CN206535526U - A kind of production system for tobacco compound fertilizer - Google Patents
A kind of production system for tobacco compound fertilizer Download PDFInfo
- Publication number
- CN206535526U CN206535526U CN201720179142.8U CN201720179142U CN206535526U CN 206535526 U CN206535526 U CN 206535526U CN 201720179142 U CN201720179142 U CN 201720179142U CN 206535526 U CN206535526 U CN 206535526U
- Authority
- CN
- China
- Prior art keywords
- pipe
- water
- exhaust emission
- power transmission
- transmission shaft
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000003337 fertilizer Substances 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 241000208125 Nicotiana Species 0.000 title claims abstract description 15
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 15
- 150000001875 compounds Chemical class 0.000 title claims abstract description 15
- 239000007921 spray Substances 0.000 claims abstract description 39
- 230000003009 desulfurizing effect Effects 0.000 claims abstract description 24
- 239000002131 composite material Substances 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 11
- 238000001816 cooling Methods 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 42
- 230000005540 biological transmission Effects 0.000 claims description 32
- 239000000463 material Substances 0.000 claims description 19
- 229910000831 Steel Inorganic materials 0.000 claims description 16
- 239000010959 steel Substances 0.000 claims description 16
- 238000009826 distribution Methods 0.000 claims description 14
- 238000009413 insulation Methods 0.000 claims description 10
- 238000004321 preservation Methods 0.000 claims description 10
- 238000003860 storage Methods 0.000 claims description 10
- 239000000835 fiber Substances 0.000 claims description 4
- 229920000728 polyester Polymers 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 3
- 210000002268 wool Anatomy 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims 1
- 238000002955 isolation Methods 0.000 claims 1
- 238000006477 desulfuration reaction Methods 0.000 abstract description 10
- 230000023556 desulfurization Effects 0.000 abstract description 8
- 239000007789 gas Substances 0.000 abstract description 8
- 239000003546 flue gas Substances 0.000 abstract description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 5
- 239000002918 waste heat Substances 0.000 abstract description 4
- 239000000779 smoke Substances 0.000 abstract description 3
- 239000003500 flue dust Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 5
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 5
- 229910052939 potassium sulfate Inorganic materials 0.000 description 5
- 235000011151 potassium sulphates Nutrition 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 210000000078 claw Anatomy 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008398 formation water Substances 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- ILRLTAZWFOQHRT-UHFFFAOYSA-N potassium;sulfuric acid Chemical compound [K].OS(O)(=O)=O ILRLTAZWFOQHRT-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
The utility model relates to composite fertilizer's technical field, more particularly to a kind of production system for tobacco compound fertilizer, including reaction tower, and the reaction tower is provided with exhaust emission pipeline and composite fertilizer's cooling lorry；Heating thin conduit is wound with the exhaust emission pipeline, the heating thin conduit is unidirectionally wound to the other end from one end of exhaust emission pipeline, and the outer sheath in exhaust emission pipeline is provided with water-supply-pipe；The exhaust emission pipeline is connected with desulfurizing tower bottom inflow pipe, the desulfurization tower bottom is provided with air inlet pipe, escape pipe is provided with above the desulfurizing tower, the circulating pump outside spray equipment, the desulfurizing tower is provided with inside the desulfurizing tower and below escape pipe spray equipment and buffer unit are connected by pipeline.The utility model can sufficiently reclaim waste heat from tail gas in reacting furnace during composite heat transfer, improve organic efficiency, and the purpose that sulfureous in flue gas, grit, flue dust realize purifying smoke is sloughed in realization.
Description
Technical field
The utility model relates to composite fertilizer's technical field, more particularly to a kind of production system for tobacco compound fertilizer.
Background technology
In composite heat transfer for example during Mannheim furnace method potassium sulfate production, potassium chloride and sulfuric acid are at high temperature
Reaction, generation potassium sulfate and hydrogen chloride, after completion of the reaction, potassium sulfate are high temperature and big block, it is necessary to by these high temperature and bulk
Shape potassium sulfate cools down and is ground into small graininess or powdery.It is usually that block potassium sulfate progress first big to high temperature is cold at present
But, then crushed and conveyed, or first cooled down and conveyed, then crushed, it is many using equipment, it is complicated,
Production procedure is more.And contain substantial amounts of waste heat in the tail gas that reacting furnace is produced, if directly discharged without recycling
Into air, on the one hand serious residual heat resources can be caused to waste so that the whole system thermal efficiency is low, and energy-output ratio is big；Separately
On the one hand high-temp waste gas is directly discharged into air and environment can be polluted.
Simultaneously in the production process of composite fertilizer, the flue gas of generation contains substantial amounts of sulfide.At present for the place of the flue gas
Reason is mainly water Membrane Desulphurization, but is due to the construction of existing spray column, and spray is not thorough enough, and desulfuration efficiency is low, generation
The standard that country externally discharges can not be still reached in waste gas, and it is also a problem to spray the liquid waste processing of generation.It is how high
Desulfurization is imitated, makes desulfurized effect more thorough, the standard for reaching waste gas and waste liquid discharge is urgent problem to be solved.
The content of the invention
In order to solve problem above, the utility model provides a kind of production system for tobacco compound fertilizer.
The technical scheme that the utility model is used：
A kind of production system for tobacco compound fertilizer, including reaction tower, the reaction tower provided with exhaust emission pipeline and
Composite fertilizer cools down lorry；
It is wound with heating thin conduit on the exhaust emission pipeline, the heating thin conduit is from one end of exhaust emission pipeline
The other end unidirectionally is wound to, water-supply-pipe is provided with the outer sheath of exhaust emission pipeline；
The heating thin conduit connects the delivery port of supply tank, heating thin conduit and water-supply-pipe with the water inlet of water-supply-pipe
Connect heat preservation storage water tank；
The exhaust gas flow heated in the water (flow) direction and exhaust emission pipeline of thin conduit and water-supply-pipe is in opposite direction, the tail
Gas discharge tube includes body, is arranged at intervals with fin on the side wall of body, the inner hollow of the fin, and fin is interior
Portion is connected with tubular body；
Preferably, the tube wall clear width of the water-supply-pipe is provided with flow distribution plate, the water-supply-pipe and exhaust emission pipeline
Between form annular water flow chamber, the flow distribution plate and fin be arranged in a crossed manner, flow distribution plate and fin in a ring, adjacent flow distribution plate
Water stream channel is formed between fin；
Heat-insulation layer is provided with the outside of the water-supply-pipe, the heat-insulation layer includes layer of polyester fiber, sheep successively from outside to inside
Felt and sponge；
It is described heating thin conduit delivery port connect three-way temperature control valve wherein Single port, the three-way temperature control valve it is another
Port is connected by pipeline with heat preservation storage water tank, and the 3rd port of the three-way temperature control valve passes through pipeline and the water inlet of water-supply-pipe
Connection.
Preferably, the exhaust emission pipeline is connected with desulfurizing tower bottom inflow pipe, and the desulfurization tower bottom is provided with air inlet
It is provided with above pipe, the desulfurizing tower inside escape pipe, the desulfurizing tower and spray equipment is provided with below escape pipe, it is described de-
Circulating pump outside sulphur tower connects spray equipment and buffer unit by pipeline, and the desulfurization tower bottom is additionally provided with outlet pipe connection
Buffer unit；
The buffer unit is provided between drainage trough, several buffer pools, several described buffer pools provided with interlaced
The isolating device being interconnected again.
It is further preferred that being provided with screen pack in several described buffer pools.
It is further preferred that the drainage trough is connected with the first buffer pool, first buffer pool and the second buffer pool
Between be provided with the first isolating device, first isolating device and the first buffer pool be one side closed close to drainage trough, described first
Isolating device is unclosed away from drainage trough side with the first buffer pool；Provided with the between second buffer pool and the 3rd buffer pool
Two isolating devices, second isolating device is unclosed close to drainage trough side with the second buffer pool, second isolating device
It is one side closed away from drainage trough with the second buffer pool.
It is further preferred that the outlet pipe is connected with drainage trough, the 3rd buffer pool is filled by pipeline with spray
Put connection.
Preferably, filter is provided with below the spray equipment, the filter is distributed for several in fold-line-shaped
Filter layer composition.
Preferably, the filter layer is non-woven fabrics or gauze, and the air inlet pipe is 30-50 degree with desulfurizing tower angle theta.
Preferably, demister is provided between the spray equipment and escape pipe, the demister is connected with cleaning pipe.
It is further preferred that the demister is provided with several flooding nozzles.
Preferably, the spray equipment is at least one layer, and each layer is provided with several spray nozzles, and the spray nozzle is straight
Footpath is 30-60nm.
Preferably, composite fertilizer's cooling lorry includes setting on power transmission shaft, including power transmission shaft successively in housing, housing
Set and crush hammer and pusher disk, housing two ends are respectively equipped with material outlet and material inlet, material inlet is located at together with crushing hammer
One end, power transmission shaft connection drive device；Housing is hollow housing, and hollow housing shell body two ends are respectively equipped with medium inlet and Jie
Matter is exported.
It is further preferred that the crushing hammer is interspersed on power transmission shaft；The pusher disk front end is provided with shoving rake；
The power transmission shaft cross section is square, circular or annular；
The power transmission shaft is square steel power transmission shaft, and square steel power transmission shaft is molded for overall processing；
The power transmission shaft two ends are provided with connecting shaft；
The power transmission shaft is steel tube driveshafts, and connecting shaft is connected with steel tube driveshafts by hot charging.
The drive device includes motor, and the motor connection gearbox, the connecting shaft is provided with gear, the gear
It is connected with gearbox；
Observation panel is set on the housing, and the observation panel is located at same one end with material outlet；
The medium inlet is located at the same one end of housing with material outlet.
The utility model has the beneficial effect that：
1st, the utility model can sufficiently reclaim waste heat from tail gas in reacting furnace during composite heat transfer, improve recovery
Efficiency, preheating cold water to preference temperature can be set fin on exhaust emission pipeline, add the contact area with current, change
Thermal effect is good, and fin can also slow down water velocity, during extension contact with the flow distribution plate formation water stream channel on the inside of water-supply-pipe
Between, waste heat of boiler tail gas is fully recycled, heat-insulation layer is set in the outside of water-supply-pipe, to be risen to the hot water after heating
To insulation effect, and heat-insulation layer is made up of layer of polyester fiber, wool felt and sponge, and high insulating effect, manufacturing cost is low.
2nd, the utility model will heat thin conduit and be connected with water-supply-pipe, and three-way temperature control valve is provided with connecting line, can
Needed to be controlled according to water temperature heating, it is easy to operate.
3rd, the utility model, which is realized, sloughs the purpose that sulfureous in flue gas, grit, flue dust realize purifying smoke, the buffering dress of setting
Put, by the drainage trough of setting, several buffer pools, interlaced isolating device is provided with again between several described buffer pools
It is interconnected, reduction waste liquid extends flow distance, the grit in waste liquid, cigarette ash are fully settled in the flowing velocity of buffer pool,
Separate step by step, it is possible to buffer pool floor space.Screen pack is provided with several buffer pools, screen pack is prevented last time buffering
Grit in pond enters next stage, improves purification efficiency, and the water of afterbody buffer pool is used directly for the spray in desulfurizing tower
Shower device water, prevents equipment from blocking, the orderly progress of biochemical reaction in influence tower.Dedusting can be reached by three buffer pools
The effect of desulfurization.
4th, the outlet pipe is connected with drainage trough, and the 3rd buffer pool is connected by pipeline with spray equipment, it is necessary to heavy
The water of drop enters drainage trough, by settling and separating layer by layer, the finally complete desulfurization and dedusting in the 3rd buffer pool, and the 3rd delays
The water rushed in pond may be directly applied to spray equipment water, and saving water resource reaches the effect of recycling.In spray equipment
Top is provided with demister, can will absorb SO2Flue gas afterwards, the drop and water smoke of entrainment are separated, to control and prevent
Sulphite is in demister and tower wall generation fouling.Spray equipment is provided with several spray nozzles, and the spray nozzle is a diameter of
30-60nm.Desulfurizing agent can be come by spray system by uniform rapid dispersion, carry out fully contacting anti-with the waste gas in tower
Should, desulfuration efficiency is high, and desulfurized effect is more obvious.
5th, the utility model, can be simultaneously to high temperature bulk composite fertilizer by setting hollow housing, crushing hammer and pusher disk
Raw material is cooled down, crushes and conveyed, and simplifies device structure, improves production efficiency；By setting square steel power transmission shaft,
Overall processing is molded, and structural soundness is good, and service life is long；Passed by setting steel tube driveshafts, and using hot charging joint steel pipe
Moving axis and connecting shaft, improve steel tube driveshafts stable connection, increase the service life；Observation panel is set on housing, can be at any time
Production status is observed, production procedure is adjusted at any time.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and examples：
Fig. 1 is structural representation of the present utility model；
Fig. 2 is structural representation of the present utility model；
Fig. 3 is structural representation of the present utility model；
In figure：Reaction tower 1, exhaust emission pipeline 2, body 201, fin 202 heats thin conduit 3, water-supply-pipe 4, supply tank
5, heat preservation storage water tank 6, flow distribution plate 7, annular water flow chamber 8, heat-insulation layer 9, three-way temperature control valve 10,
Desulfurizing tower 11, air inlet pipe 12, filter 13, escape pipe 14, spray equipment 15, pipeline 16, circulating pump 17, water outlet
Pipe 18, buffer unit 19, drainage trough 19-1, the first buffer pool 19-2, the second buffer pool 19-3, the first isolating device 19-5, the
Three buffer pool 19-4, the second isolating device 19-6, demister 20 clean pipe 21, screen pack 22, gear 23, medium inlet 24,
Crush hammer 25, power transmission shaft 26, shell 27, inner casing 28, pusher disk 29, shoving rake 30, material outlet 31, media outlet 32, observation
Mouth 33, material inlet 34, connecting shaft 35, gearbox 36, motor 37.
Embodiment
Further illustrate the utility model with reference to embodiment, but the claimed scope of the utility model not office
It is limited to the scope of embodiment statement.
Embodiment 1
A kind of production system for tobacco compound fertilizer, including reaction tower 1, the reaction tower 1 are provided with exhaust emission pipeline 2
Lorry is cooled down with composite fertilizer；
Heating thin conduit 3 is wound with the exhaust emission pipeline 2, the thin conduit 3 that heats is from exhaust emission pipeline 2
One end is unidirectionally wound to the other end, and water-supply-pipe 4 is provided with the outer sheath of exhaust emission pipeline 2；
The heating thin conduit 3 connects supply tank 5, heating thin conduit 3 and water-supply-pipe 4 with the water inlet of water-supply-pipe 4
Delivery port connects heat preservation storage water tank 6；
The exhaust gas flow heated in the water (flow) direction and exhaust emission pipeline 2 of thin conduit 3 and water-supply-pipe 4 is in opposite direction, institute
Exhaust emission pipeline 2 is stated including body 201, fin 202 is arranged at intervals with the side wall of body 201, the fin 202 it is interior
Portion is hollow, and the inside of fin 202 is connected with tubular body；
Preferably, the tube wall clear width of the water-supply-pipe 4 is provided with flow distribution plate 7, the water-supply-pipe 4 and tail gas discharging pipe
Annular water flow chamber 8 is formed between road 2, the flow distribution plate 7 and fin 202 are arranged in a crossed manner, flow distribution plate 7 is in ring with fin 202
Shape, water stream channel is formed between adjacent flow distribution plate 7 and fin 202；
The outside of the water-supply-pipe 4 is provided with heat-insulation layer 9, the heat-insulation layer 9 include successively from outside to inside layer of polyester fiber,
Wool felt and sponge；
The delivery port of the heating thin conduit 3 connects the wherein Single port of three-way temperature control valve 10, the three-way temperature control valve 10
Another port connected by pipeline with heat preservation storage water tank 6, the 3rd port of the three-way temperature control valve 10 passes through pipeline and water delivery
The water inlet connection of pipe.It can be specifically controlled according to the water temperature demand in heat preservation storage water tank 6, such as when needing water temperature higher
Heating thin conduit 3 can be made to be connected with water-supply-pipe 4, to proceed heating.Wanted when the temperature of the heating delivery port of thin conduit 3 can be met
, then can be by controlling three-way temperature control valve 10 to be directly discharged into heat preservation storage water tank 6 when asking.Can be in heat preservation storage water tank during specific design
Middle setting temperature sensor, the temperature sensor is connected with controller, and controller is connected with three-way temperature control valve, controls threeway temperature control
The conducting situation of valve.
Preferably, the exhaust emission pipeline 2 is connected with the bottom inflow pipe 12 of desulfurizing tower 11, and the top of desulfurizing tower 11 is set
Have inside escape pipe 14, the desulfurizing tower 11 and be provided with positioned at the lower section of escape pipe 14 outside spray equipment 15, the desulfurizing tower 11
Circulating pump 17 spray equipment 15 and buffer unit 19 are connected by pipeline 16, the bottom of desulfurizing tower 11 is additionally provided with outlet pipe 18
Connect buffer unit 19；
The buffer unit 19, which is provided between drainage trough 19-1, several buffer pools, several described buffer pools, is provided with phase
The isolating device being mutually staggeredly interconnected again.
It is further preferred that being provided with screen pack 22 in several described buffer pools；
The drainage trough 19-1 is connected with the first buffer pool 19-2, the first buffer pool 19-2 and the second buffer pool 19-3
Between provided with the first isolating device 19-5, the first isolating device 19-5 and the first buffer pool 19-2 close to drainage trough 19-1 mono-
Side seal is closed, and the first isolating device 19-5 and the first buffer pool 19-2 is unclosed away from drainage trough 19-1 sides；Described second
The second isolating device 19-6, the second isolating device 19-6 and second are provided between buffer pool 19-3 and the 3rd buffer pool 19-4
Buffer pool 19-3 is unclosed close to drainage trough 19-1 sides, and the isolating device 19-6 and the second buffer pool 19-3 are away from drainage trough
19-1 is one side closed.
It is further preferred that the outlet pipe 18 is connected with drainage trough 19-1, the 3rd buffer pool 19-4 passes through pipeline
It is connected with spray equipment 15；
The lower section of spray equipment 15 is provided with filter 13, and the filter 13 is distributed for several in fold-line-shaped
Filter layer is constituted.Desulfurizing agent is additionally provided with the filter layer, flue gas is sprayed into after liquid by spray equipment, passes through the mistake of lower section
Filtering layer carries out desulfurization layer by layer, and because filter layer is distributed in fold-line-shaped, increases time and the area of desulfurization absorption, improve
Desulfurized effect.
It is further preferred that the filter layer is non-woven fabrics or gauze, the air inlet pipe 12 is with the angle theta of desulfurizing tower 11
30-50 degree；
Demister 20 is provided between the spray equipment 15 and escape pipe 14, the demister 20 connects with cleaning pipe 21
Connect；The demister 20 is provided with several flooding nozzles；
The spray equipment 15 is at least one layer, and each layer is provided with several spray nozzles, and the spray nozzle is a diameter of
30-60nm。
Preferably, the height of air inlet pipe 12 is higher than outlet pipe 18, can prevent liquid from flowing backwards.
Preferably, composite fertilizer's cooling lorry includes setting on power transmission shaft 26, including power transmission shaft 26 in housing, housing
Crushing hammer 25 and pusher disk 29 are set gradually, housing two ends are respectively equipped with material outlet 31 and material inlet 34, material inlet 34
It is located at same one end, the connection drive device of power transmission shaft 26 with crushing hammer 25；Housing is hollow housing, hollow housing shell body two ends point
She You not medium inlet 24 and media outlet 32.
It is further preferred that the hammer 25 of crushing is interspersed on power transmission shaft 26；The front end of pusher disk 29 is provided with and pushed away
Claw 30；
The cross section of power transmission shaft 26 is square, circular or annular；
The power transmission shaft 26 is square steel power transmission shaft, and square steel power transmission shaft is molded for overall processing；
The two ends of power transmission shaft 26 are provided with connecting shaft 35；
The power transmission shaft 26 is steel tube driveshafts, and connecting shaft 35 is connected with steel tube driveshafts by hot charging.
The drive device includes motor 37, and the motor 37 connects gearbox 36, and the connecting shaft 35 is provided with gear
23, the gear 23 is connected with gearbox 36；
Observation panel 33 is set on the housing, and the observation panel 33 is located at same one end with material outlet 31；
The medium inlet 24 is located at the same one end of housing with material outlet 31.
Described composite fertilizer's cooling lorry, the high temperature bulk composite fertilizer of upper process production enters housing from material inlet
It is interior, crush hammer and high temperature bulk composite fertilizer is crushed, pusher disk promotes the composite fertilizer after crushing to move forward, from material outlet
Discharge；Cooling medium enters hollow housing from medium inlet, and from media outlet discharge, high-temperature sulfuric acid potassium in housing is cooled down
Cooling, cooling medium can be cooling water or cooling oil.
The utility model can be entered to high temperature bulk composite fertilizer simultaneously by setting hollow housing, crushing hammer and pusher disk
Row is cooled, crushes and conveyed, and is simplified device structure, is improved production efficiency.
The above embodiments are only optimal technical scheme of the present utility model, and are not construed as limit of the present utility model
Embodiment in system, the application and the feature in embodiment can be mutually combined in the case where not conflicting.The present invention's
Technical characteristic is equal in the technical scheme that protection domain should be recorded with claim, including the technical scheme of claim record
Alternative is protection domain.Equivalent substitution i.e. within this range is improved, also within protection domain of the present utility model.
Claims (8)
1. a kind of production system for tobacco compound fertilizer, including reaction tower（1）, it is characterised in that：The reaction tower（1）It is provided with
Exhaust emission pipeline（2）Lorry is cooled down with composite fertilizer；
The exhaust emission pipeline（2）On be wound with heating thin conduit（3）, the heating thin conduit（3）From exhaust emission pipeline
（2）One end be unidirectionally wound to the other end, in exhaust emission pipeline（2）Outer sheath be provided with water-supply-pipe（4）；
Heat thin conduit（3）Water inlet and water-supply-pipe（4）Water inlet connects supply tank（5）, heat thin conduit（3）Delivery port with
Water-supply-pipe（4）Delivery port connects heat preservation storage water tank（6）；
Heat thin conduit（3）With water-supply-pipe（4）Interior water (flow) direction and exhaust emission pipeline（2）In exhaust gas flow direction phase
Instead, the exhaust emission pipeline（2）Including body（201）, in body（201）Side wall on be arranged at intervals with fin（202）, institute
State fin（202）Inner hollow, and fin（202）Inside is connected with tubular body.
2. the production system according to claim 1 for tobacco compound fertilizer, it is characterised in that：The water-supply-pipe（4）'s
Tube wall clear width is provided with flow distribution plate（7）, the water-supply-pipe（4）With exhaust emission pipeline（2）Between formed annular water flow chamber
Room（8）, the flow distribution plate（7）With fin（202）It is arranged in a crossed manner, flow distribution plate（7）With fin（202）In a ring, flow distribution plate（7）
With fin（202）Between form water stream channel；
The water-supply-pipe（4）Outside be provided with heat-insulation layer（9）, the heat-insulation layer（9）Include polyester fiber successively from outside to inside
Layer, wool felt and sponge；
Heat thin conduit（3）Delivery port connects three-way temperature control valve（10）Wherein Single port, three-way temperature control valve（10）Another port
Pass through pipeline and heat preservation storage water tank（6）Connection, the three-way temperature control valve（10）The 3rd port entering by pipeline and water-supply-pipe
The mouth of a river is connected.
3. the production system according to claim 1 for tobacco compound fertilizer, it is characterised in that：The exhaust emission pipeline
（2）With desulfurizing tower（11）Bottom inflow pipe（12）Connection, the desulfurizing tower（11）Top is provided with escape pipe（14）, the desulfurizing tower
（11）It is internal and positioned at escape pipe（14）Lower section is provided with spray equipment（15）, the desulfurizing tower（11）Outside circulating pump（17）It is logical
Piping（16）Connect spray equipment（15）And buffer unit（19）, the desulfurizing tower（11）Bottom is additionally provided with outlet pipe（18）Even
Logical buffer unit（19）；
The buffer unit（19）Provided with drainage trough（19-1）, several buffer pools, phase is provided between several described buffer pools
The isolating device being mutually staggeredly interconnected again.
4. the production system according to claim 3 for tobacco compound fertilizer, it is characterised in that：Several described buffer pools
It is interior to be provided with screen pack（22）；
The drainage trough（19-1）With the first buffer pool（19-2）Connection, first buffer pool（19-2）With the second buffer pool
（19-3）Between be provided with the first isolating device（19-5）, first isolating device（19-5）With the first buffer pool（19-2）It is close
Drainage trough（19-1）It is one side closed, first isolating device（19-5）With the first buffer pool（19-2）Away from drainage trough（19-1）
Side is unclosed；Second buffer pool（19-3）With the 3rd buffer pool（19-4）Between be provided with the second isolating device（19-6）,
Second isolating device（19-6）With the second buffer pool（19-3）Close to drainage trough（19-1）Side is unclosed, the isolation dress
Put（19-6）With the second buffer pool（19-3）Away from drainage trough（19-1）It is one side closed.
5. the production system according to claim 4 for tobacco compound fertilizer, it is characterised in that：The outlet pipe（18）With
Drainage trough（19-1）Connection, the 3rd buffer pool（19-4）Pass through pipeline and spray equipment（15）Connection；
The spray equipment（15）Lower section is provided with filter（13）, the filter（13）It is distributed for several in fold-line-shaped
Filter layer composition.
6. the production system according to claim 5 for tobacco compound fertilizer, it is characterised in that：The filter layer is nonwoven
Cloth or gauze, the air inlet pipe（12）With desulfurizing tower（11）Angle theta is 30-50 degree；
The spray equipment（15）With escape pipe（14）Between be provided with demister（20）, the demister（20）Managed with cleaning
（21）Connection；The demister（20）It is provided with several flooding nozzles；
The spray equipment（15）At least one layer, each layer is provided with several spray nozzles, a diameter of 30- of spray nozzle
60nm。
7. the production system according to claim 1 for tobacco compound fertilizer, it is characterised in that：Composite fertilizer's cooling is pushed away
Truck includes setting power transmission shaft in housing, housing（26）, including power transmission shaft（26）On set gradually crushing hammer（25）With pusher disk
（29）, housing two ends are respectively equipped with material outlet（31）And material inlet（34）, material inlet（34）Hammered into shape with crushing（25）It is located at
Same one end, power transmission shaft（26）Connect drive device；Housing is hollow housing, and hollow housing shell body two ends are respectively equipped with medium and entered
Mouthful（24）And media outlet（32）.
8. the production system according to claim 7 for tobacco compound fertilizer, it is characterised in that：It is described to crush hammer（25）Hand over
Mistake is distributed in power transmission shaft（26）On；The pusher disk（29）Front end is provided with shoving rake（30）；
The power transmission shaft（26）Cross section is square, circular or annular；
The power transmission shaft（26）For square steel power transmission shaft, square steel power transmission shaft is molded for overall processing；
The power transmission shaft（26）Two ends are provided with connecting shaft（35）；
The power transmission shaft（26）For steel tube driveshafts, connecting shaft（35）It is connected with steel tube driveshafts by hot charging；
The drive device includes motor（37）, the motor（37）Connect gearbox（36）, the connecting shaft（35）It is provided with
Gear（23）, the gear（23）With gearbox（36）Connection；
Observation panel is set on the housing（33）, the observation panel（33）With material outlet（31）Positioned at same one end；
The medium inlet（24）With material outlet（31）Positioned at the same one end of housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720179142.8U CN206535526U (en) | 2017-02-27 | 2017-02-27 | A kind of production system for tobacco compound fertilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720179142.8U CN206535526U (en) | 2017-02-27 | 2017-02-27 | A kind of production system for tobacco compound fertilizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206535526U true CN206535526U (en) | 2017-10-03 |
Family
ID=59946370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720179142.8U Expired - Fee Related CN206535526U (en) | 2017-02-27 | 2017-02-27 | A kind of production system for tobacco compound fertilizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206535526U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113578445A (en) * | 2021-07-26 | 2021-11-02 | 高健文 | High-efficiency dust-free active carbon grinding device |
-
2017
- 2017-02-27 CN CN201720179142.8U patent/CN206535526U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113578445A (en) * | 2021-07-26 | 2021-11-02 | 高健文 | High-efficiency dust-free active carbon grinding device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100372605C (en) | Movable sulfurization active carbon heating regenerator and regeneration | |
| CN113797659B (en) | Blast furnace flue gas purification device with heat energy conversion utilizes | |
| CN103836948B (en) | A kind of fluidizing reactor of high-carbon molybdenum-nickel ore and system | |
| CN108514807A (en) | A kind of counterflow moving bed filter for installation | |
| CN106000068A (en) | Micro-temperature-variation energy-saving and smoke-eliminating system with ultra-low SO2 emission | |
| CN206535526U (en) | A kind of production system for tobacco compound fertilizer | |
| CN109107343A (en) | A kind of production system for tobacco compound fertilizer | |
| CN206027419U (en) | Desulfurization system with circulation slurry spray system and double -deck tubular flue gas uniform distributor | |
| CN101961597A (en) | Compact high-efficiency flue gas desulphurization device | |
| CN104324602B (en) | A kind of smoke exhaust pollution sources control device and process | |
| CN104368278B (en) | A kind of filtering type sulfur melting kettle | |
| RU2627808C1 (en) | Device for cleaning and utilisation of flue gases of roof boiler | |
| CN206069798U (en) | Drop a hint during a kind of u gas gasification furnace driving and parking water washing dedust device | |
| CN206121421U (en) | Exhaust -gas treatment is with defeated tuber pipe | |
| CN212818972U (en) | Colored smoke plume desorption system of high temperature water flushing sediment steam | |
| CN104787729A (en) | Sulfur steam collecting device and sulfur steam collecting method | |
| CN206276224U (en) | A kind of desulphurization system for composite heat transfer | |
| CN112933905A (en) | Efficient and energy-saving graphitized tail gas treatment system and treatment process thereof | |
| CN204661323U (en) | A kind of sulphur vapor collection setup | |
| CN203139848U (en) | Dust removing system for cast pouring | |
| CN201108791Y (en) | Three-layer jet nozzle cooling apparatus | |
| CN201799212U (en) | Compact type high-efficiency flue gas desulfurization device | |
| CN206950961U (en) | A kind of composite heat transfer system | |
| CN206549433U (en) | A kind of efficient removable miniature smoke eliminator | |
| CN205948562U (en) | Smoke and dust waste heat utilization and ash purification treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171003 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |