CN204922945U - Multistage biomass combustion device of precipice formula - Google Patents
Multistage biomass combustion device of precipice formula Download PDFInfo
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- CN204922945U CN204922945U CN201520560892.0U CN201520560892U CN204922945U CN 204922945 U CN204922945 U CN 204922945U CN 201520560892 U CN201520560892 U CN 201520560892U CN 204922945 U CN204922945 U CN 204922945U
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Abstract
The utility model discloses a multistage biomass combustion device of precipice formula, including a plurality of combustion chambers of range upon range of setting, the combustion chamber all includes furnace body, feed arrangement and fluidized -bed combustion ware, and wherein, the fluidized -bed combustion ware includes inner shell, shell and first air -blower, and inner shell and shell setting form the air cavity between inner shell and shell in the furnace body, be equipped with the gas pocket on the lateral wall of inner shell, the first air -supply line that is provided with dust discharge pipe on the shell and links to each other the air cavity with first air -blower, dust discharge pipe all with the furnace body of lower floor combustion chamber on row's ash mouthful intercommunication, a plurality of combustion chambers make it fully burn the combustion efficiency maximize to multiple biomass fuel, the flue gas preheats the abundant burning of guaranteeing fuel in getting into upper combustion chamber, and energy -conserving high -efficient, biomass ash concentrates and discharges, has solved its difficult exhaust problem of easily building bridge, send into the air and make biomass fuel seethe through first air -blower, make its and air intensive mixing, avoid the coking, guarantee biomass fuel's abundant burning, improve combustion efficiency.
Description
Technical field
The utility model relates to biomass boiler equipment technical field, particularly a kind of precipice formula multi-stage biological matter burner.
Background technology
Coal-burning boiler coal consumption is large, seriously polluted, do not meet the strategy of China's sustainable development, therefore, adopt the boiler of clear energy sources to replace existing coal-burning boiler and become the focus studied at present, and the biomass boiler utilizing forest and agricultural biomass to use as boiler oil due to have environmentally friendly, the feature such as can to regenerate, to saving conventional energy resource, optimize China's energy resource structure, alleviate environmental pollution and have positive effect, and because its price is low and operating cost is low, obtains the accreditation of user and promoted.
In prior art, biomass combustion furnace is generally horizontal single combustion chamber, because living beings are various in style, the ash fusion point of the living beings of different cultivars, ash content, moisture, burning time and calorific capacity are different again, the combustion furnace of this single combustion chamber can only burn the biomass fuel of single variety, living beings are used to cause huge obstacle in a large number to industry, effectively can not utilize biomass fuel, and in combustion, biomass fuel is in static state, the biomass fuel being positioned at bottom is difficult to fully contact with air, and easily burning is insufficient, finally causes coking.
Therefore, how to provide a kind of biomass combustion furnace, the biomass fuel of different cultivars can be used, effectively utilize various biomass fuel, and biomass fuel Thorough combustion can be ensured, avoid coking, become the important technological problems that those skilled in the art are urgently to be resolved hurrily.
Utility model content
In view of this, the utility model provides a kind of precipice formula multi-stage biological matter burner, to reach the biomass fuel that can use different cultivars, effectively utilizes various biomass fuel, and biomass fuel Thorough combustion can be ensured, avoid the object of coking.
For achieving the above object, the utility model provides following technical scheme:
A kind of precipice formula multi-stage biological matter burner, comprise stacked setting from down to up and the multiple combustion chambers be communicated with successively, each described combustion chamber includes:
Body of heater;
Be arranged on the feed arrangement on body of heater, the discharging opening of described feed arrangement is communicated with the burner hearth of described body of heater;
To be arranged in described burner hearth of the furnace body and the boiling burner be positioned at below described discharging opening, comprise inner casing, shell and the first air blast, described inner casing and described shell are arranged in described body of heater, described inner casing is nested in described shell and also and between described shell forms air cavity, the sidewall of described inner casing offers multiple pore, described shell is provided with ash releasing tube and the first blast pipe, described first blast pipe one end is communicated with described air cavity, and the other end is connected with described first blower outlet;
The body of heater of orlop combustion chamber is provided with ash discharging hole, and the ash releasing tube of each described boiling burner is all communicated with described ash discharging hole;
The superiors combustion chamber is provided with the smoke exhaust pipe for being discharged by flue gas.
Preferably, also comprise flue gas heat-exchange unit, described flue gas heat-exchange unit is arranged on the top of the superiors combustion chamber, and its gas approach is communicated with described smoke exhaust pipe, and exhanst gas outlet is connected with air-introduced machine.
Preferably, also comprise the second air blast, described second air blast is connected with each combustion chamber by the second blast pipe, described second blast pipe comprise air inlet main pipe and with each combustion chamber air intake arm one to one, described air inlet main pipe one end is communicated with the air outlet of described air blast, and the other end is connected with each air intake arm.
Preferably, described air intake arm is provided with air inlet valve near one end of described combustion chamber.
Preferably, described precipice formula multi-stage biological matter burner comprises bottom combustion chamber, combustion chamber, middle level and high-rise combustion chamber, the furnace temperature of described bottom combustion chamber is 500 DEG C ~ 600 DEG C, the furnace temperature of combustion chamber, described middle level is 700 DEG C ~ 800 DEG C, and the furnace temperature of described high-rise combustion chamber is 1100 DEG C ~ 1400 DEG C.
Preferably, the combustion space of described bottom combustion chamber, combustion chamber, described middle level and described high-rise combustion chamber increases successively.
Preferably, described feed arrangement comprises hopper and conveying worm, and the discharging opening of described conveying worm is communicated with the burner hearth of described body of heater, and described hopper comprises feeding-passage and heat exchanging part, feeding-passage has import and outlet, and described outlet is communicated with described conveying worm feeding mouth; Described heat exchanging part is wrapped in the outside of described feeding-passage, is provided with gas approach and exhanst gas outlet, and described gas approach is communicated with described smoke exhaust pipe.
Preferably, the bottom near described conveying worm in described feeding-passage is provided with filtering device, and described filtering device comprises filter net device and magnet filter.
Preferably, the discharging opening of described feed arrangement is provided with fireproof tempering device, described fireproof tempering device comprises lifting portion and cover plate, described lifting portion is hollow and two ends all have the tubular of opening, its one end is communicated with described feed arrangement discharging opening, the other end is hinged with described cover plate, and described lifting portion is inclined upwardly and meets 30 °≤α≤50 ° with the angle α of horizontal plane.
Preferably, the angle β of described feed arrangement and horizontal plane meets 8 °≤β≤15 °, and described lifting portion tilts upward away from the opening of one end of described feed arrangement, and the angle γ of its place plane and described horizontal plane meets 30 °≤γ≤50 °.
As can be seen from technique scheme, the precipice formula multi-stage biological matter burner that the utility model provides, comprise stacked setting from down to up and the multiple combustion chambers be communicated with successively, each described combustion chamber includes body of heater, feed arrangement and boiling burner, wherein, feed arrangement is arranged on body of heater, and the discharging opening of feed arrangement is communicated with the burner hearth of body of heater; Boiling burner to be arranged in burner hearth of the furnace body and to be positioned at below discharging opening, comprise inner casing, shell and the first air blast, inner casing and shell are arranged in body of heater, inner casing is nested also and between shell forms air cavity in the enclosure, the sidewall of inner casing offers multiple pore, shell is provided with ash releasing tube and the first blast pipe, first blast pipe one end is communicated with air cavity, and the other end is connected with the first blower outlet; The body of heater of orlop combustion chamber is provided with ash discharging hole, and the ash releasing tube of each boiling burner is all communicated with ash discharging hole; The superiors combustion chamber is provided with the smoke exhaust pipe for being discharged by flue gas; Owing to having multiple combustion chamber, by the furnace temperature of control combustion room, can carry out Thorough combustion to different types of biomass fuel, avoid coking, ensure that efficiency of combustion is maximum; The high-temperature flue gas that lower floor's combustion chambers burn produces enters in combustion chamber, upper strata, contribute to the raising of combustion chamber, upper strata furnace temperature, and then ensure the quick Thorough combustion of combustion chamber, upper strata endogenous substance fuel, save the energy, raise the efficiency, and the biomass ash that each combustion chamber generates all is pooled to that orlop combustion chamber is unified discharges, solves biomass ash and easily to build bridge difficult problem of discharging; When biomass fuel to enter via pay-off in the inner casing of boiling burner, the thrust of mixing merga pass air-flow to boiling burner feeding air and biomass fuel by the first air blast makes biomass fuel seethe in boiling burner, thus biomass fuel is in combustion dynamically fully mix with air, thus reach the generation avoiding coking phenomenon, ensure the Thorough combustion of biomass fuel, improve the object of ignition temperature and efficiency.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of precipice formula multi-stage biological matter burner in the utility model embodiment;
Fig. 2 is the internal structure schematic diagram of precipice formula multi-stage biological matter burner combustion chamber in the utility model embodiment;
Fig. 3 is the structural representation of hopper in precipice formula multi-stage biological matter burner in the utility model embodiment;
Fig. 4 is the structural representation of filtering device in precipice formula multi-stage biological matter burner in the utility model embodiment;
Fig. 5 is the structural representation of fireproof tempering device in precipice formula multi-stage biological matter burner in the utility model embodiment.
Detailed description of the invention
The utility model provides a kind of precipice formula multi-stage biological matter burner, to reach the biomass fuel that can use different cultivars, effectively utilizes the object of various biomass fuel.
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1 and Fig. 2, Fig. 1 is the structural representation of precipice formula multi-stage biological matter burner in the utility model embodiment; Fig. 2 is the internal structure schematic diagram of precipice formula multi-stage biological matter burner combustion chamber in the utility model embodiment.
A kind of precipice formula multi-stage biological matter burner that the utility model provides, comprise stacked setting from down to up and the multiple combustion chambers be communicated with successively, each described combustion chamber includes body of heater, feed arrangement and boiling burner.
Wherein, feed arrangement is arranged on body of heater, and the discharging opening of feed arrangement is communicated with the burner hearth of body of heater; Boiling burner to be arranged in burner hearth of the furnace body and to be positioned at below discharging opening, comprise inner casing 11, shell 12 and the first air blast 15, inner casing 11 and shell 12 are arranged in body of heater, inner casing 11 is nested in shell 12 and also and between shell 12 forms air cavity, the sidewall of inner casing 11 offers multiple pore 10, shell 12 is provided with ash releasing tube 13 and first blast pipe 14, first blast pipe 14 one end is communicated with air cavity, the other end is connected with the first air blast 15 air outlet; The body of heater of orlop combustion chamber is provided with ash discharging hole, and the ash releasing tube 13 of each boiling burner is all communicated with ash discharging hole; The superiors combustion chamber is provided with the smoke exhaust pipe for being discharged by flue gas.
Compared with prior art, the precipice formula multi-stage biological matter burner that the utility model provides, in use, owing to having multiple combustion chamber, can by the furnace temperature of control combustion room, Thorough combustion can be carried out to different types of biomass fuel, avoid coking, ensure that efficiency of combustion is maximum; The high-temperature flue gas that lower floor's combustion chambers burn produces enters in combustion chamber, upper strata, contribute to the raising of combustion chamber, upper strata furnace temperature, and then ensure the quick Thorough combustion of combustion chamber, upper strata endogenous substance fuel, save the energy, raise the efficiency, and the biomass ash that each combustion chamber generates all is pooled to that orlop combustion chamber is unified discharges, solves biomass ash and easily to build bridge difficult problem of discharging; When biomass fuel to enter via pay-off in the inner casing 11 of boiling burner, the thrust of mixing merga pass air-flow to boiling burner feeding air and biomass fuel by the first air blast 15 makes biomass fuel seethe in boiling burner, thus biomass fuel is in combustion dynamically fully mix with air, thus reach the generation avoiding coking phenomenon, ensure the Thorough combustion of biomass fuel, improve the object of ignition temperature and efficiency.
High-temperature flue gas is directly got rid of, not only can waste a part of heat energy, reduce the thermal efficiency of boiler, also can to environment, therefore, in order to optimize technique scheme further, in the utility model embodiment, precipice formula multi-stage biological matter burner also comprises flue gas heat-exchange unit 4, flue gas heat-exchange unit 4 is arranged on the top of the superiors combustion chamber, its gas approach is communicated with smoke exhaust pipe, exhanst gas outlet is connected with air-introduced machine, before flue gas is discharged, by heat exchanger, high-temperature flue gas preheating is utilized, while reduction boiler emission, improve the thermal efficiency of boiler.
In the utility model embodiment, precipice formula multi-stage biological matter burner also comprises the second air blast 5, second air blast 5 is connected with each combustion chamber by the second blast pipe, second blast pipe comprise air inlet main pipe and with each combustion chamber air intake arm one to one, air inlet main pipe one end is communicated with the air outlet of air blast 5, the other end be connected with each air intake arm.
Due to the ash fusion point of its biomass fuel used of different combustion chambers, moisture, burning times etc. are all not identical yet, so its air quantity delivered needed is also different, can both burn fully to make each biomass fuel, improve efficiency of combustion, avoid the generation of coking, in the utility model embodiment, air intake arm is provided with air inlet valve near one end of combustion chamber, in use, by adjusting the aperture of air inlet valve, the air quantity entering combustion chamber can be controlled, while the biomass fuel in each combustion chamber provides sufficient air, furnace temperature is maintained in rational scope.
Precipice formula multi-stage biological matter burner can arrange the combustion chamber of varying number as required, in the utility model embodiment, precipice formula multi-stage biological matter burner comprises bottom combustion chamber 1, combustion chamber, middle level 2 and high-rise combustion chamber 3, the furnace temperature of bottom combustion chamber 1 is 500 DEG C ~ 600 DEG C, the furnace temperature of combustion chamber, middle level 2 is 700 DEG C ~ 800 DEG C, the furnace temperature of high-rise combustion chamber 3 is 1100 DEG C ~ 1400 DEG C, wherein, bottom combustion chamber 1 be mainly used in burning fusing point low, the low forms of life matter particle that calorific value is low, as straw etc., its Control for Kiln Temperature is at 500 DEG C ~ 600 DEG C, the flue gas that burning generates rises and enters in combustion chamber, middle level 2, combustion chamber, middle level 2 is mainly used in the intermediate biological particles that fusing point is higher, calorific value is higher that burns, and as stalk etc., its Control for Kiln Temperature is at 700 DEG C ~ 800 DEG C, and the flue gas that burning generates rises and enters in high-rise combustion chamber 3, and high-rise combustion chamber 3 is mainly used in burning the advanced bio matter particle that fusing point is high, calorific value is high, as wood chip etc., its furnace temperature needs to control between 1100 DEG C ~ 1400 DEG C, finally, the biomass ash generated that burns in combustion chamber, middle level 2 and high-rise combustion chamber 3 all drops in bottom combustion chamber 1, and is discharged by the ash discharging hole of bottom combustion chamber 1.
Due in use, the flue gas that lower floor combustion chamber produces enters combustion chamber, upper strata, in order to avoid the pressure change in combustion chamber, upper strata is fluctuated greatly, affect the efficiency of combustion of biomass fuel, in the utility model embodiment, the combustion space of bottom combustion chamber 1, combustion chamber, middle level 2 and high-rise combustion chamber 3 increases successively, by progressively expanding the volume of combustion chamber, upper strata, after making the flue gas in lower floor combustion chamber enter combustion chamber, upper strata, pressure in combustion chamber, upper strata can not sharply raise, and ensure that the stable of pressure in the burner hearth.
Feed arrangement can adopt various structures, such as ribbon conveyer, chain-linked conveyer etc., in the utility model embodiment, refer to Fig. 3, Fig. 3 is the structural representation of hopper in precipice formula multi-stage biological matter burner in the utility model embodiment, feed arrangement comprises hopper 7 and conveying worm 6, the discharging opening of conveying worm 6 is communicated with the burner hearth of body of heater, hopper 7 comprises feeding-passage 701 and heat exchanging part, feeding-passage 701 has import and outlet, and outlet is communicated with conveying worm 6 feeding mouth; Heat exchanging part is wrapped in the outside of feeding-passage 701, and be provided with gas approach and exhanst gas outlet, gas approach is communicated with smoke exhaust pipe; Conveying worm 6, while conveying, can stir biomass fuel, be broken up by the fuel wherein lumpd, can reduce the generation of coking phenomenon in combustion process to a certain extent.
In use, biomass fuel enters feeding-passage 701 from charging aperture, and fall along feeding-passage 701, in dropping process, with the boiler smoke generation heat exchange in the heat exchanging part be wrapped in outside feeding-passage 701, the high-temperature flue gas of being discharged by boiler and biomass fuel carry out heat exchange, oven dry heating is carried out to biomass fuel, it is made to catch fire easily, remove moisture content, sufficient combustion, the generation of coking phenomenon can be avoided, meanwhile, flue-gas temperature reduces, heat recovery, the preheating of biomass fuel contributes to the raising of boiler hearth temperature, and then improve the thermal efficiency of boiler.
Heat exchanging part can adopt various structures, in the utility model embodiment, heat exchanging part comprises housing 702 and fin 703, wherein, housing 702 is arranged on outside feeding-passage 701, form heat exchanging interlayer between housing 702 and feeding-passage 701, gas approach and exhanst gas outlet are all arranged on housing 702; Fin 703 has multiple, staggered is arranged in heat exchanging interlayer, like this, flue gas is entering after in radiating part, due to the fin 703 be crisscross arranged, the flowing velocity of flue gas can be effectively reduced, make it to carry out sufficient heat exchange with the biomass fuel in feeding-passage 701, improve the utilization ratio to fume afterheat.
In order to avoid scattering and disappearing of heat, in the utility model embodiment, the outer wall of housing 702 being provided with heat-insulation layer, by arranging heat-insulation layer, the loss that fume afterheat is brought to external radiation by housing 702 can being reduced, improve the utilization rate of fume afterheat; Heat-insulation layer can adopt multiple material to make, such as, and asbestos fibre heat-insulation layer or fiberglass insulation.
The gas approach of heat exchanging part can directly be communicated with the smoke exhaust pipe of boiler, and also can be communicated with the smoke exhaust pipe of boiler by air-supply arrangement, in the utility model embodiment, in order to raising efficiency, gas approach is connected by air-introduced machine with smoke exhaust pipe.
In order to avoid the harmful substance heat exchanging portion in flue gas causes corrosion at housing 702 and fin 703, affect the service life of heat exchanging part, in the utility model embodiment, gas approach is provided with filtrating equipment of flue gas.
Feeding-passage 701 can adopt various structures, such as straight-tube shape etc., in the utility model embodiment, in order to improve heat exchange efficiency, feeding-passage 701 have employed three stage structure, comprise the inducer be connected successively, middle diffuser and converging portion, the diameter of middle diffuser is greater than inducer diameter, converging portion is reduced diameter from the one end be connected with middle diffuser, like this, in the dropping process of biomass fuel, the middle diffuser that diameter is larger is entered after inducer, biomass fuel can be made fully to scatter, make the pre-heating drying of biomass fuel more thorough, then, biomass fuel enters boiler furnace burning after converging portion converges.
Biomass fuel too fast meeting of falling in feeding-passage 701 causes with flue gas heat exchange insufficient, pre-heating drying effect is undesirable, therefore, in order to optimize technique scheme further, in a kind of embodiment of the utility model, the inwall of middle diffuser is multiple to the centroclinal downward buffer board of middle diffuser every being crisscross arranged between the upper and lower, like this, what biomass fuel can replace in dropping process falls on each buffer board, the falling speed of biomass fuel can be effectively reduced, make it to carry out sufficient heat exchange if having time with flue gas, improve the utilization rate of fume afterheat.
Certainly, above-mentioned fuel buffer unit also can adopt other structure, and such as, in the another kind of embodiment of the utility model, the inwall of middle diffuser is provided with the slideway under screw, ways-end is towards converging portion.
Preferably, in order to further improve the drying effect of biomass fuel pre-heating drying device, in the utility model embodiment, the top of middle diffuser is provided with blower fan, the air circulation in middle diffuser can be strengthened by blower fan, further improve the drying effect of biomass fuel.
Bulk in biomass fuel and irony impurity easily cause coking and the generation of the phenomenon such as to get stuck, harmful effect is brought to the normal use production of biomass combustion device, therefore, in order to optimize technique scheme further, in the utility model embodiment, refer to Fig. 4, Fig. 4 is the structural representation of filtering device in precipice formula multi-stage biological matter burner in the utility model embodiment, bottom near conveying worm 6 in feeding-passage 701 is provided with filtering device, and filtering device comprises filter net device 16 and magnet filter 17.
By installing filter net device 16 and magnet filter 17 in hopper 7 additional, can when charging, the bulk impurity in filtering fuel and irony impurity, effectively avoid the generation of coking and the phenomenon that gets stuck, and ensures that the normal table of biomass combustion device runs.
Magnet filter 17 can adopt various structures, and such as, in a kind of embodiment of the utility model, magnet filter 17 comprises one or more and is fixed on annular magnet on hopper 7 inwall.
Certainly, magnet filter 17 can be arranged on above filter net device 16, also can be arranged on the below of filter net device 16, and in the utility model embodiment, magnet filter 17 is arranged on the below of filter net device 16.
When magnet filter 17 is this permanent magnet of above-mentioned annular magnet, although the irony impurity in fuel can be removed, but because its magnetic unanimously exists, be not easy in the future for the cleaning of these impurity, especially when in impurity containing when being similar to the sharp object of iron nail, easily cleaning personnel are damaged, therefore, in order to optimize such scheme further, in the another kind of embodiment of the utility model, magnet filter 17 is electromagnet, comprise iron core and be wrapped in the outer and conductive winding be connected with power supply of iron core, wherein, iron core needs to use demagnetization, and soft iron or silicon steel material make faster, by adopting the electromagnet of this structure, when clearing up the irony impurity on magnet filter 17, power supply and conductive winding being disconnected to make magnet filter 17 lose magnetism, irony impurity attached thereto falls naturally, while being convenient to cleaning and collection, avoid the injury to cleaning personnel.
Preferably, in order to ensure the filter effect of electromagnet, in the utility model embodiment, above-mentioned magnet filter 17 is provided with multiple, is uniformly distributed along hopper 7 circumference.
Filter net device 16 can be made up of a screen pack, also can be made up of multiple screen pack as required, in a kind of embodiment of the utility model, in order to improve the filter effect of filter net device 16, filter net device 16 comprises multiple screen pack increased successively along material falling direction order number.By this multiple filtration structure, more careful screening can be carried out to fuel, avoid the generation of coking phenomenon.
Further, in the utility model embodiment, filter net device 16 comprises the first screen pack and the second screen pack, and the order number of the first screen pack is 1-4 order, and the order number of the second screen pack is 8-10 order.
Above-mentioned its filter effect of filter net device 16 is certain, when different user demands, underaction, adaptability is poor, therefore, in the another kind of embodiment of the utility model, filter net device 16 comprises main filter screen and the secondary filter screen with the stacked setting of main filter screen, and secondary filter screen is connected with the extension adjustment device be positioned at outside hopper 7.Like this, secondary filter screen and main filter screen can be driven to misplace by extension adjustment device, to reach the object changing filter net device 16 order number, or directly secondary filter screen is taken away main filter screen position, only use main filter screen to filter, by this structure, can when not to filter net device 16 structure be changed, change the filter effect of filter, add the flexibility of filter greatly, different user demands can be met.
Extension adjustment device can adopt various structures to realize, such as chain telescoping mechanism, the expansion bend etc. that intersects, and in the utility model embodiment, extension adjustment device comprises support and piston cylinder, and wherein, support is fixed on hopper 7 outer wall; The cylinder body of piston cylinder is fixed on support, and the piston rod of piston cylinder is connected with the secondary filter screen in hopper 7 through the flat groove on hopper 7 wall, and this extension adjustment device structure is simple, is convenient to make and safeguards.
In existing biomass combustion device, the discharge outlet of feed arrangement does not arrange any firebreak device, in the middle of practical application, easy generation tempering, cause biomass fuel at the discharging opening of feed arrangement, even just take fire in feed arrangement, affect the thermal efficiency of boiler, also safety problem may be there is, therefore, in order to optimize technique scheme further, in the utility model embodiment, refer to Fig. 5, Fig. 5 is the structural representation of fireproof tempering device in precipice formula multi-stage biological matter burner in the utility model embodiment, the discharging opening of feed arrangement is provided with fireproof tempering device, fireproof tempering device comprises lifting portion 8 and cover plate 9, lifting portion 8 is hollow and two ends all have the tubular of opening, its one end is communicated with feed arrangement discharging opening, the other end is hinged with cover plate 9, lifting portion 8 is inclined upwardly and meets 30 °≤α≤50 ° with the angle α of horizontal plane.
By arranging a lifting portion 8 raised up at feed arrangement discharging opening, and in the outlet in lifting portion 8, cover plate 9 is set, in use, the lifting portion 8 of biomass fuel through raising up, wash open cover plate 9 parabolically shape be sprinkled in boiling burner, in the dynamic process fallen, fully contact with air, sufficient combustion, efficiency of combustion is high, and ignition temperature is high, tail-off time is short, and due to lifting portion 8 raise up and cover plate 9 can be good at avoiding the generation of tempering phenomenon, reach the thermal efficiency ensureing boiler, improve the object of security.
In order to improve the powder feeding efficiency of feed arrangement, and ensure that biomass fuel can be washed cover plate 9 open and fall into Boiling Combustion room with parabolical form, in the utility model embodiment, the angle β of feed arrangement and horizontal plane meets 8 °≤β≤15 °.
Lifting portion 8 can adopt various shape, such as straight-tube shape, bell mouth shape etc., no matter but be that straight-tube shape, its opening of bell mouth shape are all larger, be unfavorable for the generation avoiding tempering phenomenon, therefore, in the utility model embodiment, lifting portion 8 is from the one end be connected with feed arrangement to other end reduced diameter, like this, the port of export in lifting portion 8 diminishes, biomass fuel not only can be made more easily to wash cover plate 9 open, and better can avoid the generation of tempering phenomenon, improve the security of feed arrangement.
Lifting portion 8 outlet can adopt multiple towards, such as export place plane parallel with perpendicular, be tilted to down or tilt upward etc., but in actual use, parallel with perpendicular or be tilted to down and all easily make biomass fuel export in lifting portion 8 or lifting portion 8 combustion, and then cause the material in feed arrangement to burn, cause tempering, therefore, in order to optimize technique scheme further, in the utility model embodiment, lifting portion 8 tilts upward away from the opening of one end of feed arrangement, and the angle γ of its place plane and horizontal plane meets 30 °≤γ≤50 °, so, in guarantee, biomass fuel is dished out, and while falling with parabola, avoid the generation of tempering phenomenon, ensure security.
It is hinged that cover plate 9 can be accomplished in several ways with lifting portion 8, and in the utility model embodiment, lifting portion 8 is provided with mount pad away from the top of one end of feed arrangement, mount pad is arranged hinged ear, cover plate 9 by hinge on hinge ear.
In order to prevent the biomass fuel gone out, cover plate 9 is rushed, make it to be in vertical state or to rotate greater angle to cause it to be difficult to fall with self gravitation, cannot continue to carry out capping to lifting portion 8, in the utility model embodiment, limited block is provided with above mount pad, can prevent cover plate 9 from rotating to vertical state or rotating greater angle by limited block, ensure its capping for lifting portion 8, avoid fireproof tempering device to lose efficacy.
In order to further improve the anti-backfire effect of fireproof tempering device, in the utility model embodiment, cover plate 9 is provided with at least one circle annular protrusion, one end hinged with cover plate 9, lifting portion 8 is provided with the annular groove matched with annular protrusion, after the opening in lifting portion 8 covers by cover plate 9, annular protrusion coordinates with annular groove, like this, it is more tight that cover plate 9 can coordinate with lifting portion 8, improves anti-backfire effect.
Annular protrusion can adopt various shape, and in the utility model embodiment, the cross section of annular protrusion is circular or oval.
In this description, each embodiment adopts the mode of going forward one by one to describe, and what each embodiment stressed is the difference with other embodiments, between each embodiment identical similar portion mutually see.
To the above-mentioned explanation of the disclosed embodiments, professional and technical personnel in the field are realized or uses the utility model.To be apparent for those skilled in the art to the multiple amendment of these embodiments, General Principle as defined herein when not departing from spirit or scope of the present utility model, can realize in other embodiments.Therefore, the utility model can not be restricted to these embodiments shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (10)
1. a precipice formula multi-stage biological matter burner, is characterized in that, comprise stacked setting from down to up and the multiple combustion chambers be communicated with successively, each described combustion chamber includes:
Body of heater;
Be arranged on the feed arrangement on body of heater, the discharging opening of described feed arrangement is communicated with the burner hearth of described body of heater;
To be arranged in described burner hearth of the furnace body and the boiling burner be positioned at below described discharging opening, comprise inner casing (11), shell (12) and the first air blast (15), described inner casing (11) and described shell (12) are arranged in described body of heater, described inner casing (11) to be nested in described shell (12) and and form air cavity between described shell (12), the sidewall of described inner casing (11) offers multiple pore (10), described shell (12) is provided with ash releasing tube (13) and the first blast pipe (14), described first blast pipe (14) one end is communicated with described air cavity, the other end is connected with described first air blast (15) air outlet,
The body of heater of orlop combustion chamber is provided with ash discharging hole, and the ash releasing tube (13) of each described boiling burner is all communicated with described ash discharging hole;
The superiors combustion chamber is provided with the smoke exhaust pipe for being discharged by flue gas.
2. precipice according to claim 1 formula multi-stage biological matter burner, it is characterized in that, also comprise flue gas heat-exchange unit (4), described flue gas heat-exchange unit (4) is arranged on the top of the superiors combustion chamber, its gas approach is communicated with described smoke exhaust pipe, and exhanst gas outlet is connected with air-introduced machine.
3. precipice according to claim 1 formula multi-stage biological matter burner, it is characterized in that, also comprise the second air blast (5), described second air blast (5) is connected with each combustion chamber by the second blast pipe, described second blast pipe comprise air inlet main pipe and with each combustion chamber air intake arm one to one, described air inlet main pipe one end is communicated with the air outlet of described air blast, and the other end is connected with each air intake arm.
4. precipice according to claim 3 formula multi-stage biological matter burner, it is characterized in that, described air intake arm is provided with air inlet valve near one end of described combustion chamber.
5. precipice according to claim 1 formula multi-stage biological matter burner, it is characterized in that, described precipice formula multi-stage biological matter burner comprises bottom combustion chamber (1), combustion chamber, middle level (2) and high-rise combustion chamber (3), the furnace temperature of described bottom combustion chamber (1) is 500 DEG C ~ 600 DEG C, the furnace temperature of combustion chamber, described middle level (2) is 700 DEG C ~ 800 DEG C, and the furnace temperature of described high-rise combustion chamber (3) is 1100 DEG C ~ 1400 DEG C.
6. precipice according to claim 5 formula multi-stage biological matter burner, is characterized in that, the combustion space of described bottom combustion chamber (1), combustion chamber, described middle level (2) and described high-rise combustion chamber (3) increases successively.
7. precipice according to claim 1 formula multi-stage biological matter burner, it is characterized in that, described feed arrangement comprises hopper (7) and conveying worm (6), the discharging opening of described conveying worm (6) is communicated with the burner hearth of described body of heater, described hopper (7) comprises feeding-passage (701) and heat exchanging part, feeding-passage (701) has import and outlet, and described outlet is communicated with described conveying worm (6) feeding mouth; Described heat exchanging part is wrapped in the outside of described feeding-passage (701), is provided with gas approach and exhanst gas outlet, and described gas approach is communicated with described smoke exhaust pipe.
8. precipice according to claim 7 formula multi-stage biological matter burner, it is characterized in that, bottom near described conveying worm (6) in described feeding-passage (701) is provided with filtering device, and described filtering device comprises filter net device (16) and magnet filter (17).
9. precipice according to claim 1 formula multi-stage biological matter burner, it is characterized in that, the discharging opening of described feed arrangement is provided with fireproof tempering device, described fireproof tempering device comprises lifting portion (8) and cover plate (9), described lifting portion (8) is for hollow and two ends all have the tubular of opening, its one end is communicated with described feed arrangement discharging opening, and the other end is hinged with described cover plate (9), and described lifting portion (8) is inclined upwardly and meets 30 °≤α≤50 ° with the angle α of horizontal plane.
10. precipice according to claim 9 formula multi-stage biological matter burner, it is characterized in that, the angle β of described feed arrangement and horizontal plane meets 8 °≤β≤15 °, described lifting portion (8) tilts upward away from the opening of one end of described feed arrangement, and the angle γ of its place plane and described horizontal plane meets 30 °≤γ≤50 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520560892.0U CN204922945U (en) | 2015-07-29 | 2015-07-29 | Multistage biomass combustion device of precipice formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520560892.0U CN204922945U (en) | 2015-07-29 | 2015-07-29 | Multistage biomass combustion device of precipice formula |
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| Publication Number | Publication Date |
|---|---|
| CN204922945U true CN204922945U (en) | 2015-12-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520560892.0U Withdrawn - After Issue CN204922945U (en) | 2015-07-29 | 2015-07-29 | Multistage biomass combustion device of precipice formula |
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| Country | Link |
|---|---|
| CN (1) | CN204922945U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105003906A (en) * | 2015-07-29 | 2015-10-28 | 重庆巴洛克新能源有限公司 | Cliff type multi-level biomass burning device |
| CN106500307A (en) * | 2016-11-03 | 2017-03-15 | 黄山容宇五金制品有限公司 | A kind of novel multi-pass biomass thermal wind furnace |
-
2015
- 2015-07-29 CN CN201520560892.0U patent/CN204922945U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105003906A (en) * | 2015-07-29 | 2015-10-28 | 重庆巴洛克新能源有限公司 | Cliff type multi-level biomass burning device |
| CN105003906B (en) * | 2015-07-29 | 2018-05-25 | 重庆森盟新能源开发有限公司 | A kind of precipice formula multi-stage biological matter burner |
| CN106500307A (en) * | 2016-11-03 | 2017-03-15 | 黄山容宇五金制品有限公司 | A kind of novel multi-pass biomass thermal wind furnace |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20151230 Effective date of abandoning: 20180525 |