CN104595913B - Ash fertilizer firing device - Google Patents
Ash fertilizer firing device Download PDFInfo
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- CN104595913B CN104595913B CN201410728767.6A CN201410728767A CN104595913B CN 104595913 B CN104595913 B CN 104595913B CN 201410728767 A CN201410728767 A CN 201410728767A CN 104595913 B CN104595913 B CN 104595913B
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
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- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
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Abstract
The invention discloses an ash fertilizer firing device which can effectively carry out firing on wheat straw in a concentrating mode, a firing process is stable and efficient, full firing can be guaranteed, prepared ash fertilizer is high in purity, generated smoke can be effectively processed, and smoke pollution can be avoided. The ash fertilizer firing device comprises an incineration kiln, a feeding device and a smoke purifying device. An incineration inner cavity is arranged at the incineration kiln. The incineration kiln is oblique, and the angle between the incineration kiln and the horizontal plane is 10-60 degrees. A transmission shaft driven by a main motor is arranged in the incineration inner cavity. A plurality of material dispersing bodies for stirring materials are arranged on the transmission main shaft. An air inlet, a smoke outlet, a feeding opening and a material clearing opening-closing door are arranged on the incineration kiln. The ash fertilizer firing device has the advantages that separating effect is good, removing of solid particles and dust in smoke can be achieved, raw materials are subjected to drying through smoke waste heat, following firing effect is improved, a preheating structure is arranged, and following incineration can be well and fully guaranteed.
Description
Technical field
The invention belongs to technical field of fertilizer production, more particularly, to a kind of ash fertilizer baking apparatus.
Background technology
Currently, often have many more intractable and little plants of value, such as the weeds in gardens, extremely
The withered tree died, the disconnected branch of plant, straw of crop etc., among this, wheat straw is sizable in the growing amount of China every year.If
Wheat straw or other plant to be filled use directly as fertilizer, because its relative volume is larger, decompose slow, actual fertilizer energy
Power is poor, easily causes many counter productives on the contrary.So, may be selected to be carried out centralized burning, thus being fired into plant ash
Fertilizer is carrying out reasonable employment.Plant ash is the ashes after various burning plants, so the mineral element contained by every plant, grass
Nearly all contain in wood ash.What wherein content was most is potassium element, typically contains potassium 6～12%；Next to that phosphorus, typically contain 1.5～
3%；Also contain the micronutrient elements such as calcium, magnesium, silicon, sulfur and ferrum, manganese, copper, zinc, boron, molybdenum.The ash of different plants, its nutrient
Content is different.When waiting potassium amount to apply plant ash, fertilizer efficiency is better than Chemical Potassium.So, it is that a kind of nutrient is complete, fertilizer efficiency
Significantly inorganic fertilizer.However, at present during burning system fertilizer, having several main weak points：Easily produce substantial amounts of
Surrounding enviroment, thus forming flue dust, are adversely affected by solid particulate matter：Because centralized burning, burning process easily occurs not
Sufficiently phenomenon, raw material availability is limited and impurity content can be led to too high；And due to impurity in the Plant ash fertilizer made, remaining
Material is more, needs to carry out follow-up process, increased operation, production efficiency and cost are adversely affected.
Content of the invention
The present invention is to overcome deficiency of the prior art, there is provided one kind can be effectively residual to the plants such as wheat straw, plant
Material carries out concentration and fires process, sintering procedure stability and high efficiency, can ensure burning fully, and the ash fertilizer purity made is high, and can be to product
Raw flue gas is effectively treated, and can avoid causing the device of smoke contamination.
To achieve these goals, the present invention employs the following technical solutions：
A kind of ash fertilizer baking apparatus, including incinerating kiln, pay-off, net cigarette device：
Described incinerating kiln has burning inner chamber, and described incinerating kiln is tilted and become 10 to 60 degree, institute between horizontal plane
State burn inner chamber in be provided with the transmission main shaft being driven by mair motor, described transmission main shaft be provided with multiple for stirring material
Bulk cargo body, described incinerating kiln be provided with air inlet, smoke portion, charging aperture, clearly expect open and close door；
Described pay-off includes feed cylinder, compression unit, is provided with feeding auger in described feed cylinder, described compression
Portion is connected between feed cylinder and charging aperture, and the bore of described compression unit is gradually reduced from feeding auger to charging aperture direction；
Described net cigarette device includes discharge fume outer course, falling pond, and described smoke evacuation outer course connected with smoke portion, described row
In cigarette outer course, top is provided with multiple water drenching heads, and water drenching direction is that described smoke evacuation outer course is connected with falling pond from top to bottom；
Described bulk cargo body is provided with some through holes of igniting, and the described axis of through hole of igniting is put down with transmission main shaft axis
OK.
Preferably, described net cigarette device also includes a smoke-exhaust pipeline, described smoke-exhaust pipeline inwall and overboard water
Form the whole road of smoke evacuation between face, be provided with multiple aerosol apparatus in described smoke evacuation end road, the water source of described aerosol apparatus is falling pond,
Described smoke evacuation end road entrance and smoke evacuation outer course outlet.
Preferably, described air inlet is in the subaerial one end of incinerating kiln, smoke portion is in incinerating kiln remotely
The one end in face, described air inlet connects a compressing device, is provided with ash fertilizer immersed tube, institute between described smoke portion and net cigarette device
It is connected by pipe between the ash fertilizer immersed tube stated and smoke portion, passed through smoke pipe between ash fertilizer immersed tube and net cigarette device and be connected,
The bore of described net cigarette device is 3 to 10 times of pipe bore.
Preferably, the connecting portion of described pipe and ash fertilizer immersed tube is in the top of ash fertilizer immersed tube one end mouth of pipe, mistake
The connecting portion of smoke pipe and ash fertilizer immersed tube is in the top of the ash fertilizer immersed tube other end mouth of pipe, and described ash fertilizer immersed tube bottom is provided with unloads fertilizer
Door.
Preferably, being provided with preheating barrel in described incinerating kiln, described preheating barrel is connected with charging aperture, described
Preheating barrel is in one end away from air inlet in incinerating kiln.
Preferably, also including raw material desiccation apparatus, described raw material desiccation apparatus include one and can revolve along own axes
The concentrator bowl turning, described concentrator bowl is the circular cone shape of upper and lower opening, and concentrator bowl upper shed is feed(raw material)inlet, and under shed is former
Material outlet.
Preferably, being arranged with hot dry cylinder outside described concentrator bowl, described heat does medial wall of the tube, upper lower bottom part and centrifugation
Form the dry chamber of heat, described heat is done chamber and is provided with heat supply mouth, outlet, and the two ends of a damp and hot trachea are respectively between cylinder lateral wall
Connect heat supply mouth, net cigarette device.
Preferably, described heat does medial wall of the tube is provided with a continuous, spiral internal partition, described is interior
Dry for heat chamber is separated into a continuous airway by dividing plate, and the originating port of described airway connects heat supply mouth, described ventilation
The termination section connection outlet in road.
Preferably, also including a dozen dirty motors, described transmission main shaft is provided with main shaft inner chamber, one and transmission main shaft
Coaxial transmission interior axle stretches among main shaft inner chamber, and described transmission interior axle one end is connected with beating dirty motor output shaft, the other end
Be connected with inner shaft bearing, described transmission main shaft be provided with multiple beat dirty device, described beat dirty device include beating dirt ball,
Spacing ball, receipts ball spring, slide bar, the slide opening on transmission main shaft wall, described slide bar is slidably matched with slide opening, and described beats
Dirty ball is connected with slide bar two ends respectively with spacing ball, and described receipts ball spring is set on slide bar and is in spacing ball and transmission master
Between axle medial wall, described play dirty ball and contact with transmission main shaft lateral wall, described transmission interior axle be provided with multiple for pushing away
The push pedal of dynamic spacing ball, each spacing ball corresponds to a push pedal.
Preferably, described dirty device of beating also includes extending protection group, in described prolongation protection group and transmission main shaft
Side wall connects, and described slide bar passes through and extends protection group, and described receipts ball both ends of the spring compresses spacing ball respectively, extends protection
Base, for be under the jurisdiction of same beat dirty device and make dirty ball and slide bar, therein beat the vertical of the dirty ball centre of sphere and transmission main shaft axis
Direct-connected line, becomes 20 to 45 degree angles between slide bar therein.
The invention has the beneficial effects as follows：The purification ＆ isolation realizing plant ash can be blown by air, separating effect is excellent；Tool
There are spraying and water drenching purification function, twice cleaning procedure realizes the removing to solid particulate matter in flue gas and dust perfectly；Profit
With fume afterheat, raw material is carried out with mummification, improves and subsequently fire effect；There is preheating structure, can more preferably more fully ensure follow-up
Burning；The cleaning operation of fouling can quickly be realized after the completion of work, can increase the service life, ensure that burning next time is imitated
Really.
Brief description
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the structural representation at incinerating kiln of the present invention and pay-off；
Fig. 3 is the structural representation of raw material desiccation apparatus of the present invention；
Fig. 4 is the structural representation of intracavity in main shaft in the embodiment of the present invention 2；
Fig. 5 is the structural representation of bulk cargo body of the present invention.
In figure：Incinerating kiln 1, pay-off 2, net cigarette device 3, mair motor 4, transmission main shaft 5, bulk cargo body 6, air inlet 7, go out
Cigarette portion 8, feed cylinder 9, compression unit 10, feeding auger 11, smoke evacuation outer course 12, falling pond 13, water drenching head 14, smoke-exhaust pipeline 15, row
Yan Zhong road 16, aerosol apparatus 17, ash fertilizer immersed tube 18, pipe 19, cross smoke pipe 20, unload fertile door 21, preheating barrel 22, raw material mummification dress
Put 23, concentrator bowl 24, hot dry cylinder 25, heat supply mouth 26, outlet 27, damp and hot trachea 28, internal partition 29, airway 30, in main shaft
Chamber 31, transmission interior axle 32, beat dirty ball 33, spacing ball 34, receive ball spring 35, slide bar 36, push pedal 37, prolongation protection group 38, ignite
Through hole 39.
Specific embodiment
The present invention will be further described with reference to the accompanying drawings and detailed description.
Embodiment 1：As shown in Figure 1, Figure 2, in the embodiment shown in Fig. 3, Fig. 5, a kind of ash fertilizer baking apparatus, including incinerating kiln 1,
Pay-off 2, net cigarette device 3：Described incinerating kiln has burning inner chamber, and described incinerating kiln is tilted and become between horizontal plane
10 to 60 degree, described burning in inner chamber is provided with the transmission main shaft 5 being driven by mair motor 4, and described transmission main shaft is provided with many
The individual bulk cargo body 6 for stirring material, described incinerating kiln is provided with air inlet 7, smoke portion 8, charging aperture；Described feeding dress
Put including feed cylinder 9, compression unit 10, in described feed cylinder, be provided with feeding auger 11, described compression unit is connected to feed cylinder
And charging aperture between, the bore of described compression unit is gradually reduced from feeding auger to charging aperture direction；Described net cigarette device
Including smoke evacuation outer course 12, falling pond 13, described smoke evacuation outer course is connected with smoke portion, and the interior top of described smoke evacuation outer course is provided with many
Individual water drenching head 14, water drenching direction is that described smoke evacuation outer course is connected with falling pond from top to bottom；If described bulk cargo body is provided with
Dry through hole 39 of igniting, the described axis of through hole of igniting and transmission main shaft diameter parallel.
Burning inner chamber is available for wheat straw etc. and burns wherein, and a large amount of wheat straws are fed auger and push, and open after reaching compression unit
Begin mutual jam-packed enter charging aperture with this state, and air or other combustion-supporting gas then enter incinerating kiln from air inlet.Wheat straw
Incinerating kiln is entered with the state of jam-packed, therefore at charging aperture, air can not circulate, and straw herein will not burn substantially, at most only
There is the head portion that straw enters incinerating kiln may guide to some flames, but because lack of air is also difficult to extend on a large scale, because
This ensure that straw in the outer part will not first incinerate in a large number first, it is to avoid first burn because of outside straw, carbonization, leads to squeezed
Subsequently it is difficult to ignite it is impossible to clean-burning problem in middle straw.After wheat straw enters bulk cargo body region, start to be stirred always
Move and advance, break up, now scattered wheat straw can be fully contacted with air, can preferably be burnt, direct shape after having burnt
Plant ash is become to stay in incinerating kiln.After crop straw burning, some unburnt parts can be left unavoidably, and the impurity such as soil and
The plant ash having been formed can cover these unburnt parts so as to be difficult to burn away, now, because bulk cargo body exists always
The straw of raw feed and unburnt straw can be included bringing up together with impurity, plant ash, so that it is fallen again by agitation
Under, thus repeatedly breaing up, recycling igniting and for fire of raw feed, realizing burning again.Through hole of igniting on bulk cargo body was both beneficial to
Ventilation, is also preferably contacted with raw material beneficial to pilot flame, the agitation function of bulk cargo body is to drive transmission main shaft by mair motor
Rotate and realize, in use, the auxiliary device such as decelerator can also be set up according to actual needs on mair motor, thus allowing
The rotating speed of transmission main shaft can be in more reasonably scope, and transmission main shaft can be with pedestal, bearing or other conventional joining with axle
The structure closed is being supported, to position so as to the stable work of energy incinerating kiln in.The heat smoke producing after straw burning
Up to 600 to 700 degree, it is contained within a large amount of solid particulate matters, and now, heat smoke enters aerofluxuss outer course by smoke portion.Aerofluxuss
Water drenching head in outer course with water drenching, can form one section of exhaust gases passes in similar rainfall portion in aerofluxuss outer course, and heat smoke temperature is fitted
Work as reduction, solid particulate matter is taken away in a large number by " rainwater ", and enters falling pond together with the water falling, thus realizing flue gas
Purify.
Described net cigarette device also includes a smoke-exhaust pipeline 15, shape between described smoke-exhaust pipeline inwall and the falling pond water surface
Become the whole road 16 of smoke evacuation, be provided with multiple aerosol apparatus 17 in described smoke evacuation end road, the water source of described aerosol apparatus is falling pond, described
Smoke evacuation end road entrance and smoke evacuation outer course outlet.
In order to the resistance that prevents from discharging fume is excessive, water drenching will keep gap between each stock current when purifying it is impossible to allow under pouring
Water large area fill, cover smoke evacuation outer course, therefore after primary purification discharge flue gas still contain a certain amount of solid particulate matter with
Dust.Now, these flue gases can spray water smoke through the whole road of smoke evacuation, aerosol apparatus, is formed large-area net in the whole road of smoke evacuation
Change water smoke, these purify, and water smoke smoke evacuation resistance is little, be evenly distributed and fill the whole road of smoke evacuation, solid particulate matter one water receiving in flue gas
Easily combine the water droplet in water smoke after mist, also easily repeatedly combine, absorption quickly becomes big water droplet, drop back into falling pond together, fall
Water in pond pass through aerosol apparatus can iterative cycles, always flue gas is filtered and is purified, energy consumption is only aerosol apparatus
The electric energy consuming, effect substantially, can Infinite Cyclic use, the resource of water supply of also very environmental protection, and water drenching head can be overboard
Pond, forms overall circulation, also can save extras.
Described air inlet is in the subaerial one end of incinerating kiln, and smoke portion is in incinerating kiln one end away from ground,
Described air inlet connects a compressing device, is provided with ash fertilizer immersed tube 18 between described smoke portion and net cigarette device, described ash
It is connected by pipe 19 between fertile immersed tube and smoke portion, passed through smoke pipe 20 between ash fertilizer immersed tube and net cigarette device and be connected, institute
The bore of the net cigarette device stated is 3 to 10 times of pipe bore.
Compressing device can be the arbitrarily conventional gas booster such as air pump, aerator.As long as can be by air with certain pressure
Send into incinerating kiln, so, be equivalent to and define one in incinerating kiln there is certain speed, lasting air-flow,
This strand of air-flow can ensure that the oxygen of in the air can more be brought in incinerating kiln, it is to avoid leads to oxygen because air velocity is excessively slow
Gas is just depleted near air inlet, leads to burning in incinerating kiln too uneven.And, after burning till plant ash, due to grass
Wood ash is relatively very light, and straw, impurity, uncombusted part are then relatively heavy, and plant ash is blown together with air-flow, from smoke
Portion is left, and is equivalent to and defines " pneumatic jig ", directly separates plant ash and other raw materials, impurity, and taken out of by air-flow
Plant ash, after entering into ash fertilizer immersed tube, because ash fertilizer immersed tube bore rises sharply relatively, air-flow directly slows down, and blows plant ash ability
It is greatly reduced, plant ash starts to be settled down to ash fertilizer immersed tube bottom, and air-flow then leaves ash fertilizer with relatively lighter solid particulate matter
Immersed tube, enters net cigarette device.This process is directly realized plant ash purification, extracts the plant ash purity pole of ash fertilizer immersed tube
Height, impurity etc. has then been left in incinerating kiln at the very start, and high-purity plant ash can directly carry out packaging and follow-up use, and
And this process does not need what high cost equipment and isolation of purified process, Financial cost is very low, and after the completion of burning, clear material opens and closes
Door can be opened, thus the defective material of incinerating kiln bottom, impurity etc. can be cleared up.
The connecting portion of described pipe and ash fertilizer immersed tube is in the top of ash fertilizer immersed tube one end mouth of pipe, crosses smoke pipe and ash fertilizer
The connecting portion of immersed tube is in the top of the ash fertilizer immersed tube other end mouth of pipe, and described ash fertilizer immersed tube bottom is provided with unloads fertile door 21.Avoid
Plant ash after sedimentation directly contacts rapidly air-flow, preferably keeps plant ash here.
It is provided with preheating barrel 22, described preheating barrel connected with charging aperture, described pre- hot material in described incinerating kiln
Cylinder is in the one end in incinerating kiln away from air inlet.The straw of jam-packed, after charging, can't be directly entered bulk cargo body model mutually
Enclose and broken up, but first pass through preheating barrel, air from air inlet entrance after, because burning can be heated, the air-flow after heating
Reach at preheating barrel, straw is first preheated.Preheated straw, closer to ignition temperature, once large area touches fire, combustion
Burn up more fierce, more rapid, evenly, therefore, it is possible to more fully after-flame, improve the burn-off rate of primary combustion.
Also include raw material desiccation apparatus 23, described raw material desiccation apparatus include one can be along the centrifugation of own axes rotation
Cylinder 24, described concentrator bowl is the circular cone shape of upper and lower opening, and concentrator bowl upper shed is feed(raw material)inlet, and under shed goes out for raw material
Mouthful.It is arranged with hot dry cylinder 25, described heat is done between medial wall of the tube, upper lower bottom part and concentrator bowl lateral wall outside described concentrator bowl
Form the dry chamber of heat, described heat is done chamber and is provided with heat supply mouth 26, outlet 27, and the two ends of a damp and hot trachea 28 connect confession respectively
Hot mouth, net cigarette device.Described heat is done medial wall of the tube and is provided with a continuous, spiral internal partition 29, and described is interior
Dry for heat chamber is separated into a continuous airway 30 by dividing plate, and the originating port of described airway connects heat supply mouth, and described is logical
The termination section connection outlet of air flue.
The raw materials such as straw are because making moist, rainfall and the reason such as originally aqueous, are not dry, desiccation apparatus can pass through
Centrifugation whipping, suitably removes water.And the flue gas finally discharged is through water drenching and water smoke area decontamination, its temperature is about at 130 degree
To 250 degree, different depending on the impact of the factors such as water smoke region, the length in water drenching region and air velocity, but at least or high
Warm air.But, contain water vapour in this strand of high temperature gas flow, be therefore directly used in the not science of the mummification to raw material, easily lead
Moisture condensation is caused to return in raw material.And passed through airway, then mummification can be carried out to raw material by indirect heat conducting.Raw material quilt
After centrifugation whipping, can be formed and be attached on concentrator bowl " adherent " effect, therefore be subject to heat drying effect more preferable.Raw material after mummification is again
By feeding packing auger feed, burn it is possible to reducing energy consumption, improve incinerating kiln in efficiency of combustion and burning adequacy.
Embodiment 2：, with embodiment 1, its difference is for the basic structure of the present embodiment and embodiment, as Fig. 4 institute
Show, also include a dozen dirty motors, described transmission main shaft is provided with main shaft inner chamber 31, in a transmission coaxial with transmission main shaft
Axle 32 stretches among main shaft inner chamber, and described transmission interior axle one end is connected with beating dirty motor output shaft, the other end and inner shaft bearing
Be connected, make dirty motor and can also be located among main shaft inner chamber, described transmission main shaft be provided with multiple beat dirty device, described
Dirty device of beating include beating dirty ball 33, spacing ball 34, receive ball spring 35, slide bar 36, the slide opening on transmission main shaft wall, described
Slide bar be slidably matched with slide opening, described play dirty ball and be connected with slide bar two ends respectively with spacing ball, described receipts ball spring housing
It is located on slide bar and is between spacing ball and transmission main shaft medial wall, described dirty ball of beating is contacted with transmission main shaft lateral wall,
Described transmission interior axle is provided with multiple push pedals 37 for promoting spacing ball, and each spacing ball corresponds to a push pedal.
After burning terminates, in incinerating kiln, kiln wall, substantial amounts of ash, the fouling of mud can be left, incinerating kiln is big due to volume, relatively
Difficult dismounting and cleaning, the time one is long, easily causes and adheres to too many lump on kiln wall, use afterwards is adversely affected.This
When, can start and make dirty motor, drive transmission interior axle quickly to rotate, transmission interior axle drives push pedal high-speed rotation together, and push pedal pushes away
Dynamic, strike limiting section is displaced outwardly, and receives ball spring and is compressed, and plays dirty ball and leaves transmission main shaft, starts to tap mummification main cylinder inwall,
At the same time it can also allow the relatively slow transmission main shaft work rotation of rotating speed, band moving slide-bar constantly shifts one's position, towards so that every
Individual beat the many places that dirty ball can tap mummification main cylinder inwall, by direct tap, indirectly vibrations realize fouling in incinerating kiln
Cleaning, maintains good follow-up work environment, extends the service life of incinerating kiln.
Described dirty device of beating also includes extending protection group 38, and described prolongation protection group is with transmission main shaft medial wall even
Connect, described slide bar passes through and extends protection group, described receipts ball both ends of the spring compresses spacing ball respectively, extends protection group, for
Be under the jurisdiction of same beat dirty device make dirty ball and slide bar, the vertical join line beating the dirty ball centre of sphere and transmission main shaft axis therein,
20 to 45 degree angles are become between slide bar therein.
By extending protection group, slide bar is protected, its axle can be reduced partially, prevent it from losing.Slide bar be have certain
Drift angle, therefore can be it is allowed to design less main shaft inner chamber on the premise of identical slide bar length.And play dirty ball and reclaiming
Cheng Zhong, is also no longer vertical percussion to transmission main shaft, can disperse the vertical percussion power being subject on transmission main shaft radial direction, reach
Effect to protection.
Claims (9)
1. a kind of ash fertilizer baking apparatus, is characterized in that, including incinerating kiln, pay-off, net cigarette device：
Described incinerating kiln has burning inner chamber, and described incinerating kiln tilts and become between horizontal plane 10 to 60 degree, described
Burn inner chamber in be provided with the transmission main shaft being driven by mair motor, described transmission main shaft be provided with multiple for stir material dissipate
Material body, described incinerating kiln is provided with air inlet, smoke portion, charging aperture, expects clearly open and close door；
Described pay-off includes feed cylinder, compression unit, is provided with feeding auger in described feed cylinder, and described compression unit is even
It is connected between feed cylinder and charging aperture, the bore of described compression unit is gradually reduced from feeding auger to charging aperture direction；
Described net cigarette device includes discharge fume outer course, falling pond, and described smoke evacuation outer course is connected with smoke portion, outside described smoke evacuation
In road, top is provided with multiple water drenching heads, and water drenching direction is that described smoke evacuation outer course is connected with falling pond from top to bottom；
Described bulk cargo body is provided with some through holes of igniting, the described axis of through hole of igniting and transmission main shaft diameter parallel；
Described air inlet is in the subaerial one end of incinerating kiln, and smoke portion is in incinerating kiln one end away from ground, described
Air inlet connect a compressing device, be provided with ash fertilizer immersed tube between described smoke portion and net cigarette device, described ash fertilizer immersed tube
It is connected by pipe between smoke portion, passed through smoke pipe between ash fertilizer immersed tube and net cigarette device and be connected, described net cigarette fills
The bore put is 3 to 10 times of pipe bore.
2. a kind of ash fertilizer baking apparatus according to claim 1, is characterized in that, described net cigarette device also includes a smoke evacuation
Pipeline, forms the whole road of smoke evacuation, is provided with multiple in described smoke evacuation end road between described smoke-exhaust pipeline inwall and the falling pond water surface
Aerosol apparatus, the water source of described aerosol apparatus is falling pond, described smoke evacuation end road entrance and smoke evacuation outer course outlet.
3. a kind of ash fertilizer baking apparatus according to claim 1, is characterized in that, the company of described pipe and ash fertilizer immersed tube
Socket part is in the top of ash fertilizer immersed tube one end mouth of pipe, and the connecting portion crossing smoke pipe with ash fertilizer immersed tube is in the ash fertilizer immersed tube other end mouth of pipe
Top, described ash fertilizer immersed tube bottom is provided with unloads fertile door.
4. a kind of ash fertilizer baking apparatus according to claim 1 or 3, is characterized in that, be provided with preheating in described incinerating kiln
Barrel, described preheating barrel is connected with charging aperture, and described preheating barrel is in one end away from air inlet in incinerating kiln.
5. a kind of ash fertilizer baking apparatus according to claim 1 and 2, is characterized in that, also include raw material desiccation apparatus, institute
The raw material desiccation apparatus stated include one can be along the concentrator bowl of own axes rotation, and described concentrator bowl is the frustum of a cone of upper and lower opening
Shape, concentrator bowl upper shed is feed(raw material)inlet, and under shed is material outlet.
6. a kind of ash fertilizer baking apparatus according to claim 5, is characterized in that, are arranged with heat dry outside described concentrator bowl
Cylinder, described heat is done and is formed the dry chamber of heat between medial wall of the tube, upper lower bottom part and concentrator bowl lateral wall, and described heat is done chamber and is provided with
Heat supply mouth, outlet, the two ends of a damp and hot trachea connect heat supply mouth, net cigarette device respectively.
7. a kind of ash fertilizer baking apparatus according to claim 6, is characterized in that, described heat is done medial wall of the tube and is provided with one
Bar is continuous, spiral internal partition, and dry for heat chamber is separated into a continuous airway by described internal partition, and described is logical
The originating port connection heat supply mouth of air flue, the termination section of described airway connects outlet.
8. a kind of ash fertilizer baking apparatus according to claim 1, is characterized in that, also include a dozen dirty motors, described biography
Dynamic main shaft is provided with main shaft inner chamber, and a transmission interior axle coaxial with transmission main shaft stretches among main shaft inner chamber, described transmission
Interior axle one end is connected with beating dirty motor output shaft, and the other end is connected with inner shaft bearing, and described transmission main shaft is provided with many
Individual beat dirty device, described dirty device of beating includes beating dirty ball, spacing ball, receipts ball spring, slide bar, the cunning on transmission main shaft wall
Hole, described slide bar is slidably matched with slide opening, described play dirty ball and be connected with slide bar two ends respectively with spacing ball, described receipts ball
Spring is set on slide bar and is between spacing ball and transmission main shaft medial wall, and described beats dirty ball and transmission main shaft lateral wall
Contact, described transmission interior axle is provided with multiple push pedals for promoting spacing ball, and each spacing ball corresponds to a push pedal.
9. a kind of ash fertilizer baking apparatus according to claim 8, is characterized in that, described dirty device of beating also includes extending protecting
Shield base, described prolongation protection group is connected with rotor main shaft medial wall, described slide bar through prolongation protection group, described receipts ball
Both ends of the spring compresses spacing ball respectively, extends protection group, makes dirty ball and slide bar for being under the jurisdiction of same dirt device of beating, wherein
The vertical join line beating the dirty ball centre of sphere and rotor main shaft axis, becomes 20 to 45 to spend angles between slide bar therein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410728767.6A CN104595913B (en) | 2014-12-04 | 2014-12-04 | Ash fertilizer firing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410728767.6A CN104595913B (en) | 2014-12-04 | 2014-12-04 | Ash fertilizer firing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104595913A CN104595913A (en) | 2015-05-06 |
| CN104595913B true CN104595913B (en) | 2017-02-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410728767.6A Expired - Fee Related CN104595913B (en) | 2014-12-04 | 2014-12-04 | Ash fertilizer firing device |
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| CN (1) | CN104595913B (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104913317B (en) * | 2015-06-23 | 2017-12-12 | 内江市雨果生物科技有限公司 | The environment-friendly treatment method of rice straw |
| CN106311716B (en) * | 2016-08-05 | 2018-09-25 | 奚正文 | Garbage disposer |
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| CN2775496Y (en) * | 2005-03-17 | 2006-04-26 | 蒋惠民 | Low cost high efficiency dust removing desulfurizing device |
| CN201606882U (en) * | 2010-01-15 | 2010-10-13 | 张圣东 | High-efficiency incinerator with circulating fluidized grates |
| CN102667342A (en) * | 2009-07-10 | 2012-09-12 | 孟凡利 | Gas barrier |
| CN103939921A (en) * | 2014-03-26 | 2014-07-23 | 洛阳豫新工程技术有限公司 | Treatment device for agricultural waste |
| CN204026711U (en) * | 2014-07-16 | 2014-12-17 | 银梅 | Flue gas ash removal and the waste heat recovery circulatory system |
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| JPH0674887B2 (en) * | 1988-06-28 | 1994-09-21 | 宇部興産株式会社 | Multi-stage bed combustion device for high water content residue |
| JP2013189609A (en) * | 2012-03-15 | 2013-09-26 | Osutorando:Kk | Pyrolytic gasifying method and pyrolytic gasifying apparatus of organic waste |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2199928A (en) * | 1987-01-08 | 1988-07-20 | Wang Chi Chen | A multi-function automatic garbage incinerator |
| CN2775496Y (en) * | 2005-03-17 | 2006-04-26 | 蒋惠民 | Low cost high efficiency dust removing desulfurizing device |
| CN102667342A (en) * | 2009-07-10 | 2012-09-12 | 孟凡利 | Gas barrier |
| CN201606882U (en) * | 2010-01-15 | 2010-10-13 | 张圣东 | High-efficiency incinerator with circulating fluidized grates |
| CN103939921A (en) * | 2014-03-26 | 2014-07-23 | 洛阳豫新工程技术有限公司 | Treatment device for agricultural waste |
| CN204026711U (en) * | 2014-07-16 | 2014-12-17 | 银梅 | Flue gas ash removal and the waste heat recovery circulatory system |
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| CN104595913A (en) | 2015-05-06 |
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