace for for combustion furnace
Hopper 11 is fed, and the solenoid valve 36 is arranged on the aspirating air pipe 33 that vacuum hopper 37 is connect with vacuum pump, the weight valve
38 are arranged in 37 bottom of vacuum hopper;When solenoid valve 36 on vacuum pump startup and certain or a plurality of aspirating air pipe 33 is opened,
Under vacuum action, the weight valve 38 of 33 corresponding vacuum hopper of aspirating air pipe, 37 bottom remains closed, and biological particles
Fuel is sent into through corresponding charging line in the vacuum hopper 37;When the solenoid valve 36 is closed, the gravity after vacuum is unloaded
Valve 38 is opened under the self gravitation effect of biomass granule fuel in vacuum hopper 37 and from the hopper 11 in trend combustion furnace
Feed.
Skilled artisans will appreciate that, every barn of bulk curing barn can generally prepare a combustion furnace 1 and one
Heat exchanger 2, thus set up five combustion furnaces separately outside five disjunctor barns as shown in Figure 9, use concentration feeding system of the present invention
Can be that above-mentioned five combustion furnaces are fed.Specifically, can be that concentration confession is used alone in certain combustion furnace in some period
Material system can also be to have two or more combustion furnaces in some period while using the concentration feeding system.In the present invention,
The auger feed mechanism is also known as screw feed mechanism, and main function is stirring fuel and fuel is sent into institute from storage vat
It states in feeding distribution joint.Stirring structure therein can prevent biomass granule fuel from blocking the feeding distribution joint.Institute
Stating auger feed mechanism 35 can be identical or different with the helical blade feeder 12 in combustion furnace 1, but both general using not
With the machine of model, for example, both blade diameter is different or screw pitch is different and the feeding ability that both causes is different.
In a kind of specific embodiment, the internal diameter of the aspirating air pipe 33 is 20~150mm, the charging line 34
Internal diameter be 20~150mm.In a kind of specific embodiment, the internal diameter of the aspirating air pipe 33 is 30~120mm, preferably
40~100mm, specifically for example, 50mm.The internal diameter of the charging line 34 is 30~120mm, preferably 40~100mm, concrete example
Such as it is 50mm.
In a kind of specific embodiment, the air entry 330 being connected to the aspirating air pipe on vacuum hopper is located at very
On the roof of empty hopper, the material sucking port 340 being connected to the charging line on vacuum hopper is located at the upper of the side wall of vacuum hopper
Portion;The top of the vacuum hopper is equipped with filter screen 371, and the material sucking port 340 on vacuum hopper is located at below filter screen, vacuum
Air entry 330 on hopper is located above filter screen, and the solenoid valve is Unidirectional solenoid valve, and the vacuum pump is liquid-ring type vacuum
Pump.The setting of filter screen can prevent biomass granule fuel to be drawn in vacuum pump.In a kind of specific embodiment, institute
The power for stating water-ring vacuum pump is 3kw or more, preferably 5~10kw, for example, 7.5kw.
In a kind of specific embodiment, the weight valve 38 includes valve plate, shaft and weight member, valve plate and counterweight
Component is connect with shaft, when not being loaded with biomass granule fuel in vacuum hopper and during vacuum pump opens feeding, weight
The valve plate of power valve 38 is closed under the action of weight member, and is loaded with biomass granule fuel in vacuum hopper and is unloaded
When carrying vacuum, valve plate automatically opens under the gravity compressing of biomass granule fuel to be fed in the hopper 11 to combustion furnace.This hair
In bright, according to the weight of weight member described in the density of biomass granule fuel and the volume respective design of vacuum hopper so that
The weight valve is closed when can realize zero load, the function that when closed when vacuumizing and load opens.
In a kind of specific embodiment, the volume of the vacuum hopper 37 is less than or equal to the hopper 11 in combustion furnace
Volume.In a kind of specific embodiment, the volume of the vacuum hopper 37 be the volume of the hopper 11 in combustion furnace about
1/2, thus vacuum intake can then be automatically filled with the hopper 11 twice.Those skilled in the art can be from understanding, the present invention
Described in vacuum hopper only play the role of to biomass granule fuel it is temporary, when vacuum pump stops suction, in vacuum hopper
Granular fuel is then dropped to automatically in hopper below.In a kind of specific embodiment, also set on the hopper 11
It is equipped with glass vision panel, whether observe charging situation for staff normal.
Further include controller in the Material sucking machine 31 containing vacuum pump in a kind of specific embodiment, the control
Device is electrically connected control with the material-level measure sensor being arranged in combustion furnace, the controller also with the motor of auger feed mechanism,
The starter of vacuum pump and solenoid valve electrical connection control.In a kind of specific embodiment, controller is according to setting
The scarce material institute feedack that material-level measure sensor in combustion furnace detects both manually or can be automatically controled the collection
The start and stop of middle feeding system, selection is to the vacuum hopper feed on specified one or more combustion furnaces.In a kind of specific reality
It applies in mode, the latter linked each charging line of feeding distribution joint is respectively provided with feeding solenoid valve, when certain combustion furnace
When occurring to lack material alarm, controller controls the electricity on vacuum pump, the motor of auger feed mechanism, feeding solenoid valve and aspirating air pipe
Magnet valve is opened, and under the suction of vacuum pump, biomass granule fuel is drawn from feeding distribution joint to mutually corresponding vacuum
In hopper, the weight valve of vacuum hopper bottom keeps air-tight state under vacuum action at this time.When feeding reaches certain time length
Afterwards, solenoid valve, vacuum pump and the auger feed mechanism on controller control aspirating air pipe are closed, and are stopped suction, are unloaded vacuum,
Grain fuel is opened weight valve under its gravity and is down to from vacuum hopper in the hopper of combustion furnace.
Concentrate feeding system advantageous effect:1) concentration feeding system provided by the invention concentrates feed using vacuum, ensures
Feeding system is stable, and in conveying, pipeline is in sealing vacuum state, and absolutely not putty happens.2) provided by the invention
It concentrates feeding system to use Automatic Control, responds the scarce material warning device 182 of each different combustion furnace of its connection with right
The combustion furnace carries out sub-material conveying.Its feeding is accurate, fuel will not be caused to lack because personnel feed not in time, and then influence cigarette
Leaf toasts.3) service life of the concentration feeding system is long, and service life is spiral, belt-type feeder apparatus service life
5-10 times.4) saving of labor, time saving, reduction labor intensity, reduction baking cost.
It can be that combustion furnace is fed in time that biomass granule fuel provided by the invention, which concentrates feeding system, and whole system is certainly
Dynamic control feeding, only needs manpower or machinery that biomass granule fuel is unpacked and is poured into the storage vat 32, other processes are
Full-automatic mechanical operates, and saves a large amount of manpower and materials.
Four, heating equipment
All welding are all made of mechanical hand automatic welding in heating equipment provided by the invention, and welding position is selected and base material
Consistent wlding is welded, and ensures that all weld seams are tight, smooth, pore-free is air tight without slag inclusion, and mechanical performance reaches base material
Performance.When high-grade base material and inferior grade base material weld, the wlding consistent with high-grade base material must be selected.
The outer metallic surface of heating equipment provided by the invention is all made of resistance to 500 DEG C or more high temperature, anti-oxidant, strong adhesive force
Environment-friendly materials carry out preservative treatment, external coating simultaneously through blasting treatment make surface cleanness grade reach GB/T 8923 provide
The requirement of Sa2.5 grades, surfaces externally and internally carries out 3 sprayings using high temperature, epoxy zinc rich primer, and finishing coat is (roasting using electrostatic spraying
Paint), this technique has the characteristic of high temperature resistant and resistant to strong corrosion, extends the service life of heating equipment.The heating equipment makes
With the service life up to 10 years or more, generally 12 years or more.
In conclusion on the basis of existing technology, applicant of the present invention successfully develops high-efficiency low-pollution energy-saving ring
The biomass granule fuel heat supply complete set of equipments of guarantor, realizes biomass fuel and fully burns, solve previous biomass fuel
The technical barrier that tar can't burn completely coking caking is generated in burning.The present invention also successfully develops novel heat exchanger,
Solve the problems, such as that heat exchange utilization rate is not high in current tobacco flue-curing.And successfully develop new tobacco baking intelligent control
System processed, the effect of full-automatic regulation firepower that realizes biomass combustion according to tobacco flue-curing heat demand have reached burning
Materials are few, and the quality of tobacco for toasting gained is high, energy-saving and environment-friendly purpose.In the base for meeting tobacco roasting temperature control process requirement
On plinth, the function of fully automatic operation, self-skimming, energy-saving and emission-reduction, environment-protection low-consumption is not only realized, also there is fast, heating of lighting a fire
Soon, firepower is strong, the features such as being readily burned and be precisely controlled.
Specifically:
1, equipment electromechanical integration, high degree of automation is stable, safety.The machine is using automatic feed, automatic point
Fire, automatic adjustment oxygen supply, temperature automatically controlled, operating in a key, precisely run, and combustion process is in semi-closed state, outside the flames of anger
It lets out, no pressure operation, low-voltage power supply;Unique self-skimming Functional Design completes self-skimming, safety and stability.
2, combustion furnace power regulation amplitude is big, and temperature-controlled precision is high.Combustor (combustion furnace) power can be according to tobacco flue-curing work
The demand of skill is arbitrarily adjusted, and achievees the purpose that accurately control baking by controlling automatic function.Tobacco flue-curing work can be fully met
The needs of skill pass through accurate temperature control (temperature-controlled precision is up to 0.1~0.5 DEG C, and precision is higher than 1~3 DEG C coal-fired of temperature-controlled precision), energy
Effectively evade the mass loss that the factors such as temperature control is inaccurate are brought.Rationally compact, light-weight (the only traditional flue-cured tobacco of burner structure
The half weight of equipment), installation it is simple and convenient.
3, biological particles burning is abundant, and efficiency of combustion reaches 87%.Combustor uses half integrated gasification combined combustion technology, tool
There is multi-faceted high temperature to supply oxygen the characteristic of half gasification, and combustion, energy long-time low power run, burning is abundant, no soot emission, thermal effect
Rate is high, and flue dust, sulphur are nitrogen discharged low, sulfur dioxide, hydrogen sulfide zero-emission, non-secondary pollution, and shop environment is clean.Evade because of combustion
Influence of the flue dust and pernicious gas of coal to flue cured tobacco quality, the color, smell and taste for tobacco leaf of coming out of the stove are strong, and quality of tobacco is obviously improved.
4, heat exchanger heat utilization ratio is high.Heat exchanger (radiator) heat exchange area is big, and sootfall room temperature is high, effectively
Ground solves equipment coking phenomenon, and smoke tar can gasify and burn out, heat exchange efficiency is greatly improved, overall heat exchange efficiency is made to reach
57.8%.
5, fuel tolerance is wide, energy-saving and emission-reduction.The combustor is using biological particles as fuel, specially agriculture (straw, wheat
Grass, cornstalk, corncob, rice husk, peanut shell, levant cotton exocarp, cotton stem, cogongrass, weeds ...) woods (trees, bark, tree root, tree
Leaf, wood shavings, bamboo powder, sawdust ...) the like waste is fuel, burning is abundant, and the consumption energy is few.
6, equipment operation is simple, high degree of automation, saves labor.Baking initially enters full-automatic control since click
System concentrates feed, automatic feed, automatic adjustment oxygen supply, temperature automatically controlled, self-skimming, realizes " one-touch " operation and operation
Stablize, precisely.By taking the baking workshop of 50 barns as an example, traditional coal heating flue-cured tobacco 15 people of needs or so (including it is roasting
Cigarette master worker), the normal operation at a workshop could be maintained, and biological particles combustion apparatus flue-cured tobacco provided by the invention is taken,
5 people or so are only needed, the efficiency than the baking of traditional coal heating improves 3 times or more.
7, energy consumption and baking cost are reduced.Why more at low cost than baked by using fire coal biomass fuel tobacco flue-curing cost is, and one
It is efficiency of combustion and heat exchanger effectiveness greatly improves that energy consumption is caused to be greatly lowered;Second is that accurately automatic feeding system avoids
The waste of redundancy fuel in heating and cooling process;Third, highly integrated automated control technology has greatly saved human cost.It adopts
The baking direct cost that 1 kilogram of tobacco leaf is dried with traditional coal heating equipment at least wants 2.26 yuan, and takes raw in the present invention
Material grains fuel barn dries only 1.73 yuan or so of the baking direct cost of 1 kilogram of dry tobacco leaf, and per kilogram tobacco leaf saves 0.54
Member often cheats flue-cured tobacco 312 yuan or so of expense capable of saving fuel.In addition, automatic ignition of the present invention, heating rate are steady, temperature control
Stablize, automatic adjustment temperature, auto feed (adding once per 48h), dry tobacco leaf quality preferable (orange cigarette rate is high), remove automatically
Slag, the utilization rate of slag ash are high (containing elements such as abundant nitrogen, phosphorus, potassium, can be used as fertilizer returning to the field).
8, emission reduction effect is notable.In the Tobacco Leaf Curing of the present invention, basic smoke dust, sulphur is nitrogen discharged low, carbon monoxide,
Hydrogen sulfide zero-emission, non-secondary pollution, baking shop environment is clean, pollution is low.Biological particles combustion apparatus toasts and fire coal
The exhaust emissions comparison of heating equipment baking is as shown in table 1.
Table 1
Heating equipment provided by the invention is adapted to roasting with original metal barn (coal heating), advanced composite material (ACM) heat supply
The matching of the different types barns such as room, biomass heat supply bulk curing barn and biomass heat supply movable type board house structure barn.
Biomass granule fuel heating equipment provided by the invention detects the conclusion obtained through the Central China University of Science and Technology:Burning
The inspection of efficiency, maximum output thermal power, heat exchange efficiency, hopper capacity, feed, igniting, fin radiator, control system etc.
It is all qualified to survey result.
As shown in Fig. 1 and Fig. 9, Figure 10, the present invention provides a kind of biomass granule fuel heating equipment, the heating equipment
It is described to change including combustion furnace 1, heat exchanger 2, the concentration feeding system 3 and barn 4 for providing for combustion furnace biomass granule fuel
Hot device 2 is used to be connected to 14 one end of horizontal converter nose of combustion furnace 1, and the barn 4 includes for hot cell 41, and the heat exchanger 2 is arranged
In for hot cell 41, the combustion furnace 1 and concentration feeding system 3 are arranged outside barn 4;The concentration feeding system 3 is for being
More than two combustion furnaces 1, which are concentrated, provides biomass granule fuel, and the concentration feeding system 3 includes the Material sucking machine containing vacuum pump
31, storage vat 32, two or more aspirating air pipe 33, two or more charging line 34, auger feed mechanism 35, feeding distribution connect
Head, more than two solenoid valves 36, more than two vacuum hoppers 37 and more than two weight valves 38;The storage vat 32 is for concentrating
Biomass granule fuel is stored, its bottom is provided with auger feed mechanism 35 and for granular fuel to be sent into different feedings
The feeding distribution joint of pipeline 34, the vacuum hopper 37 are arranged at the top of combustion furnace for being that the hopper 11 in combustion furnace supplies
Material, the solenoid valve 36 are arranged on the aspirating air pipe 33 that vacuum hopper 37 is connect with vacuum pump, and the setting of the weight valve 38 exists
37 bottom of vacuum hopper;When solenoid valve 36 on vacuum pump startup and certain or a plurality of aspirating air pipe 33 is opened, make vacuumizing
Under, the weight valve 38 of 33 corresponding vacuum hopper of aspirating air pipe, 37 bottom remains closed, and biomass granule fuel is through phase
The charging line answered is sent into the vacuum hopper 37;When the solenoid valve 36 is closed, the weight valve 38 after vacuum is unloaded true
It opens under the self gravitation effect of biomass granule fuel in empty hopper 37 and is fed from the hopper 11 in trend combustion furnace.
In a kind of specific embodiment, the heating equipment is tobacco flue-curing heating equipment, and the barn is also
Including hanging smoke-box 42 and positioned at for hot cell 41 and the insulated wall 43 between smoke-box 42 is hung, and being additionally provided with high circulated at low velocity in barn
Wind turbine 46 is for driving air for being circulated between hot cell 41 and extension smoke-box 42.
In a kind of specific embodiment, the combustion furnace includes converter nose 14, and the converter nose 14 includes horizontal setting
Converter nose 141 and the outer converter nose 142 of truncated cone-shaped, form hollow ventilated area 146, the interior stove in cylinder between interior converter nose and outer converter nose
The burner hearth of combustion furnace described in main composition inside mouth, in Horizontal cylinder the bottom of converter nose offer ventilation hole for be biomass
Grain fuel combustion provides air;Interior converter nose axial direction one end is connect with the bottom of burning feed pipe 13, and the axial other end is for being inserted into
In the heat exchanger 2 being connect with combustion furnace 1;It is miner diameter end that outer converter nose, which is equally used for being inserted into axial one end in the heat exchanger 2,
1421, outer converter nose is its bigger diameter end 1422 close to axial one end of burning feed pipe, and the inner wall of outer converter nose miner diameter end 1421 arrives
The circumferential weld width d of radial distance, that is, bocca periphery between interior converter nose outer wall is 0.8~5mm.
In a kind of specific embodiment, the combustion furnace includes burning air supply system 15, the burning air supply system
15 include small wind turbine 151, air blower 152 and the matching air box 153 being sequentially connected in series, and the small wind turbine is charged pool power supply and wind turbine work(
For rate in the wind turbine of 10~200w, the air blower 152 is power of fan more than small power of fan and for providing master for combustion furnace
The wind turbine for the fresh air wanted, the matching air box 153 be used for distribute fresh air and it include multiple parallel connections outlet, it is described more
The outlet of a parallel connection is connect with main ajutage 154, discharge nozzle anti-backfire ajutage 155 and other purposes ajutages 156 respectively.
In a kind of specific embodiment, the combustion furnace includes slag removal mechanism 16, and the slag removal mechanism includes level
The slagging-off of setting with tooth push rod 162, for slagging-off with tooth push rod provide with the slagging-off motor 161 of passing power and gear 165, be arranged
It is described in the slagging-off rod bush 163 with tooth push rod radial outside that removes the gred, the push rod directive wheel 164 being oriented to tooth push rod for slagging-off
The axial one end of slagging-off with tooth push rod is arranged in the burner hearth that converter nose 141 is formed in the cylinder by horizontal setting, slagging-off band tooth
The axial other end of push rod is arranged outside burner hearth and pushes away slag movement by the level of controller control push rod.
In a kind of specific embodiment, the heat exchanger 2 includes the secondary combustion chamber 21 for being located at lower part, is arranged two
In secondary combustion chamber and for the deduster 22 of flame and high temperature fume dust removal, for after dedusting high-temperature flue gas and air progress
The radiator 23 of heat exchange and the chimney 24 that heat exchanger is discharged for the flue gas after heat exchange;The deduster 22 includes connecting
Connect the converter nose 14 and for will the flame and high-temperature flue gas that are laterally sprayed in converter nose introduce fume inlet passage 225 in heat exchanger,
Two axial directions for being connected to 225 end of fume inlet passage are arranged at the cylindrical dedusting main body 222 of vertical direction, are located at two circles
The intersubjective flame kicker baffle 221 of cylindricality dedusting and top in each cylindrical dedusting main body and with cylinder
The frustum structure 223 of dedusting main body coaxial arrangement, the flame kicker baffle 221 are vertically arranged and are used for the flame and height
Warm flue gas from being introduced tangentially into two cylindrical dedusting main bodys, the bigger diameter end of the frustum structure 223 in upper and miner diameter end under,
Its bigger diameter end is connect with cylindrical dedusting body seal so that flame and high-temperature flue gas after fume inlet passage enters deduster,
It is rotated under the guiding role of flame kicker baffle in cylindrical dedusting main body, then from the center taper through-hole shape of frustum structure
At flue gas rising passway 224 in outflow deduster and enter the radiator 23.
In a kind of specific embodiment, high low speed circulating fan 46 drives air from 43 top of insulated wall for hot cell
Return air inlet 44 enters for hot cell 41, and is flowed out from 43 bottom of insulated wall for hot cell 41 for hot cell air outlet 45 and enter and hang smoke-box
42;The extension smoke-box 42 is provided with extension smoke-box gate 421 and is passed in and out for personnel and material, and cold wind import is additionally provided in the barn
47。
The present invention provides a kind of containing above-mentioned combustion furnace, heat exchanger and the heating equipment for concentrating feeding system.The present invention carries
The heating equipment of confession realizes the repeated combustion of biomass granule fuel, keeps the burnings such as fuel, smoke tar, dust abundant, after burning
Noresidue efficiently solves the tar generated during biomass combustion, cinder blocking heat-exchanger, tail gas residue pollution environment
And key issues of etching apparatus, significantly improve the utilization rate of biomass energy calorific value.The heating equipment at least has such as
Lower feature.
1, safety:There is open fire generation using coal as fuel, it is possible to which leakage fire causes tobacco leaf to burn, and leads to that tobacco grower's is huge
Big loss;And in the present invention combustion furnace be arranged outside barn, heat exchanger be sealingly disposed in barn in hot cell, in barn
It hangs smoke-box and is kept apart by insulated wall for hot cell, the open fire generated in combustion furnace is totally-enclosed in combustion furnace and heat exchanger, thus
The consequence of tobacco leaf burning is not will produce.
2, environmentally friendly:Entire heating equipment under operation, is emerged, sulphur is nitrogen discharged low, an oxygen without any dust, flue gas
Change carbon and hydrogen sulfide zero-emission, baking shop environment is clean, pollution-free.And coal combustion especially dissipate coal baking when contain hook fire add
The program of coal has the drift of a large amount of coal ash dirt to raise and SO2Release influences and pollutes environment.
3, the baked goods of high quality:The concentration feeding system of the present invention, burning air supply system, is removed burning feed mechanism
It includes helical blade feeder, helical-blade that slag mechanism etc., which is in the automated system of program control, such as burning feed mechanism,
Piece feeder is set as automatic open close by program, and firepower size in combustion furnace is determined according to its opening and closing time, and then determines whole
The real-time heating load of a heating equipment so that dry-bulb temperature and wet-bulb temperature and heating-up time, steady warm time in barn etc.
The equal controllable precise of parameter.Wherein without unstable temperature change fluctuated, cold dust and hot dust etc. will not be caused without using
It is good to bake the quality of tobacco come for the low quality tobacco leaf of value.In addition, the tobacco flue-curing program of automation standard setting can be to avoid
Many maloperations and bring waste product, and so that the quality of tobacco leaf is more well-balanced more preferable.
4, saving of work and time:Full-automatic setting can save a large amount of manual labor.Whole process generally only needs manpower will be biological
Matter granular fuel be sent into concentrate feeding system storage vat in (process also can by machinery complete), and the clinker of after-flame from
It is cleared in the breast hole of heat exchanger.Concentrate feeding system that biological particles are sent into vacuum material from storage vat 32 automatically
In bucket 37, biological particles are sent into from vacuum hopper 37 in hopper 11 automatically after feed, burning air supply system automatic adjustment
Clinker in burner hearth is pushed into heat exchange by the air capacity being sent into combustion furnace, slag removal mechanism with a small amount of not sufficiently combusted clout automatically
Carry out second-time burning in device, burn in burner hearth and heat exchanger in the high-temperature flue gas that generates of second-time burning after dedusting in radiator
To being discharged from chimney after the circulation air heating in barn, the high low speed circulating fan 46 in barn promotes the heat in barn empty at place
Gas circulates and carries out heated baking to tobacco in smoke-box 42 from flowing into hang for hot cell 41, and the temperature and humidity hung in smoke-box is same
Sample is also used and is automatically controlled.These processes are all automatic to be carried out, and a large amount of manpower and time are saved.And people is avoided to be fired with burning
Being in direct contact for material, is conducive to the health of tobacco grower.
5, energy-efficient:The present invention changes the mode of the suspension combustion in the b of combustion chamber in first technology, is changed to biomass
Grain, which is controllably deposited in converter nose, to burn, then by adjusting the burning air supply system of the present invention so that its efficiency of combustion is by 82%
It is further increased to 87%, the raising of efficiency of combustion generates remarkable result to energy saving of system.In addition, the present invention is good in exhaust emissions
In the case of good and combustion furnace noncoking, not slagging, it is not required to provide strong impetus and energy so that biological particles suspension combustion
Amount consumption, further reduced the energy consumption of entire combustion furnace and heating equipment.
6, the service life of equipment is long:The heating equipment uses the steel of special substance, has high temperature resistant, anticorrosion, prolongs
The features such as long life;Equipment surface application and surface cleanness grade is set to reach as defined in GB/T 8923 through blasting treatment
Sa2.5 grades of requirements, surfaces externally and internally carry out three sprayings using high temperature, epoxy zinc rich primer, and finishing coat uses electrostatic spraying (baking vanish),
This technique has the characteristics that high temperature resistant, resistant to strong corrosion, prolongs the service life, and the service life of the heating equipment generally can reach 12 years
More than, it is more durable than other heating equipments.
7, equipment is applied widely:The heating equipment can be accomplished to dock and combine closely easily with all kinds of barns, and should
Heating equipment is suitble to move, and such as certain cigarette district former years can plant cigarette but this year cannot plant, and must change to another place kind, then can be with
A whole set of biomass granule fuel heating equipment is moved to other flue-cured tobacco area to toast.In addition, heat supply provided by the invention is set
It is standby to be also used as drying equipment, including medicinal material, paddy, honeysuckle, day lily of various agricultural product etc..
The foregoing is only a preferred embodiment of the present invention, is not intended to restrict the invention, for the skill of this field
For art personnel, the invention may be variously modified and varied.All within the spirits and principles of the present invention, any made by repair
Change, equivalent replacement, improvement etc., should all be included in the protection scope of the present invention.