CN205119460U - Spiral plate type hot -blast furnace and use rape whirlwind formula flash distillation drying -machine of this hot -blast furnace - Google Patents
Spiral plate type hot -blast furnace and use rape whirlwind formula flash distillation drying -machine of this hot -blast furnace Download PDFInfo
- Publication number
- CN205119460U CN205119460U CN201520800433.5U CN201520800433U CN205119460U CN 205119460 U CN205119460 U CN 205119460U CN 201520800433 U CN201520800433 U CN 201520800433U CN 205119460 U CN205119460 U CN 205119460U
- Authority
- CN
- China
- Prior art keywords
- air
- heat exchanger
- flow
- spiral
- hot
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a spiral plate type hot -blast furnace, the furnace who includes spiral plate heat exchanger, hot -blast furnace shell and be used for heating, spiral plate heat exchanger includes spiral heat exchanger, lower spiral heat exchanger, two go up the spiral plate, twice spiral plates and center tube, treat the helical coiled passage opening inflow of the air current of heating from last / lower spiral heat exchanger, helical coiled passage through last spiral heat exchanger under with, under following / upward spiral heat exchanger's helical coiled passage opening outflow, a helical coiled passage upwards flows into for heating the hot gas flow from last spiral heat exchanger with down spiral heat exchanger is adjacent with above -mentioned helical coiled passage, two strands of air currents along the adjacent flow of helical coiled passage in the helical coiled passage, use this heated gas that treats for flowing into to spread heat, radiation and convection current principle are adopted in the heat exchange, clean hot air drying material has been guaranteed. The utility model also discloses a rape whirlwind formula flash distillation drying -machine of using this spiral plate type hot -blast furnace.
Description
Technical field
The utility model relates to field of agricultural machinery, especially a kind of screw plate type hot-air furnace and use the rape cyclone type flash dryer of this hot-blast stove.
Background technology
The waste situation producing rapeseed in the storage of rapeseed owing to going mouldy is very serious.Because rapeseed gathers in the crops Yangtze river basin plum rain season just, the rapeseed moisture content of results is between 15% ~ 30%, rapeseed seed footpath is 1.27 ~ 2.10mm, between particle, gap is less, and heat transfer is slow, not easy heat radiation dehydration, additional respiratory intensity is higher, easy heating is gone mouldy, so the wet oil vegetable seed of fresh harvest has to pass through applicable drying, and can safe storage.The traditional natural drying efficiency of rapeseed very low, the manpower that the process need such as rapeseed is piled up, spread out, carrying is a large amount of, adds the burden of rapeseed processing enterprise cost.Therefore employing rapeseed mechanical drying is the important development trend of modern rapeseed processing enterprise.
That commonly uses in drying equipment at home has drying generator, is positioned in the warehouse of ventilating system, utilizes the fresh material of results the hot-air of natural air or uniform temperature as drying medium, carry out force ventilation cyclic drying to material.But drying generator amount is large, drying time is uncertain large, causes material easy appearance part in dry run to generate heat mildew phenomena.
Another kind of common equipment is then that convection type is dry, operation principle carrys out the air in absorbing environmental with blower fan and is heated the temperature required by the specific material of drying, by the air after heating through drying hopper, and by the mode heated material of convection current to remove moisture.But the drying efficiency of the convection type drying that domestic market occurs is low, and dry amount is little, can not meet the needs of production.Therefore be necessary to design the Novel drying device for granule materials such as rapeseed that a kind of cost is lower, drying efficiency is high.
Utility model content
The utility model provides high, the clean clean screw plate type hot-air furnace of a kind of heat exchange efficiency and uses the rape cyclone type flash dryer of this hot-blast stove.
For achieving the above object, the technical solution of the utility model is as follows:
A kind of screw plate type hot-air furnace, comprises spiral heat exchanger, hot-blast stove shell and the burner hearth for heating; Described spiral heat exchanger comprises spiral plate on spiral heat exchanger, lower spiral heat exchanger, two, twice spiral plates and central tube, and described upper spiral heat exchanger and lower spiral heat exchanger make two helical ducts spaced apart from each other up and down of equivalent size size by the roll of steel plate that two pieces are parallel to each other; Described upper spiral plate and lower spiral plate are made corresponding with the helical duct entering air-flow process of upper spiral heat exchanger and lower spiral heat exchanger spiral-shaped by steel plate, two blocks of upper spiral plates are connected in spiral heat exchanger upper and lower side blanket gas circulation road, and two blocks of lower spiral plates are connected in lower spiral heat exchanger upper and lower side blanket gas circulation road; The spiral center equal diameters of described central tube and upper spiral parallel operation and lower spiral heat exchanger and center are opened and a sector region of the initial same widths by helical duct of lower spiral heat exchanger air-flow and the upper and lower welded seal of central tube, central tube inserts in upper spiral heat exchanger and lower spiral heat exchanger, and spiral heat exchanger is connected by sector region with the helical duct of lower spiral heat exchanger; Air-flow to be heated flows into from the helical duct opening of up/down spiral heat exchanger, through the helical duct of upper spiral heat exchanger and lower spiral heat exchanger, flow out from the helical duct opening of lower/upper spiral heat exchanger, thermal current for heating upwards flows into from the helical duct that upper spiral heat exchanger is adjacent with above-mentioned helical duct with lower spiral heat exchanger, two strands of air-flows in helical duct are along helical duct adjacent flow, as the air-flow heat transfer to be heated flowed into, heat exchange adopts radiation and convective principles, ensure that clean heated air drying material; Flue is provided with in the middle of described burner hearth, described screw plate type hot-air furnace outside forms hot-blast stove shell by cylindrical shape Plate Welding, separated by steel plate between described flue and lower spiral heat exchanger, produce thermal current own in screw plate type hot-air furnace by heating in flue.
Wherein, described hot-blast stove shell upper and bottom are cylindrical, bottom is larger relative to shaped upper part, centre is by the Plate Welding of taper, described stove cylinder top is provided with furnace crown, the side of described furnace crown is provided with exhaust outlet, and described spiral heat exchanger and heating component are all arranged at hot-blast stove outer casing underpart.
Wherein, described burner hearth inside is provided with a cylindrical steel plate, and it is inner forms flue, formed between described cylindrical steel plate and hot-blast stove shell one with the passage of lower spiral heat exchanger air outlet formed objects, allow and to be passed through by the air-flow after heating, flow out from the air outlet bottom furnace enclosure.
Wherein, described upper spiral plate and lower spiral plate reserve a part and do not cut, central tube height a little more than upper spiral heat exchanger, for location and installation.
Wherein, described burner hearth also comprises firewood adding hole, and on one, annulus is located under firewood adding hole, and upper annulus is provided with many fire grate seamless pipes, and upper annulus lower end is provided with ash hole.
Rape cyclone type flash dryer, comprise screw plate type hot-air furnace as above, and driving mechanism, centrifugal high pressure fan, valve-type feeder, drier, whirlwind collector, Star-like unloader, hot-blast stove air outlet is connected with the circular passage entrance of valve-type feeder lower end of duct and drying bottom, described whirlwind collector top is provided with helical airflow inlet tube and air guide outlet, be connected with fan inlet pipe with drier respectively, lower end is connected with Star-like unloader by whirlwind collector lower taper pipe; During heating, driving mechanism drives draught fan impeller to rotate and produces air-flow, the air intake vent pipe that air-flow flows into screw plate type hot-air furnace top through fan outlet pipe flows into inner helical duct again, air-flow is along passage screw, in hot-blast stove, thermal current own upwards flows into from adjacent helical duct, and two strands of air-flows in helical duct, along helical duct adjacent flow, conduct heat as the air-flow flowed into, heat exchange adopts radiation and convective principles, ensure that clean heated air drying material; Flowed out by the air outlet pipe that the air-flow after conducting heat flows out through hearth of hot-blast stove bottom from helical duct, carry and enter into drier by spiral air intake vent from drier base position from the material of valve-type feeder feeding, and after the classified device classification in drier top, the material of drying is sent into whirlwind collector, the air-flow rotated contracts to center flow in whirlwind rewinding body adduction, upwards form secondary vortex flow, air guide outlet through top flows into the inlet tube of draught fan impeller, carry waste heat and start heat drying operation next time, the gas flow loop that formation one is closed thus.
Wherein, described fan outlet pipe and the air intake vent pipe of screw plate type hot-air furnace have certain gap, the inlet tube that the high-temperature high-pressure air flow of discharging from whirlwind tripper top wireway is admitted to draught fan impeller enters the drying that heat-exchanging furnace continues to heat up for material, and in high-temperature high-pressure air flow, entrained a small amount of assorted excess separated through cyclone separator is discharged outside body because of the existence in the gap of the air intake vent pipe of fan outlet pipe and screw plate type hot-air furnace before the air intake vent pipe entering screw plate type hot-air furnace.
Wherein, described drier comprises hothouse, clasfficiator, base, and wherein hothouse consists of connector multistage hollow cylindrical container, on hothouse top, clasfficiator is housed, base position connects the air inlet offering tangential direction, is upwards fluidisation section between clasfficiator from drier bottom; Material feeds from valve-type feeder, the circulating line carried bottom material drying device by air-flow tangentially enters fluidisation section, form the rotation spray moving air flow of high velocity, low pressure, material carries out heat and mass transfer process at fluidisation Duan Zhongyu air-flow, moisture removes gradually, be able to drying, material is subject to spiralling airflow entrainment and moves to clasfficiator, and the dry material particle reaching drying requirement enters in whirlwind collector with air-flow by clasfficiator centre bore because moisture content is low accumulating to drier axis position; The material particles not reaching drying requirement will be in empty periphery, clasfficiator center be graded device stop appoint so stay in drier continue dry, until reach the material water ratio requirement that drying specifies, dry material particles up to standard enters whirlwind collector with air-flow by clasfficiator centre bore, move downward along spiral inner wall formula, material particles is subject to get rid of to wall under the effect of centrifugal force in whirlwind collector, and fall under gravity into Star-like unloader, and clear foreign material are separated under the effect of whirlwind collector.
Wherein, described drier is also provided with base, and it is set to spiral of Archimedes structure and air inlet duct width reduces gradually, reaches minimum at drier air inlet duct width, and air-flow flow to drier air inlet wind speed and reaches maximum.
Wherein, described Star-like unloader comprises the impeller of rotor of several pieces blades, housing, seal and motor, described Star-like unloader upper end is provided with flange port, the impeller of rotor axis direction that flange port lower end is provided with is concentric with electrical axis, discharger outer wall is housing, top accepts the material that whirlwind collector is discharged, the impeller of rotor rotated is relied on to play at the uniform velocity discharge and sealing function, when the material flowed out from whirlwind collector to fall by deadweight in the space be filled between impeller of rotor, the rotation with impeller of rotor draws off.
The beneficial effects of the utility model are:
1, the utility model heat exchange adopts radiation and convective principles, ensure that clean heated air drying material, is highly suitable for the drying of the crops such as rapeseed.
2, the screw plate type hot-air furnace of the utility model rape cyclone type flash dryer use, its spiral heat exchanger is provided with at least one pair of spirality channel spaced apart from each other, air-flow can conduct heat along helical duct adjacent flow, be delayed the time that air-flow moves in hot-blast stove, heat exchange between air-flow is more abundant, and heat utilization rate is high.Further, the thermal current with ashes in the air-flow of Dryly use and hot-blast stove is isolated, and can obtain clean air-flow during drying machine operation;
3, the utility model screw plate type hot-air furnace reserves a part and does not cut (i.e. dash area in Fig. 7, Fig. 8), and central tube height, a little more than upper spiral heat exchanger, for location and installation, reduces installation difficulty.
4, have between the utility model screw plate type hot-air furnace steel plate and hot-blast stove shell one with the passage of lower spiral heat exchanger air outlet formed objects, allow and to be passed through by the air-flow after heating, flow out from the air outlet bottom furnace enclosure, is combined closely in space between spiral heat exchanger and burner hearth and use, effectively save space again.
Accompanying drawing explanation
Fig. 1 is the overall schematic front view of the utility model embodiment rape cyclone type flash dryer.
Fig. 2 is the overall schematic top plan view of the utility model embodiment rape cyclone type flash dryer.
Fig. 3 is the utility model embodiment screw plate type hot-air furnace members schematic diagram.
Fig. 4 is the central tube schematic diagram of the utility model embodiment.
Fig. 5 is the upper spiral heat exchanger top view of the utility model embodiment.
Fig. 6 is the lower spiral heat exchanger top view of the utility model embodiment.
Fig. 7 is the upper spiral plate top view of the utility model embodiment.
Fig. 8 is the lower spiral plate top view of the utility model embodiment.
Fig. 9 is the burner hearth fragmentary front view of the utility model embodiment.
Figure 10 is the burner hearth top partial view diagram of the utility model embodiment.
Figure 11 is the burner hearth partial side elevation view of the utility model embodiment.
Figure 12 is the whirlwind collector of the utility model embodiment and the side view of Star-like unloader.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described further.
See Fig. 1 to Figure 12, the present embodiment rape cyclone type flash dryer comprises frame 1, variable-frequency motor 2, centrifugal high pressure fan 3, belt transmission group mechanism 4, screw plate type hot-air furnace 5, screw K type M6 metric system thermocouple 6, valve-type feeder 7, drier 8, whirlwind collector 9, Star-like unloader 10.Belt transmission group mechanism 4 comprises belt 42, shaft coupling 41, described shaft coupling 41 shell is semicircle and both sides extended spot rectangular slab is threaded with frame, described shaft coupling 41 on one side axle is connected with the axle of variable-frequency motor 2 by belt 42, and another side axle and centrifugal high pressure fan 3 internal impeller 31 are connected.Described centrifugal high pressure fan 3 comprises impeller 31, fan supporter 32, blower housing 33, fan inlet pipe 98, the blower housing 33 of described centrifugal high pressure fan 3 designs with the form fit impeller 31 of A Ji meter helix, be connected in frame 1 by the fan supporter 32 be welded on blower housing 33, the pipeline air outlet of blower housing 33 is relative with screw plate type hot-air furnace 5 air intake vent concentric and leave certain interval, is convenient to record wind speed.Described impeller 31 is connected by axle with shaft coupling 41, vertical direction is placed in blower housing 33, described impeller 31 is faced impeller 31 direction with shaft coupling 41 and is rotated clockwise generation air-flow, flows in screw plate type hot-air furnace 5 from the pipeline air outlet of described blower housing 33.
Described screw plate type hot-air furnace 5 comprises firewood adding hole 51, furnace enclosure 52, flue 53, annulus 54, fire grate seamless pipe 55, ash hole 56, airflow line 57, upper spiral heat exchanger 58, lower spiral heat exchanger 59, hot-blast stove shell 11, upper spiral plate 12, lower spiral plate 13, central tube 14, stove cylinder 15 and furnace crown 16.Described hot-blast stove shell 11 bottom is larger cylinder steel plate, and top is stove cylinder 15 is cylinder steel plates that shape is less, and centre is by the Plate Welding of taper, and described stove cylinder 15 top is furnace crown 16, and the side of described furnace crown 16 is provided with exhaust outlet.Described firewood adding hole 51 is set to and is cylindrically connected on furnace enclosure 52, for cylindrical steel plate is formed in described flue 53, described annulus 54 is welded on burner hearth, annulus 54 is welded with the fire grate seamless pipe 55 of ten different sizes, all leave certain space between every root fire grate seamless pipe 55, play the function of being convenient to put fuel and downward ash discharge.Described ash hole 56 is set to cuboid, is arranged on annulus 54 and firewood adding hole 51 bottom.Separated by steel plate between described flue 53 and lower spiral heat exchanger 59, being used for isolated fuel contamination gas and so on enters in air-flow.The steel plate that described upper spiral heat exchanger 58 and lower spiral heat exchanger 59 are parallel to each other by two pieces, roll into two spirality channels spaced apart from each other up and down of equivalent size size, be positioned at the comparatively large cylinder steel plate upper end of hot-blast stove shell 11, the air intake vent of upper spiral heat exchanger 58 is connected with screw plate type hot-air furnace 5 air intake vent.Upper spiral plate 12 and lower spiral plate 13 cut into corresponding with the helical duct entering air-flow process of upper spiral heat exchanger 58 and lower spiral heat exchanger 59 spiral-shaped by steel plate, and reserve a part and do not cut (i.e. dash area in Fig. 7, Fig. 8), be convenient to location and installation, two blocks of upper spiral plates 12 are welded on spiral heat exchanger 58 upper and lower side blanket gas circulation road, and two blocks of lower spiral plates 13 are welded on lower spiral heat exchanger 59 upper and lower side blanket gas circulation road.The spiral center equal diameters of described central tube 14 and upper spiral parallel operation 58 and lower spiral heat exchanger 59 and center are opened and a sector region of the initial same widths by helical duct of lower spiral heat exchanger 59 air-flow and central tube about 14 welded seal, central tube 14 inserts in upper spiral heat exchanger 58 and lower spiral heat exchanger 59, it is a little that central tube 14 will exceed upper spiral heat exchanger 58, is convenient to install.Described flue 53 top is welded with one block of circular steel plate, formed between steel plate and hot-blast stove shell 11 one with the passage of lower spiral heat exchanger 59 air outlet formed objects, allow and to be passed through by the air-flow after heating, flow out from the air outlet bottom furnace enclosure 52.This programme heat exchange adopts radiation and convective principles, ensure that clean heated air drying material.Air-flow flows into inner helical duct from the air intake vent of screw plate type hot-air furnace 5, air-flow is along passage screw, in screw plate type hot-air furnace 5, thermal current own upwards flows into from adjacent helical duct, two strands of air-flows in helical duct are along helical duct adjacent flow, as the air-flow heat transfer flowed into, flow out from helical duct after the air-flow being used in screw plate type hot-air furnace 5 conducting heat conducts heat and move upward along stove cylinder, from the furnace crown be provided with 16 mouthfuls outflow, flowed out by the air outlet that the air-flow after conducting heat flows out through hot-blast stove lower furnace shell 52 from helical duct.
Described screw K type M6 metric system thermocouple 6 is filled between hot-blast stove discharge pipe and valve-type feeder 7, described valve-type feeder 7 comprises feeding mouth pipeline 71 and valve 72, described feeding mouth pipeline 71 upper end is set to column type feeding mouth, feeding mouth cover plate is made up of the circular steel plate of loose-leaf system, the column type pipeline that lower end welding is tilted, weld with hot-blast stove discharge pipe, middle-end by taper steel plate by upper-lower section weld and taper steel plate lower end is provided with spiral valve 72, described valve 72 and the interface of pipeline are set to the circular steel plate equal with line size.Before air-flow flows into drier 8, measure gas flow temperature by the screw K type M6 metric system thermocouple 6 between spiral hot-blast stove 5 air outlet pipe and reinforced organ pipe, material feeds from valve-type feeder 7.The circulating line carried bottom material drying device 8 by air-flow tangentially enters fluidisation section, forms the rotation spray moving air flow of high velocity, low pressure.
Described drier 8 is made up of hothouse 83, clasfficiator 81, base 82, outlet water law orchid 84, flange fagging 85, flange 86 etc., wherein hothouse consists of flange fagging 85, flange 86 multistage hollow cylindrical container, on hothouse 83 top, clasfficiator 81 is housed, base 82 place connects the air inlet offering tangential direction.The structure that described outlet water law orchid 84 is set to square-outside and round-inside is threaded with cyclone separator 9 air intake pipe orifice at drier 8 top, the circular baffle plate that described clasfficiator 81 is set to band centre bore is formed, described flange 86 is set to the loop configuration of cylindrical inner circle, described clasfficiator 81 is mounted between upper and lower flange 86 by installation number demand screw, play a supportive role between the bucket wall that described flange fagging 85 is welded on flange 86 and drier 8, described drier 8 and spiral hot-blast stove 5 shell are all with the insulation of heat-preservation cotton parcel.Described base 82 is set to spiral of Archimedes structure and air inlet duct width reduces gradually, reaches minimum at drier 8 air inlet duct width, and air-flow flow to drier 8 air inlet wind speed and reaches maximum.The circulating line carried bottom material drying device 8 by air-flow tangentially enters fluidisation section, forms the rotation spray moving air flow of high velocity, low pressure.Air-flow is upwards fluidisation section from base 82 between clasfficiator, and material carries out heat and mass transfer process at fluidisation Duan Zhongyu air-flow, and moisture removes gradually, is able to drying.Material moves to clasfficiator 81 along with spiralling airflow entrainment, and dry material particle continues the centre bore moving up through clasfficiator 81; Wet stock particle spiral around wall moves upward and to collide with clasfficiator 81 and to fall under gravity, and shuttling movement is dry with this again, until reach the quality of material requirement that drying specifies.Dry material particles up to standard with air-flow by clasfficiator 81 by dryer export water law orchid 84 by tangentially entering whirlwind collector 9.
Described whirlwind collector 9 comprises shell 91, helical airflow inlet tube 92 and air guide outlet 93.Described helical airflow inlet tube 92 is set to spiral of Archimedes structure installment in whirlwind collector 9 upper end, described air guide outlet 93 is arranged on whirlwind collector 9 top, described shell 91 lower end is set to conical pipe, and described drier 8 and whirlwind collector 9 each layer interface place silicone gasket seal and scribble fluid sealant and prevent gas leakage.Air-flow moves downward along spiral inner wall formula, and material particles gets rid of under the influence of centrifugal force to wall, and falls under gravity into Star-like unloader 10.
Described Star-like unloader 10 comprises housing 94, impeller of rotor 95, seal 96 and motor 97.Housing 94 upper end is provided with flange port, strictly seal with the Star-like unloader interface of described whirlwind collector and bottom, using Star-like unloader 10 as the rewinding room of whirlwind collector 9, the impeller of rotor 95 be provided with in described housing 94 is coaxial with motor 97, and the axle portion between impeller of rotor 95 and motor 97 seals by described seal 96.When the material flowed out from whirlwind collector 9 to fall by deadweight in the space be filled between impeller of rotor 95, the rotation with impeller of rotor 95 draws off from bottom, and therefore, Star-like unloader 10 can quantitatively and continuously discharging; Through the negative-pressure sealing of Star-like unloader 10, the air-flow of rotation shrinks to center flow in whirlwind collector 9 body, upwards forms secondary vortex flow, and the air guide outlet 93 through top flows into the inlet tube 98 of draught fan impeller, the gas flow loop that formation one is closed thus.
The utility model rape cyclone type flash dryer operation principle is: during drying machine operation, variable-frequency motor drives draught fan impeller to rotate by belt gear and produces air-flow, the air intake vent pipe that air-flow flows into screw plate type hot-air furnace top through fan outlet pipe flows into inner helical duct again, air-flow is along passage screw, in hot-blast stove, thermal current own upwards flows into from adjacent helical duct, two strands of air-flows in helical duct are along helical duct adjacent flow, as the air-flow heat transfer flowed into, flow out from helical duct after the air-flow being used in stove conducting heat conducts heat and move upward along stove cylinder, flow out from the furnace crown mouth be provided with, flowed out by the air outlet pipe that the air-flow after conducting heat flows out through hot-blast stove lower furnace from helical duct.Before air-flow flows into drier, by the screw K type M6 metric system thermocouple measurement gas flow temperature between hot-blast stove air outlet pipe and reinforced organ pipe, material feeds from valve-type feeder, the circulating line carried bottom material drying device by air-flow tangentially enters fluidisation section, forms the rotation spray moving air flow of high velocity, low pressure.Material carries out heat and mass transfer process at fluidisation Duan Zhongyu air-flow, and moisture removes gradually, is able to drying.Material moves to clasfficiator along with spiralling airflow entrainment, and dry material particle continues to move up through clasfficiator centre bore; Wet stock particle spiral around wall moves upward and to collide with clasfficiator and to fall under gravity, and shuttling movement is dry with this again, until reach the quality of material requirement that drying specifies.Dry material particles up to standard tangentially enters whirlwind collector by clasfficiator by drier top exit water law orchid with air-flow, and move downward along spiral inner wall formula, material particles gets rid of under the influence of centrifugal force to wall, and falls under gravity into Star-like unloader.When the material flowed out from whirlwind collector to fall by deadweight in the space be filled between impeller of rotor, the rotation with impeller of rotor draws off from bottom, and therefore, Star-like unloader can quantitatively and continuously discharging; Through the negative-pressure sealing of discharger, the air-flow of rotation is in the contracting of whirlwind rewinding body adduction to center flow, and upwards form secondary vortex flow, the air guide outlet through top flows into the inlet tube of draught fan impeller, the gas flow loop that formation one is closed thus.Like this, both achieved the degassing function of air-introduced machine, again thermal current had been recycled, again substantially increased heat utilization rate.
Claims (10)
1. a screw plate type hot-air furnace, is characterized in that, comprises spiral heat exchanger, hot-blast stove shell and the burner hearth for heating; Described spiral heat exchanger comprises spiral plate on spiral heat exchanger, lower spiral heat exchanger, two, twice spiral plates and central tube, and described upper spiral heat exchanger and lower spiral heat exchanger make two helical ducts spaced apart from each other up and down of equivalent size size by the roll of steel plate that two pieces are parallel to each other; Described upper spiral plate and lower spiral plate are made corresponding with the helical duct entering air-flow process of upper spiral heat exchanger and lower spiral heat exchanger spiral-shaped by steel plate, two blocks of upper spiral plates are connected in spiral heat exchanger upper and lower side blanket gas circulation road, and two blocks of lower spiral plates are connected in lower spiral heat exchanger upper and lower side blanket gas circulation road; The spiral center equal diameters of described central tube and upper spiral parallel operation and lower spiral heat exchanger and center are opened and a sector region of the initial same widths by helical duct of lower spiral heat exchanger air-flow and the upper and lower welded seal of central tube, central tube inserts in upper spiral heat exchanger and lower spiral heat exchanger, and spiral heat exchanger is connected by sector region with the helical duct of lower spiral heat exchanger; Air-flow to be heated flows into from the helical duct opening of up/down spiral heat exchanger, through the helical duct of upper spiral heat exchanger and lower spiral heat exchanger, flow out from the helical duct opening of lower/upper spiral heat exchanger, thermal current for heating upwards flows into from the helical duct that upper spiral heat exchanger is adjacent with above-mentioned helical duct with lower spiral heat exchanger, two strands of air-flows in helical duct are along helical duct adjacent flow, as the air-flow heat transfer to be heated flowed into, heat exchange adopts radiation and convective principles, ensure that clean heated air drying material; Flue is provided with in the middle of described burner hearth, described screw plate type hot-air furnace outside forms hot-blast stove shell by cylindrical shape Plate Welding, separated by steel plate between described flue and lower spiral heat exchanger, produce thermal current own in screw plate type hot-air furnace by heating in flue.
2. screw plate type hot-air furnace according to claim 1, it is characterized in that, described hot-blast stove shell upper and bottom are cylindrical, bottom is larger relative to shaped upper part, centre is by the Plate Welding of taper, described stove cylinder top is provided with furnace crown, and the side of described furnace crown is provided with exhaust outlet, and described spiral heat exchanger and heating component are all arranged at hot-blast stove outer casing underpart.
3. screw plate type hot-air furnace according to claim 1, it is characterized in that, described burner hearth inside is provided with a cylindrical steel plate, its inner formation flue, formed between described cylindrical steel plate and hot-blast stove shell one with the passage of lower spiral heat exchanger air outlet formed objects, allow and to be passed through by the air-flow after heating, flow out from the air outlet bottom furnace enclosure.
4. screw plate type hot-air furnace according to claim 1, is characterized in that, described upper spiral plate and lower spiral plate reserve a part and do not cut, central tube height a little more than upper spiral heat exchanger, for location and installation.
5. screw plate type hot-air furnace according to claim 1, is characterized in that, described burner hearth also comprises firewood adding hole, and on one, annulus is located under firewood adding hole, and upper annulus is provided with many fire grate seamless pipes, and upper annulus lower end is provided with ash hole.
6. a rape cyclone type flash dryer, it is characterized in that, comprise as the screw plate type hot-air furnace as described in arbitrary in claim 1 to 5, and driving mechanism, centrifugal high pressure fan, valve-type feeder, drier, whirlwind collector, Star-like unloader, hot-blast stove air outlet is connected with the circular passage entrance of valve-type feeder lower end of duct and drying bottom, described whirlwind collector top is provided with helical airflow inlet tube and air guide outlet, be connected with fan inlet pipe with drier respectively, lower end is connected with Star-like unloader by whirlwind collector lower taper pipe, during heating, driving mechanism drives draught fan impeller to rotate and produces air-flow, the air intake vent pipe that air-flow flows into screw plate type hot-air furnace top through fan outlet pipe flows into inner helical duct again, air-flow is along passage screw, in hot-blast stove, thermal current own upwards flows into from adjacent helical duct, and two strands of air-flows in helical duct, along helical duct adjacent flow, conduct heat as the air-flow flowed into, heat exchange adopts radiation and convective principles, ensure that clean heated air drying material, flowed out by the air outlet pipe that the air-flow after conducting heat flows out through hearth of hot-blast stove bottom from helical duct, carry and enter into drier by spiral air intake vent from drier base position from the material of valve-type feeder feeding, and after the classified device classification in drier top, the material of drying is sent into whirlwind collector, the air-flow rotated contracts to center flow in whirlwind rewinding body adduction, upwards form secondary vortex flow, air guide outlet through top flows into the inlet tube of draught fan impeller, carry waste heat and start heat drying operation next time, the gas flow loop that formation one is closed thus.
7. rape cyclone type flash dryer according to claim 6, it is characterized in that, described fan outlet pipe and the air intake vent pipe of screw plate type hot-air furnace have certain gap, the inlet tube being admitted to draught fan impeller from the high-temperature high-pressure air flow of whirlwind tripper top wireway discharge enters the drying of heat-exchanging furnace continuation intensification for material, in high-temperature high-pressure air flow, entrained a small amount of assorted excess separated through cyclone separator is discharged outside body because of the existence in the gap of the air intake vent pipe of fan outlet pipe and screw plate type hot-air furnace before the air intake vent pipe entering screw plate type hot-air furnace.
8. rape cyclone type flash dryer according to claim 6, it is characterized in that, described drier comprises hothouse, clasfficiator, base, wherein hothouse consists of connector multistage hollow cylindrical container, on hothouse top, clasfficiator is housed, base position connects the air inlet offering tangential direction, is upwards fluidisation section between clasfficiator from drier bottom; Material feeds from valve-type feeder, the circulating line carried bottom material drying device by air-flow tangentially enters fluidisation section, form the rotation spray moving air flow of high velocity, low pressure, material carries out heat and mass transfer process at fluidisation Duan Zhongyu air-flow, moisture removes gradually, be able to drying, material is subject to spiralling airflow entrainment and moves to clasfficiator, and the dry material particle reaching drying requirement enters in whirlwind collector with air-flow by clasfficiator centre bore because moisture content is low accumulating to drier axis position; The material particles not reaching drying requirement will be in empty periphery, clasfficiator center be graded device stop appoint so stay in drier continue dry, until reach the material water ratio requirement that drying specifies, dry material particles up to standard enters whirlwind collector with air-flow by clasfficiator centre bore, move downward along spiral inner wall formula, material particles is subject to get rid of to wall under the effect of centrifugal force in whirlwind collector, and fall under gravity into Star-like unloader, and clear foreign material are separated under the effect of whirlwind collector.
9. rape cyclone type flash dryer according to claim 6, it is characterized in that, described drier is also provided with base, it is set to spiral of Archimedes structure and air inlet duct width reduces gradually, reach minimum at drier air inlet duct width, air-flow flow to drier air inlet wind speed and reaches maximum.
10. rape cyclone type flash dryer according to claim 6, it is characterized in that, described Star-like unloader comprises the impeller of rotor of several pieces blades, housing, seal and motor, described Star-like unloader upper end is provided with flange port, the impeller of rotor axis direction that flange port lower end is provided with is concentric with electrical axis, discharger outer wall is housing, top accepts the material that whirlwind collector is discharged, the impeller of rotor rotated is relied on to play at the uniform velocity discharge and sealing function, when the material flowed out from whirlwind collector to fall in the space be filled between impeller of rotor by deadweight, rotation with impeller of rotor draws off.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520800433.5U CN205119460U (en) | 2015-10-13 | 2015-10-13 | Spiral plate type hot -blast furnace and use rape whirlwind formula flash distillation drying -machine of this hot -blast furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520800433.5U CN205119460U (en) | 2015-10-13 | 2015-10-13 | Spiral plate type hot -blast furnace and use rape whirlwind formula flash distillation drying -machine of this hot -blast furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205119460U true CN205119460U (en) | 2016-03-30 |
Family
ID=55575068
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520800433.5U Withdrawn - After Issue CN205119460U (en) | 2015-10-13 | 2015-10-13 | Spiral plate type hot -blast furnace and use rape whirlwind formula flash distillation drying -machine of this hot -blast furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205119460U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105222334A (en) * | 2015-10-13 | 2016-01-06 | 湖南农业大学 | Screw plate type hot-air furnace and use the rape cyclone type flash dryer of this hot-blast stove |
| CN107965986A (en) * | 2017-11-23 | 2018-04-27 | 南宁众创空间科技有限公司 | A kind of energy-saving heat cycle formula Chinese medicinal material drying equipment for drying |
| CN109373621A (en) * | 2018-11-23 | 2019-02-22 | 烟台通天达风机制造有限公司 | Induced oscillation heat high-temperature warm air machine |
| CN114025863A (en) * | 2019-06-25 | 2022-02-08 | 应用材料公司 | High efficiency trap for particle collection in vacuum foreline |
-
2015
- 2015-10-13 CN CN201520800433.5U patent/CN205119460U/en not_active Withdrawn - After Issue
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105222334A (en) * | 2015-10-13 | 2016-01-06 | 湖南农业大学 | Screw plate type hot-air furnace and use the rape cyclone type flash dryer of this hot-blast stove |
| CN105222334B (en) * | 2015-10-13 | 2017-12-22 | 湖南农业大学 | Screw plate type hot-air furnace and the rape cyclone type flash dryer using the hot-blast stove |
| CN107965986A (en) * | 2017-11-23 | 2018-04-27 | 南宁众创空间科技有限公司 | A kind of energy-saving heat cycle formula Chinese medicinal material drying equipment for drying |
| CN107965986B (en) * | 2017-11-23 | 2019-10-01 | 广州一品红制药有限公司 | A kind of energy-saving heat cycle formula Chinese medicinal material drying equipment for drying |
| CN109373621A (en) * | 2018-11-23 | 2019-02-22 | 烟台通天达风机制造有限公司 | Induced oscillation heat high-temperature warm air machine |
| CN114025863A (en) * | 2019-06-25 | 2022-02-08 | 应用材料公司 | High efficiency trap for particle collection in vacuum foreline |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205119460U (en) | Spiral plate type hot -blast furnace and use rape whirlwind formula flash distillation drying -machine of this hot -blast furnace | |
| CN201331247Y (en) | Helix tube airflow drier | |
| CN203586721U (en) | Biomass wood chip drying system | |
| CN106382790A (en) | Brown coal drying method and device utilizing waste heat of smoke and steam of power plant | |
| CN104457189B (en) | Thermal source built-in double-side heat exchange tunnel type drying room | |
| CN206207959U (en) | A kind of energy saving biomass particle drying plant | |
| CN104930831A (en) | Numerical control energy-saving flame isolation dryer | |
| CN105758148A (en) | Rapid briquette coal drying system and briquette coal drying furnace | |
| CN103604285A (en) | Biomass wood bit drying system and biomass wood bit drying method | |
| CN106440732A (en) | Food drying device | |
| CN205119739U (en) | Rape whirlwind formula flash distillation drying -machine | |
| CN203719350U (en) | Continuous pelleting drying device | |
| CN105222334B (en) | Screw plate type hot-air furnace and the rape cyclone type flash dryer using the hot-blast stove | |
| CN105222557B (en) | Rape cyclone type flash dryer | |
| CN102175073B (en) | Iron ore concentrate drying device and method for pelletizing | |
| CN205191627U (en) | Chimney waste heat recovery unit | |
| CN204466779U (en) | Harvester waste heat recovery drying unit | |
| CN202009662U (en) | Vertical grain drying tower | |
| CN105509418A (en) | Movable grain dryer | |
| CN202692623U (en) | Boiler waste heat secondary drying device | |
| CN204202159U (en) | Novel biomass particle high-temperature hot-blast stove | |
| CN210512155U (en) | Rice husk type environment-friendly energy-saving suspension furnace | |
| CN203940712U (en) | Movable grain drying machine | |
| CN207716825U (en) | A kind of dry-heat air furnace apparatus | |
| CN206959328U (en) | A kind of biological particle hot air furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160330 Effective date of abandoning: 20171222 |