CN202648311U - Heat pump impulse dryer - Google Patents
Heat pump impulse dryer Download PDFInfo
- Publication number
- CN202648311U CN202648311U CN 201220185450 CN201220185450U CN202648311U CN 202648311 U CN202648311 U CN 202648311U CN 201220185450 CN201220185450 CN 201220185450 CN 201220185450 U CN201220185450 U CN 201220185450U CN 202648311 U CN202648311 U CN 202648311U
- Authority
- CN
- China
- Prior art keywords
- drying chamber
- heat pump
- dryer
- drying
- pulsation
- 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
- 238000001035 drying Methods 0.000 claims abstract description 66
- 238000009413 insulation Methods 0.000 claims description 14
- 238000007599 discharging Methods 0.000 claims description 11
- 238000007664 blowing Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract description 17
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000005457 optimization Methods 0.000 abstract description 2
- 238000004321 preservation Methods 0.000 abstract 4
- 238000007791 dehumidification Methods 0.000 abstract 1
- 238000010981 drying operation Methods 0.000 abstract 1
- 230000000630 rising Effects 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 229920002456 HOTAIR Polymers 0.000 description 4
- 238000005243 fluidization Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 2
- 230000003628 erosive Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000007605 air drying Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000011345 viscous material Substances 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
Abstract
The utility model relates to the technical field of drying devices, in particular to a heat pump impulse dryer. The dryer is provided with a drying chamber, and a loading mesh plate is arranged at the bottom of the drying chamber. A rotatable gas distribution device is arranged under the loading mesh plate and communicated with a heat preservation channel. The other end of the heat preservation channel is connected with a wind outlet of the drying chamber. One end of the heat preservation channel close to the wind outlet of the drying chamber is connected with a heat pump evaporator and a heat pump condenser in sequence along the wind direction in embedded mode. A fan is arranged in the heat preservation channel, and a material feed inlet and a material discharge outlet are arranged in the drying chamber. Through optimization of structural design, the heat pump impulse dryer utilizes the high temperature heat pump technology to generate hot wind, is quick in temperature rising, high in efficiency, and capable of effectively reducing consumption of electrical power energy, reduces use cost, and greatly meets requirements of drying operation. Combination of heat pump dehumidification and fluidized drying is adopted, so materials are evenly dried, moreover, a solar panel can heat through absorbing solar energy, so drying time is reduced, and energy resources are saved.
Description
Technical field
The utility model relates to the drying unit technical field, especially relates to a kind of heat pump dryer.
Background technology
At present, the domestic agricultural product dried forms that generally adopts is hot air convective drying, comprises fixed bed and common fluid bed etc.Wherein fixed bed drying speed is slower, and common fluid bed guarantees rate of drying in order to make material reach fluidized state, and thermal current pressure is generally all larger, and flow velocity is higher, so energy consumption is larger, and very easily produce cavitation erosion, the phenomenons such as channel, local caking.The heated-air drying that adopts at present mostly is open, and after the drying, the hot blast of temperature up to 50 ℃ directly is discharged into workshop.Not only greatly wasted the energy, and contaminated environment, cause workman's working condition extremely abominable.In a word, the problem such as existing hot air convective drying mode exists the energy consumption height, and link hand-manipulated is many, and production efficiency is low, its market competitiveness is worse and worse.So-called gas fluidized drying refers to that material in the drying box is in dry run, by a kind of air-flow institute fluidisation of press the some cycles variation.When material carries out drying in this state, be conducive to suppress the phenomenons such as the often cavitation erosion of appearance, channel, local caking in the common fluid bed, improve the motion state of material particles in air-flow, be conducive to viscous material and the drying that is not easy the fluidisation material.It is compared with traditional fluid bed, has the advantages such as the particle size range that adapts to material is wider, heat and mass speed high, energy-saving effect is obvious.Utilize the pulsate fluidizing principle that material is carried out drying, can also reduce thermograde and the gradation of moisture of granule interior.Result of study shows, because the endocorpuscular pulsation of fluid bed, nusselt number is large when not pulsing, and pulsation phenomenon is more obvious, and the particle heat transfer coefficient is just larger.Therefore, the strong pulsation of fluid bed endoparticle is favourable to conducting heat in the bed.If aggravate artificially the fluctuation intensity of this particle, it is a kind of effective method of further strengthening the fluid-bed heat transfer mass transport process.The applicant has developed the technical program for this reason.
Summary of the invention
The purpose of this utility model is to provide a kind of structure optimization, and operating cost is low, utilizes heat pump techniques to generate hot blast, good energy-conserving effect, and can realize the heat pump pulsation dryer that the material pulsation is dried.
For achieving the above object, the utility model adopts following technical scheme:
Heat pump pulsation dryer, this dryer has drying chamber, the drying chamber inner bottom part is provided with the carrying web plate, the below of carrying web plate is provided with rotating gas distributor, gas distributor is communicated with a thermal insulation air channel, and the other end of thermal insulation air channel connects the air outlet of drying chamber, down the wind embeds successively to connect evaporator with heat pump and heat pump condenser on a close end of drying chamber air outlet of thermal insulation air channel, be provided with blower fan in the thermal insulation air channel, described drying chamber is provided with dog-house and discharging opening.
Such scheme further is: a side of described drying chamber also be provided with can absorb solar energy and to the oven dry heating indoor solar panels.
Such scheme further is: described gas distributor is installed in the rotating shaft, and rotating shaft connects motor by gear drive.
Such scheme further is: also be provided with moisture exhausting port for subsequent use on the described drying chamber.
Such scheme further is: described rotary shaft hollow, and inner port is communicated with drying chamber, and outside the external port pass-out drying chamber, forms the discharging opening of drying chamber; Be provided with the blowing rod of the discharging opening that can close and open drying chamber in the inner port of rotating shaft.
Such scheme further is: motor is buncher.
The utility model passes through optimizing structure design, utilize the high temperature heat pump technology to generate hot blast, temperature rise is fast, efficient is high, effectively reduce the consumption of electric power energy, reduce use cost, greatly satisfy the drying work demand, adopt heat pump dehumidifying and fluidized drying combination, have the advantages such as the particle size range that adapts to material is wider, heat and mass speed high, energy-saving effect is obvious in fluidized drying, so that dry material is more even, solar panels absorb solar energy heating in addition, also shorten to the full extent the dry time, thereby saved the energy.
A utility model again advantage is simple in structure, and is scientific and reasonable, easily makes, and cost of investment is low, and the operation operation is easy, and Maintenance and Repair are very convenient, greatly improved operation ratio and the operability of equipment.
Description of drawings:
Accompanying drawing 1 is structural representation of the present utility model.
The specific embodiment:
Below in conjunction with accompanying drawing the utility model is further specified:
Consult shown in Figure 1, the heat pump pulsation dryer that the utility model provides, this dryer has drying chamber 1, drying chamber 1 inner bottom part is provided with carrying web plate 2, the below of carrying web plate 2 is provided with rotating gas distributor 3, gas distributor 3 connects a thermal insulation air channel 4, the other end of thermal insulation air channel 4 connects the air outlet of drying chamber 1, on a close end of drying chamber air outlet of thermal insulation air channel 4, down the wind embed successively and connect evaporator with heat pump 5 and heat pump condenser 6, be provided with blower fan 41 in the thermal insulation air channel 4, described drying chamber 1 is provided with dog-house 11 and discharging opening 12.
Shown in Figure 1, in the present embodiment, also be provided with in a side of drying chamber 1 and can absorb solar energy and to the solar panels 7 of oven dry heating indoor.Described gas distributor 3 is installed in the rotating shaft 8 together, and rotating shaft 8 connects motor 9 by gear drive, and motor 9 drive shafts 8 are rotated thus, then can drive gas distributor 3 rotations.Motor 9 is buncher, realizes adjustment of rotational speed, to satisfy actual needs.Rotating shaft 8 hollows, inner port is communicated with drying chamber 1, and outside the external port pass-out drying chamber 1, forms the discharging opening 12 of drying chamber 1; Be provided with the blowing rod 81 of the discharging opening 12 that can close and open drying chamber in the inner port of rotating shaft 21, control thus the discharging opening 12 that blowing rod 81 can realize closing and opening drying chamber.
In the present embodiment, also be provided with moisture exhausting port 13 for subsequent use on the described drying chamber 1, with the suitable wet steam of getting rid of, guarantee that the gas in the drying chamber 1 can be too unsaturated, so that affect the effect of fluidized drying, reach energy savings.
During work, material is put into drying chamber 1 from dog-house 11, drop on the carrying web plate 2, motor 9 work, by drive shaft 8 rotations, thereby drive gas distributor 3 rotations, blower fan 41 work in the thermal insulation air channel 4, to be transported to gas distributor 3 times through the high-temperature hot-air of evaporator with heat pump 5 and heat pump condenser 6 formation, hot blast is blown in the drying chamber 1 from the air outlet on the gas distributor 3, and the in addition rotation of gas distributor 3 is so that the material on the carrying web plate 2 is constantly blown afloat from the bottom, become the fluidisation shape, promote drying effect.Hot blast after the work enters thermal insulation air channel 4 again from air outlet, through evaporator with heat pump 5 and heat pump condenser 6 heating, forms high-temperature hot-air successively again, enters drying chamber 1, forms circulation.
The solar panels 7 of drying chamber 1 one sides absorb solar energy drying chamber 1 are further heated, and have further shortened the time of dry materials fluidisation, raising efficiency.After fluidized drying is finished, to control blowing rod 81 and material can be emitted from discharging opening 12, the work of a fluidized drying is finished.
Certainly, more than diagram is preferred embodiment of the present utility model only, is not to limit practical range of the present utility model with this, so every principle according to the utility model is done the equivalence variation or modified, and all should be covered by in the protection domain of the present utility model.
Claims (7)
1. heat pump pulsation dryer, it is characterized in that: this dryer has drying chamber (1), drying chamber (1) inner bottom part is provided with carrying web plate (2), the below of carrying web plate (2) is provided with rotating gas distributor (3), gas distributor (3) is communicated with a thermal insulation air channel (4), the other end of thermal insulation air channel (4) connects the air outlet of drying chamber (1), on a close end of drying chamber air outlet of thermal insulation air channel (4), down the wind embed successively and connect evaporator with heat pump (5) and heat pump condenser (6), be provided with blower fan (41) in the thermal insulation air channel (4), described drying chamber (1) is provided with dog-house (11) and discharging opening (12).
2. heat pump according to claim 1 pulsation dryer is characterized in that: a side of described drying chamber (1) also is provided with and can absorbs solar energy and to the solar panels (7) of oven dry heating indoor.
3. heat pump according to claim 1 pulsation dryer, it is characterized in that: described gas distributor (3) is installed in the rotating shaft (8), and rotating shaft (8) connects motor (9) by gear drive.
4. heat pump pulsation dryer according to claim 1 is characterized in that: also be provided with moisture exhausting port for subsequent use (13) on the described drying chamber (1).
5. heat pump according to claim 3 pulsation dryer, it is characterized in that: rotating shaft (8) hollow, inner port is communicated with drying chamber (1), and outside the external port pass-out drying chamber (1), forms the discharging opening (12) of drying chamber (1).
6. heat pump pulsation dryer according to claim 5 is characterized in that: the blowing rod (81) that is provided with the discharging opening (12) that can cut out and open drying chamber in the inner port of rotating shaft (8).
7. heat pump according to claim 3 pulsation dryer, it is characterized in that: motor (9) is buncher.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220185450 CN202648311U (en) | 2012-04-27 | 2012-04-27 | Heat pump impulse dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220185450 CN202648311U (en) | 2012-04-27 | 2012-04-27 | Heat pump impulse dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202648311U true CN202648311U (en) | 2013-01-02 |
Family
ID=47417408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220185450 Expired - Fee Related CN202648311U (en) | 2012-04-27 | 2012-04-27 | Heat pump impulse dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202648311U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103471349A (en) * | 2013-09-03 | 2013-12-25 | 张家港保税区万盛机械工业有限公司 | Pulsed crystallization bed |
| CN104697295A (en) * | 2013-12-04 | 2015-06-10 | 铜陵市永生机电制造有限责任公司 | Fluidized bed |
| CN111023747A (en) * | 2019-12-27 | 2020-04-17 | 安徽麦稻之星机械科技有限公司 | Solar heat pump dryer |
-
2012
- 2012-04-27 CN CN 201220185450 patent/CN202648311U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103471349A (en) * | 2013-09-03 | 2013-12-25 | 张家港保税区万盛机械工业有限公司 | Pulsed crystallization bed |
| CN104697295A (en) * | 2013-12-04 | 2015-06-10 | 铜陵市永生机电制造有限责任公司 | Fluidized bed |
| CN111023747A (en) * | 2019-12-27 | 2020-04-17 | 安徽麦稻之星机械科技有限公司 | Solar heat pump dryer |
| CN111023747B (en) * | 2019-12-27 | 2021-03-30 | 安徽麦稻之星机械科技有限公司 | Solar heat pump dryer |
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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: 20130102 Termination date: 20160427 |