CN204128325U - Vibratingfluidbeddrier - Google Patents
Vibratingfluidbeddrier Download PDFInfo
- Publication number
- CN204128325U CN204128325U CN201420536846.2U CN201420536846U CN204128325U CN 204128325 U CN204128325 U CN 204128325U CN 201420536846 U CN201420536846 U CN 201420536846U CN 204128325 U CN204128325 U CN 204128325U
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- China
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- bed body
- fluidized bed
- vibratingfluidbeddrier
- drying
- drying machine
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Abstract
The utility model relates to drying equipment technical field, especially a kind of Vibratingfluidbeddrier.Existing Vibratingfluidbeddrier drying effect is not good, and equipment is easy to impaired, causes maintenance cost to increase.This Vibratingfluidbeddrier comprises drying machine main body, three laminarization bed bodies are provided with in drying machine main body, every laminarization bed body is end to end, keep same inclination angle, tilted by the feed end of fluidized bed body to discharge end, fluidized bed body one is straight mesh plate, fluidized bed body two is vertical web orifice plate, fluidized bed body three is inclined hole mesh plate, and upper box and lower box employing soft strength are closed and be connected, and air outlet place is provided with air-introduced machine.Drying machine after improvement is under the prerequisite of same consumption energy, improve drying efficiency, improve production capacity, shorten the production cycle, effectively save energy consumption, effectively alleviate carrying live load, reduce power match power, reduce equipment material and manufacture consumption, the equipment use economy reducing Failure Rate of Weapon Equipment, reach energy-conservation, lower consumption.
Description
Technical field
The utility model relates to drying equipment technical field, especially a kind of Vibratingfluidbeddrier.
Background technology
Vibratingfluidbeddrier is applicable to pharmacy, chemical industry, food service industry are produced the drying of graininess, sheet, ghost water material, and adopting the drying mechanism of vibratory liquefaction, is the comparatively typical dry production equipment of current drying technical field.Existing Vibratingfluidbeddrier has the structure such as individual layer and multilayer, individual layer Vibratingfluidbeddrier material can only carry out a heat exchange, drying efficiency is low, though multi-layer oscillation fluidized bed dryer hot blast and dried material can carry out repeatedly heat exchange, but drying area and the dry materials time of staying all uncontrollable, drying efficiency does not still significantly improve, add on existing Vibratingfluidbeddrier and be bolted to connection merely between lower box, during work, upper box participates in vibration, live load increases, and often occurs the phenomenon of device damage.
Utility model content
In order to overcome existing above-mentioned deficiency, the utility model provides a kind of Vibratingfluidbeddrier.
The utility model solves the technical scheme that its technical problem adopts: a kind of Vibratingfluidbeddrier, comprise drying machine main body, drying machine main body is divided into upper box and lower box, upper box is provided with air outlet, air inlet is provided with bottom lower box, vibrating motor is provided with bottom lower box, drying machine main body one end is provided with feeding mouth, the other end is provided with discharging opening, three laminarization bed bodies are provided with in drying machine main body, described three laminarization bed bodies are inclination Z-shaped, every laminarization bed body is end to end, keep same inclination angle, tilted to discharge end by the feed end of fluidized bed body, fluidized bed body one is straight mesh plate, fluidized bed body two is vertical web orifice plate, fluidized bed body three is inclined hole mesh plate, the hole shape of inclined hole mesh plate and bed surface are 45° angle.
According to another embodiment of the present utility model, comprise described upper box further and be connected with lower box employing soft strength is closed, junction is provided with elastic sealing gasket, is provided with stage clip between sealing gasket.
According to another embodiment of the present utility model, comprise described air outlet place further and be provided with air-introduced machine.
The beneficial effects of the utility model are,
(1) multilayer fluidized drying is under the prerequisite of same consumption energy, improves drying efficiency, improves production capacity, shortens the production cycle, effectively saves energy consumption;
(2) soft strength technology effective alleviates carrying live load, reduction power match power, reduces equipment material and manufactures consumption, the equipment use economy reducing Failure Rate of Weapon Equipment, reach energy-conservation, lower consumption.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is external structure schematic diagram of the present utility model.
Fig. 2 is internal structure schematic diagram of the present utility model.
1. drying machine main body, 2. upper box, 3. lower boxes in figure, 4. air outlet, 5. air inlet, 6. vibrating motor, 7. feeding mouth, 8. discharging opening, 9. fluidized bed body, 9-1. fluidized bed body one, 9-2. fluidized bed body two, 9-3. fluidized bed body three, 10. feed end, 11. discharge ends, 12. elastic sealing gaskets, 13. stage clips, 14. air-introduced machines.
Detailed description of the invention
As Fig. 1, shown in 2, a kind of Vibratingfluidbeddrier, comprise drying machine main body 1, drying machine main body 1 is divided into upper box 2 and lower box 3, upper box 2 is provided with air outlet 4, air inlet 5 is provided with bottom lower box 3, vibrating motor 6 is provided with bottom lower box 3, drying machine main body 1 one end is provided with feeding mouth 7, the other end is provided with discharging opening 8, three laminarization bed bodies 9 are provided with in drying machine main body 1, described three laminarization bed bodies 9 are in inclination Z-shaped, every laminarization bed body 9 is end to end, keep same inclination angle, tilted to discharge end 11 by the feed end 10 of fluidized bed body 9, fluidized bed body one 9-1 is straight mesh plate, fluidized bed body two 9-2 is vertical web orifice plate, fluidized bed body three 9-3 is inclined hole mesh plate, the hole shape of inclined hole mesh plate and bed surface are 45° angle, described upper box 2 and lower box 3 adopt soft strength close be connected, junction is provided with elastic sealing gasket 12, stage clip 13 is provided with between elastic sealing gasket 12, described air outlet 4 place is provided with air-introduced machine 14.
Fluidized bed body one 9-1 to be tilted certain angle to discharge end 11 by feed end 10, the feed end 10 of fluidized bed body two 9-2 is arranged on the below of fluidized bed body one 9-1 discharge end 11, namely the discharge end 11 of fluidized bed body two 9-2 is the feed end 10 of fluidized bed body three 9-3, same maintenance inclination angle, so that material is in dry run, push ahead produce the promotion of vibration frequency at vibrating motor 6 under, until discharging completes dry production overall process, this Vibratingfluidbeddrier is under equivalent energy consumption condition, improve dry tenacity, i.e. dry heat medium, heat exchange is carried out by the percolation of the mesh of fluid bed and the wet stock of bed surface, simultaneously, hot gas is along with the effect of upper box 2 air-introduced machine 14, hot gas is again by fluidized bed body two 9-2 mesh, the wet stock of percolation and bed surface carries out heat exchange, until after fluidized bed body three 9-3 heat exchange, discharge outside machine by air-introduced machine 14, so that make full use of hot-air heat-transfer effect, make product water content can reach the quality technology requirement of 0.5%, compared with traditional vibratory liquefaction bed technique, the thermal efficiency can improve 40%, production cycle can shorten 30%, energy resource consumption can save more than 40%.
Along with the change of mesh plate, material can play the different fluidised change such as skip-forwards, deceleration in dry run, so that play and regulate the inherent effect such as flow direction of material, the advance speed of service or drying residencing time, when material initial water content is higher, answer proper extension material in the time of staying of dry run, and along with the continuity of drying time, material moisture also reduces thereupon, and this, answer corresponding quickening material at the flow velocity of dry run, and when material moisture is close to butt, its drying residencing time more should reduce.Based on above-mentioned, when fluidized bed body one 9-1 material initial water content is higher, the time of staying of material in dry run can be extended accordingly, so fluidized bed body one 9-1 is straight mesh plate, and arrive fluidized bed body two 9-2 time, along with the continuity of being heated heat exchange and drying time of wet stock, its water content also reduces thereupon, so the mesh of fluidized bed body two 9-2 is designed to upright opening, compared with fluidized bed body one 9-1 technology, can corresponding increase material at the flow velocity of dry run, accelerate material and push ahead speed in dry run, and when material enters fluidized bed body three 9-3, its water content will close to end product quality requirement, around here, honest fresh supplemented hot-air enters by bottom lower box 3, hold heat higher, more should accelerate the flow velocity of dried material in fluidized bed body three 9-3 dry run for this reason, reduce drying residencing time, for this reason, fluidized bed body three 9-3 mesh is designed to oblique, hole shape and bed surface are 45 °, by the thrust of hot-air, complete the overall process of dry materials.Upper box 2 and lower box 3 adopt soft strength close be connected, in the junction of upper box 2 with fluid bed lower box 3, an elastic sealing gasket 12 is formed with fabric, stage clip 13 is provided with between sealing gasket 12, by the elasticity of stage clip 13, many technological deficiencies that alleviation conventional vibration fluid bed upper box 2 jointly participates in vibrating with lower box 3 and causes, reduce vibrating motor 6 match power, save electric power power consumption, reduce the operating cost causing parts to keep in repair because of conventional vibration bed accordingly simultaneously.
Vibratingfluidbeddrier after improvement is under the prerequisite of same consumption energy, not only improve drying efficiency, improve production capacity, shorten the production cycle, effectively save energy consumption, can also effectively alleviate carrying live load, reduce power match power, reduce equipment material and manufacture consumption, the equipment use economy reducing Failure Rate of Weapon Equipment, reach energy-conservation, lower consumption.
Claims (3)
1. a Vibratingfluidbeddrier, comprise drying machine main body (1), drying machine main body (1) is divided into upper box (2) and lower box (3), upper box (2) is provided with air outlet (4), lower box (3) bottom is provided with air inlet (5), lower box (3) bottom is provided with vibrating motor (6), drying machine main body (1) one end is provided with feeding mouth (7), the other end is provided with discharging opening (8), three laminarization bed bodies (9) are provided with in drying machine main body (1), it is characterized in that, described three laminarization bed bodies (9) are in inclination Z-shaped, every laminarization bed body (9) is end to end, keep same inclination angle, tilted to discharge end (11) by the feed end (10) of fluidized bed body (9), fluidized bed body one (9-1) is straight mesh plate, fluidized bed body two (9-2) is vertical web orifice plate, fluidized bed body three (9-3) is inclined hole mesh plate, the hole shape of inclined hole mesh plate and bed surface are 45° angle.
2. Vibratingfluidbeddrier according to claim 1, is characterized in that, described upper box (2) and lower box (3) employing soft strength are closed and be connected, and junction is provided with elastic sealing gasket (12), is provided with stage clip (13) between elastic sealing gasket (12).
3. Vibratingfluidbeddrier according to claim 1, is characterized in that, described air outlet (4) place is provided with air-introduced machine (14).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420536846.2U CN204128325U (en) | 2014-09-18 | 2014-09-18 | Vibratingfluidbeddrier |
Applications Claiming Priority (1)
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CN201420536846.2U CN204128325U (en) | 2014-09-18 | 2014-09-18 | Vibratingfluidbeddrier |
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CN204128325U true CN204128325U (en) | 2015-01-28 |
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CN201420536846.2U Expired - Fee Related CN204128325U (en) | 2014-09-18 | 2014-09-18 | Vibratingfluidbeddrier |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104941960A (en) * | 2015-06-06 | 2015-09-30 | 安徽瀚洋节能科技有限公司 | Granular-substance cooling and cleaning fluidized bed |
CN106091584A (en) * | 2016-08-15 | 2016-11-09 | 常州力马干燥科技有限公司 | A kind of Vibratingfluidbeddrier |
WO2022139714A1 (en) * | 2020-12-25 | 2022-06-30 | İmaş Maki̇na Sanayi̇ Anoni̇m Şi̇rketi̇ | Preparation unit before dryer for flake feed products |
-
2014
- 2014-09-18 CN CN201420536846.2U patent/CN204128325U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104941960A (en) * | 2015-06-06 | 2015-09-30 | 安徽瀚洋节能科技有限公司 | Granular-substance cooling and cleaning fluidized bed |
CN106091584A (en) * | 2016-08-15 | 2016-11-09 | 常州力马干燥科技有限公司 | A kind of Vibratingfluidbeddrier |
WO2022139714A1 (en) * | 2020-12-25 | 2022-06-30 | İmaş Maki̇na Sanayi̇ Anoni̇m Şi̇rketi̇ | Preparation unit before dryer for flake feed products |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150128 Termination date: 20190918 |
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CF01 | Termination of patent right due to non-payment of annual fee |