CN204555586U - Rotatingandflashstreamingdrier group - Google Patents
Rotatingandflashstreamingdrier group Download PDFInfo
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- CN204555586U CN204555586U CN201520225505.8U CN201520225505U CN204555586U CN 204555586 U CN204555586 U CN 204555586U CN 201520225505 U CN201520225505 U CN 201520225505U CN 204555586 U CN204555586 U CN 204555586U
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Abstract
The utility model belongs to Rotatingandflashstreamingdrier field, particularly relates to a kind of Rotatingandflashstreamingdrier group; There is provided a kind of simple to operate, occupy little space, production capacity is large, saves material and avoids material waste, the Rotatingandflashstreamingdrier group that can effectively prevent material from piling up in crushing chamber; Comprise air-supply arrangement and flash distillation main frame, the quantity of described air-supply arrangement is two groups and two groups of air-supply arrangements are symmetricly set on two air inlet of flash distillation main frame, described air-supply arrangement comprises pressure fan and heater, the outlet of described pressure fan is connected with the import of heater, and the outlet of heater is connected for providing hot-air to flash distillation main frame with the air inlet of flash distillation main frame; The discharge outlet of described flash distillation main frame is connected with diffusion cyclone separator, and the top of described diffusion cyclone separator is connected with air box impulse sack cleaner by cleaning shaft, and described air box impulse sack cleaner is connected with exhaust blower by pipeline.
Description
Technical field:
The utility model belongs to Rotatingandflashstreamingdrier field, particularly relates to a kind of Rotatingandflashstreamingdrier group.
Background technology:
Rotatingandflashstreamingdrier group is a kind of drying equipment dry technology and fluidization technology are comprehensively integrated, and which overcomes the shortcoming of the large and recirculating fluidized bed uneven drying of drying equipment energy consumption.Mainly be applicable to the convection drying of the material such as paste, filter cake, solve the deficiency that rake drying efficiency is low and output is little.The drying of the materials such as the high viscosity of the chemical industries such as light industry, oil, chemical fibre, food, mine and intermediate, high-consistency is widely used in along with Rotatingandflashstreamingdrier.
But also there is a lot of problems in existing Rotatingandflashstreamingdrier group: existing Rotatingandflashstreamingdrier group normally adopts single air-supply arrangement in the process of application, single air-supply arrangement in use, because the wind speed of air inlet is larger, material is easy to pile up in the side of air inlet symmetry, can affect the operating efficiency of flash distillation main frame after solid accumulation.Existing diffusion cyclone separator outlet section is cylindrical shape in addition, and columnar exit resistance is comparatively large, when air-flow is discharged from outlet, can form interior eddy current, be carried away by separated particle, cause secondary to waste from outlet.
Existing flash distillation main frame does not arrange cooling device in the air inlet of flash distillation main frame, because hot blast contacts with material from during the air inlet of flash distillation main frame, temperature is much larger than the temperature in crushing chamber, if residence time of material is long in operation, material deterioration will be caused due to high-temperature hot-air, even occur situation about melting.The crushing efficiency of the breaker of existing flash distillation main frame is low in addition, and the easy binding material of the inwall of crushing chamber, affect the efficiency of flash distillation main frame.
Summary of the invention:
The utility model overcomes the deficiency that prior art exists, solve prior art Problems existing, aim to provide a kind of simple to operate, occupy little space, production capacity is large, save material and avoid material waste, the Rotatingandflashstreamingdrier group that can effectively prevent material from piling up in crushing chamber.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: Rotatingandflashstreamingdrier group, comprise air-supply arrangement and flash distillation main frame, the quantity of described air-supply arrangement is two groups and two groups of air-supply arrangements are symmetricly set on two air inlet of flash distillation main frame, described air-supply arrangement comprises pressure fan and heater, the air outlet of described pressure fan is connected with the air inlet of heater, and the air outlet of heater is connected for providing hot-air to flash distillation main frame with the air inlet of flash distillation main frame;
The discharge outlet of described flash distillation main frame is connected with diffusion cyclone separator, and the top of described diffusion cyclone separator is connected with air box impulse sack cleaner by cleaning shaft, and described air box impulse sack cleaner is connected with exhaust blower by pipeline.
Further, described diffusion cyclone separator comprises separator body, the top of separator body is provided with blast pipe, the middle part of described blast pipe is provided with blast pipe, described blast pipe be back taper and the bottom of blast pipe lower than the height of described blast pipe, separator body bottom be the ash accumulating chamber of taper, the bottom of described ash accumulating chamber is provided with star-shaped ash unloading valve.
Further, described blast pipe is helically wound around the top of separator body and is connected with separator interior.
Further, described flash distillation main frame comprises cylindrical shell, and the bottom of described cylindrical shell is provided with stirring breaker, and the side of stirring breaker overhead cylinder is provided with double-shaft spiral feeding device, and the middle and upper part of described cylindrical shell is provided with grading plant; The top of cylindrical shell is provided with air outlet;
Described stirring breaker comprises the base for supporting being fixedly installed on ground and the crushing chamber housing be fixedly installed on above base for supporting, the internal chamber of described crushing chamber housing is connected with inner barrel chamber, crushing chamber housing upper is back taper, bottom is straight barrel type, the bottom of crushing chamber housing is symmetrically arranged with air inlet, the middle part of crushing chamber housing is provided with broken main shaft, the top of described broken main shaft is provided with broken moving knife, described broken moving knife is stratified and set on broken main shaft, the inwall of the crushing chamber housing that broken moving knife is corresponding is provided with broken quiet cutter, the interlaced setting of the quiet cutter of fragmentation of adjacent layer,
The bottom of described broken main shaft extends to the outside of crushing chamber housing, extend to outside broken spindle nose and be fixedly installed driven pulley, described driven pulley is connected with power set by belt, described power set comprise buncher and driving wheel, buncher is connected with driving wheel key, and buncher drives broken main axis by belt transmission.
Further, described air inlet is provided with water cooling plant, described water cooling plant comprises water inlet, circulation line, delivery port and water circulating pump, described circulation line annular spread is in air inlet, water inlet and delivery port are all arranged on air inlet and are connected with circulation line, and water circulating pump to be connected with delivery port by water inlet and to drive recirculated water shuttling movement in circulation line.
Further, described broken moving knife comprises moving knife main body, and one end of described moving knife main body is fixedly installed scraper plate, and the lateral surface of described scraper plate is inclined-plane, and the lateral surface of described scraper plate is identical with the angle of inclination of crushing chamber housing upper taper surface.
Further, described grading plant comprises interval and is fixedly installed on three perforates circle baffle plates on cylindrical shell, and on described three perforates circle baffle plate, the diameter in hole reduces from top to bottom successively, perforate circle baffle plate be provided with backing plate up and down.
The utility model compared with prior art has following beneficial effect: the utility model by offering two air inlets and being symmetrical arranged air-supply arrangement two air inlet on flash distillation main frame, two groups of air-supply arrangements all tangentially enter in crushing chamber, and such material would not occur solid accumulation in crushing chamber.Symmetrical air-supply simultaneously can increase the heat exchanger effectiveness of material, accelerates air-flow turbulence, and strengthening fluidization work, promotes operating efficiency.
Do in an inverted cone by the blast pipe of diffusion cyclone separator, such air-flow when discharging from blast pipe, and the situation forming secondary vortex flow reduces, remitted its fury.Be not easy the secondary droplets causing material, improve gas solid separation corresponding, saved material and avoided material waste.In addition, screw type blast pipe decreases the impact of inlet air flow on vortex gas flow, reduces the resistance at blast pipe place, promotes powder feeding efficiency, promotes the operating efficiency of Rotatingandflashstreamingdrier group on the whole.
By arranging water cooling plant in the air inlet of flash distillation main frame, the temperature of flash distillation main frame air inlet air-flow can be reduced, avoiding producing localized hyperthermia, causing the appearance of material deterioration situation.Improve the drying efficiency of material, reduce material waste, promote operating efficiency.In addition, in crushing chamber, arrange broken moving knife and the quiet cutter of fragmentation, moving knife and quiet cutter are crisscross arranged, and improve material and fall probability on crushing cutter, effectively improve effect and the efficiency of particle.
Accompanying drawing illustrates:
Below in conjunction with accompanying drawing, the utility model is described in more detail
Fig. 1 is the structural representation of Rotatingandflashstreamingdrier group.
Fig. 2 is the structural representation of diffusion cyclone separator.
Fig. 3 is the structural representation of flash distillation main frame.
Fig. 4 is D place partial enlarged drawing figure in Fig. 3.
Fig. 5 is the structural representation of broken moving knife.
Fig. 6 is the structural representation of perforate circle baffle plate.
In figure: 1 is air-supply arrangement, 11 pressure fan, 12 is heater, 2 is flash distillation main frame, 21 is cylindrical shell, 22 for stirring breaker, 221 is base for supporting, 222 is crushing chamber housing, 223 is air inlet, 224 is broken main shaft, 225 is broken moving knife, 226 is broken quiet cutter, 227 is driven pulley, 228 is buncher, 229 is driving wheel, 23 is double-shaft spiral feeding device, 24 is grading plant, 241 is perforate circle baffle plate, 242 is backing plate, 25 is air outlet, 26 is water cooling plant, 261 is water inlet, 262 is circulation line, 263 is delivery port, 27 is moving knife main body, 28 is scraper plate, 3 is diffusion cyclone separator, 31 is separator body, 32 is blast pipe, 33 is blast pipe, 34 is ash accumulating chamber, 35 is star-shaped ash unloading valve, 4 is air box impulse sack cleaner, 5 is exhaust blower.
Detailed description of the invention:
As shown in Figure 1, Rotatingandflashstreamingdrier group, comprise air-supply arrangement 1 and flash distillation main frame 2, the quantity of described air-supply arrangement 1 is two groups and two groups of air-supply arrangements 1 are symmetricly set on two air inlet 223 places of flash distillation main frame 2, described air-supply arrangement 1 comprises pressure fan 11 and heater 12, the outlet of described pressure fan 11 is connected with the import of heater 12, and the outlet of heater 12 is connected for providing hot-air to flash distillation main frame 2 with the air inlet 223 of flash distillation main frame 2;
The discharge outlet of described flash distillation main frame 2 is connected with diffusion cyclone separator 3, and the top of described diffusion cyclone separator 3 is connected with air box impulse sack cleaner 4 by cleaning shaft, and described air box impulse sack cleaner 4 is connected with exhaust blower 5 by pipeline.
The workflow of Rotatingandflashstreamingdrier group: material enters flash distillation main frame 2 crushing chamber through the preliminary fragmentation of double-shaft spiral feeding device 23, hot blast after heated is sent in crushing chamber by the air inlet 223 of flash distillation main frame 2 by air-supply arrangement 1, material is broken further in crushing chamber, centrifugal, under hot wind action, make material form fluidized state come to life, material sends into diffusion cyclone separator 3 under hot blast effect, the tiny material sent into after diffuser casing cyclone enters air box impulse sack cleaner 4 and is separated, air enters air through exhaust blower 5, material is discharged by air box impulse sack cleaner 4, finished product packing dispatches from the factory.
As shown in Figure 2, described diffusion cyclone separator 3 comprises separator body 31, the top of separator body 31 is provided with blast pipe 32, the middle part of described blast pipe 32 is provided with blast pipe 33, described blast pipe 33 be back taper and the bottom of blast pipe 33 lower than the height of described blast pipe 32, separator body 31 bottom be the ash accumulating chamber 34 of taper, the bottom of described ash accumulating chamber 34 is provided with star-shaped ash unloading valve 35.
Further, described blast pipe 32 is helically wound around the top of separator body 31 and is connected with separator interior.Screw type blast pipe 32 decreases the impact of inlet air flow on vortex gas flow, reduces the resistance at blast pipe 32 place, promotes powder feeding efficiency, promotes the operating efficiency of Rotatingandflashstreamingdrier group on the whole.
As shown in figures 3 to 6, described flash distillation main frame 2 comprises cylindrical shell 21, the bottom of described cylindrical shell 21 is provided with stirs breaker 22, and the side of stirring breaker 22 overhead cylinder 21 is provided with double-shaft spiral feeding device 23, and the middle and upper part of described cylindrical shell 21 is provided with grading plant 24; The top of cylindrical shell 21 is provided with air outlet 25;
Described stirring breaker 22 comprises the base for supporting 221 being fixedly installed on ground and the crushing chamber housing 222 be fixedly installed on above base for supporting 221, the internal chamber of described crushing chamber housing 222 is connected with cylindrical shell 21 internal chamber, crushing chamber housing 222 top is back taper, bottom is straight barrel type, the bottom of crushing chamber housing 222 is symmetrically arranged with air inlet 223, the middle part of crushing chamber housing 222 is provided with broken main shaft 224, the top of described broken main shaft 224 is provided with broken moving knife 225, described broken moving knife 225 is stratified and set on broken main shaft 224, the inwall of the crushing chamber housing 222 that broken moving knife 225 is corresponding is provided with broken quiet cutter 226, the interlaced setting of the quiet cutter of fragmentation 226 of adjacent layer,
The bottom of described broken main shaft 224 extends to the outside of crushing chamber housing 222, extend to outside broken main shaft 224 end winding support and be provided with driven pulley 227, described driven pulley 227 is connected with power set by belt, described power set comprise buncher 228 and driving wheel 229, buncher 228 is connected with driving wheel 229 key, and buncher 228 drives broken main shaft 224 to rotate by belt transmission.
The course of work of flash distillation main frame 2: material sends into crushing chamber through double-shaft spiral feeding device 23, granule in material floats with the hot blast of spiral status, bulky grain is then because gravity sinks, stir through broken moving knife 225 and the quiet cutter 226 of fragmentation in crushing chamber and smash, particle after refinement is through the drying of hot blast, material after refinement is brought into graded region by hot blast, grading plant 24 will not meet the requirements of material and again stop back that crushing chamber carries out refinement, meet the requirements of material and discharge from the air outlet 25 at flash distillation main frame 2 top.
Further, described air inlet 223 place is provided with water cooling plant 26, described water cooling plant 26 comprises water inlet 261, circulation line 262, delivery port 263 and water circulating pump, described circulation line 262 annular spread is at air inlet 223 place, water inlet 261 is all arranged on air inlet 223 place with delivery port 263 and is connected with circulation line 262, and water circulating pump to be connected with delivery port 263 by water inlet 261 and to drive recirculated water shuttling movement in circulation line 262.The temperature of flash distillation main frame 2 air inlet 223 place air-flow can be reduced, avoid producing localized hyperthermia, cause the appearance of material deterioration situation.Improve the drying efficiency of material, reduce material waste, promote operating efficiency.
Further, described broken moving knife 225 comprises moving knife main body 27, one end of described moving knife main body 27 is fixedly installed scraper plate 28, and the lateral surface of described scraper plate 28 is inclined-plane, and the lateral surface of described scraper plate 28 is identical with the angle of inclination in crushing chamber housing 222 upper taper face.Scraper plate 28 can prevent material from crushing chamber inwall, forming stammerer phenomenon, is peeled off before materials from bonding is firm, and preventing from stammering affects the normal work of breaker.
Further, described grading plant 24 comprises interval and is fixedly installed on three perforates circle baffle plates 241 on cylindrical shell 21, and on described three perforates circle baffle plate 241, the diameter in hole reduces from top to bottom successively, perforate circle baffle plate 241 be provided with backing plate 242 up and down.
Above content combines embodiment accompanying drawing and has made detailed description to specific embodiments of the invention.In this description, each embodiment adopts the mode of going forward one by one to describe, and what each embodiment stressed is the difference with other embodiments, between each embodiment identical similar portion mutually see.
By reference to the accompanying drawings embodiments of the invention are explained in detail above, but the present invention is not limited to above-described embodiment, in the ken that those of ordinary skill in the art possess, various change can also be made under the prerequisite not departing from present inventive concept.
Claims (7)
1. a Rotatingandflashstreamingdrier group, it is characterized in that: comprise air-supply arrangement (1) and flash distillation main frame (2), the quantity of described air-supply arrangement (1) is two groups and two groups of air-supply arrangements (1) are symmetricly set on two air inlet (223) places of flash distillation main frame (2), described air-supply arrangement (1) comprises pressure fan (11) and heater (12), the outlet of described pressure fan (11) is connected with the import of heater (12), the outlet of heater (12) is connected for providing hot-air to flash distillation main frame (2) with the air inlet (223) of flash distillation main frame (2),
The discharge outlet of described flash distillation main frame (2) is connected with diffusion cyclone separator (3), the top of described diffusion cyclone separator (3) is connected with air box impulse sack cleaner (4) by cleaning shaft, and described air box impulse sack cleaner (4) is connected with exhaust blower (5) by pipeline.
2. Rotatingandflashstreamingdrier group according to claim 1, it is characterized in that: described diffusion cyclone separator (3) comprises separator body (31), the top of separator body (31) is provided with blast pipe (32), the middle part of described blast pipe (32) is provided with blast pipe (33), described blast pipe (33) for back taper and the bottom of blast pipe (33) lower than the height of described blast pipe (32), separator body (31) bottom be the ash accumulating chamber (34) of taper, the bottom of described ash accumulating chamber (34) is provided with star-shaped ash unloading valve (35).
3. Rotatingandflashstreamingdrier group according to claim 2, is characterized in that: described blast pipe (32) is helically wound around the top of separator body (31) and is connected with separator interior.
4. Rotatingandflashstreamingdrier group according to claim 1, it is characterized in that: described flash distillation main frame (2) comprises cylindrical shell (21), the bottom of described cylindrical shell (21) is provided with stirs breaker (22), the side of stirring breaker (22) overhead cylinder (21) is provided with double-shaft spiral feeding device (23), and the middle and upper part of described cylindrical shell (21) is provided with grading plant (24); The top of cylindrical shell (21) is provided with air outlet (25);
Described stirring breaker (22) comprises the base for supporting (221) being fixedly installed on ground and the crushing chamber housing (222) being fixedly installed on base for supporting (221) top, the internal chamber of described crushing chamber housing (222) is connected with cylindrical shell (21) internal chamber, crushing chamber housing (222) top is back taper, bottom is straight barrel type, the bottom of crushing chamber housing (222) is symmetrically arranged with air inlet (223), the middle part of crushing chamber housing (222) is provided with broken main shaft (224), the top of described broken main shaft (224) is provided with broken moving knife (225), described broken moving knife (225) is stratified and set on broken main shaft (224), the inwall of the crushing chamber housing (222) that broken moving knife (225) is corresponding is provided with broken quiet cutter (226), the quiet cutter of fragmentation (226) the interlaced setting of adjacent layer,
The bottom of described broken main shaft (224) extends to the outside of crushing chamber housing (222), extend to outside broken main shaft (224) end winding support and be provided with driven pulley (227), described driven pulley (227) is connected with power set by belt, described power set comprise buncher (228) and driving wheel (229), buncher (228) is connected with driving wheel (229) key, and buncher (228) drives broken main shaft (224) to rotate by belt transmission.
5. Rotatingandflashstreamingdrier group according to claim 4, it is characterized in that: described air inlet (223) place is provided with water cooling plant (26), described water cooling plant (26) comprises water inlet (261), circulation line (262), delivery port (263) and water circulating pump, described circulation line (262) annular spread is at air inlet (223) place, water inlet (261) is all arranged on air inlet (223) place with delivery port (263) and is connected with circulation line (262), water circulating pump is connected with delivery port (263) by water inlet (261) and drives recirculated water shuttling movement in circulation line (262).
6. Rotatingandflashstreamingdrier group according to claim 5, it is characterized in that: described broken moving knife (225) comprises moving knife main body (27), one end of described moving knife main body (27) is fixedly installed scraper plate (28), the lateral surface of described scraper plate (28) is inclined-plane, and the lateral surface of described scraper plate (28) is identical with the angle of inclination in crushing chamber housing (222) upper taper face.
7. Rotatingandflashstreamingdrier group according to claim 6, it is characterized in that: described grading plant (24) comprises interval and is fixedly installed on three perforates circle baffle plate (241) on cylindrical shell (21), the diameter in the upper hole of described three perforates circle baffle plate (241) reduces from top to bottom successively, perforate circle baffle plate (241) be provided with backing plate (242) up and down.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520225505.8U CN204555586U (en) | 2015-04-10 | 2015-04-10 | Rotatingandflashstreamingdrier group |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520225505.8U CN204555586U (en) | 2015-04-10 | 2015-04-10 | Rotatingandflashstreamingdrier group |
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| Publication Number | Publication Date |
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| CN204555586U true CN204555586U (en) | 2015-08-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520225505.8U Expired - Fee Related CN204555586U (en) | 2015-04-10 | 2015-04-10 | Rotatingandflashstreamingdrier group |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105043055A (en) * | 2015-08-25 | 2015-11-11 | 付锦帆 | Mixed steam drying device and method |
| CN105222561A (en) * | 2015-09-17 | 2016-01-06 | 苏州新协力特种工业模板有限公司 | A kind of Rotatingandflashstreamingdrier |
| CN106766819A (en) * | 2017-02-04 | 2017-05-31 | 河南佳尚农业科技发展有限公司 | A kind of rosemary fat-soluble extract expansion drying system |
| CN110407429A (en) * | 2019-08-27 | 2019-11-05 | 第一环保（深圳）股份有限公司 | A kind of quick anhydration system of low energy consumption wet stock and method |
| CN111121398A (en) * | 2020-02-14 | 2020-05-08 | 九江富达实业有限公司 | Full-process-automation solid-liquid separation and drying system for dye intermediate |
| CN111250241A (en) * | 2020-02-17 | 2020-06-09 | 河北维果生物科技有限公司 | Feed milk powder drying device |
| CN114234557A (en) * | 2021-11-24 | 2022-03-25 | 深圳亦永生物科技有限公司 | Drying-free collision dehydration equipment for porous or spongy powdery materials |
| CN115127322A (en) * | 2022-08-31 | 2022-09-30 | 山东德利科工业装备有限公司 | Circulation heat accumulation formula spin flash dryer convenient to clearance |
-
2015
- 2015-04-10 CN CN201520225505.8U patent/CN204555586U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105043055A (en) * | 2015-08-25 | 2015-11-11 | 付锦帆 | Mixed steam drying device and method |
| CN105222561A (en) * | 2015-09-17 | 2016-01-06 | 苏州新协力特种工业模板有限公司 | A kind of Rotatingandflashstreamingdrier |
| CN106766819A (en) * | 2017-02-04 | 2017-05-31 | 河南佳尚农业科技发展有限公司 | A kind of rosemary fat-soluble extract expansion drying system |
| CN110407429A (en) * | 2019-08-27 | 2019-11-05 | 第一环保（深圳）股份有限公司 | A kind of quick anhydration system of low energy consumption wet stock and method |
| CN110407429B (en) * | 2019-08-27 | 2023-11-24 | 第一环保（深圳）股份有限公司 | Low-energy-consumption wet material rapid drying system and method |
| CN111121398A (en) * | 2020-02-14 | 2020-05-08 | 九江富达实业有限公司 | Full-process-automation solid-liquid separation and drying system for dye intermediate |
| CN111250241A (en) * | 2020-02-17 | 2020-06-09 | 河北维果生物科技有限公司 | Feed milk powder drying device |
| CN114234557A (en) * | 2021-11-24 | 2022-03-25 | 深圳亦永生物科技有限公司 | Drying-free collision dehydration equipment for porous or spongy powdery materials |
| CN115127322A (en) * | 2022-08-31 | 2022-09-30 | 山东德利科工业装备有限公司 | Circulation heat accumulation formula spin flash dryer convenient to clearance |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20160410 |
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| CF01 | Termination of patent right due to non-payment of annual fee |