CN203771954U - Grain drying machine - Google Patents
Grain drying machine Download PDFInfo
- Publication number
- CN203771954U CN203771954U CN201420055195.5U CN201420055195U CN203771954U CN 203771954 U CN203771954 U CN 203771954U CN 201420055195 U CN201420055195 U CN 201420055195U CN 203771954 U CN203771954 U CN 203771954U
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- China
- Prior art keywords
- condenser
- evaporimeter
- air
- pipeline
- intake stack
- 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- Withdrawn - After Issue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
- 238000001035 drying Methods 0.000 title claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000003507 refrigerant Substances 0.000 claims description 36
- 230000008676 import Effects 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 4
- 210000002421 cell wall Anatomy 0.000 claims description 3
- 239000004745 nonwoven fabric Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract description 2
- 238000009920 food preservation Methods 0.000 abstract 1
- 235000013339 cereals Nutrition 0.000 description 20
- 230000000694 effects Effects 0.000 description 9
- 238000007791 dehumidification Methods 0.000 description 5
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 208000011580 syndromic disease Diseases 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000035784 germination Effects 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/90—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
- Y02A40/963—Off-grid food refrigeration
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a grain drying machine, and belongs to the technical field of agriculture food preservation and processing. An air inlet of the drying machine is provided with an air inlet device, the air inlet device comprises a first compressor, a second compressor, an air inlet pipeline, a first evaporator, a first condenser and a second condenser, the first evaporator, the first condenser and the second condenser are sequentially arranged in the air inlet pipeline in the air flow direction of the air inlet pipeline, the air inlet pipeline is communicated with the air inlet of the drying machine and an air outlet of the drying machine is provided with a second evaporator; the first compressor is respectively communicated with the first evaporator and the first condenser, and the second compressor is respectively communicated with the second evaporator and the second condenser; the outside of the air inlet pipeline is provided with a heat absorbing piece, and a fan is arranged around the heat absorbing piece; a water collecting tank is arranged under the first evaporator, and a water discharging pump is arranged in the water collecting tank. According to the drying machine, dehumidifying and heating are carried out on dry air flow through air, drying efficiency is high and the grain drying machine is low in energy consumption, low-carbon and environmentally friendly.
Description
Technical field
The utility model relates to a kind of foodstuff drying device, belongs to agricultural food product and preserves and processing technology field.
Background technology
Grain is lived organism, and moisture is its conditions on which persons or things depend for existence.But growing of insect and microorganism brought out in the too high meeting of moisture, easily cause grain heating, fermentation, rotten and germination percentage decline.Taking cereal as example, moisture content when grain harvest is 25～30%, in the time preserving, need to drop to as early as possible safe moisture 13～15%.The cereal of China is gathered in the crops 1～3 time for 1 year, several years of storage, but in cereal production process and grain-drying link, natural drying is easily subject to the restriction of the impact such as weather and place.Along with the large scale application of corn mowing machine and the rise of big farming household, natural drying more and more can not satisfy the demands, must be by means of grain drying.
Current grain drying device mainly contains two kinds, tower dryer and liquefied bed drying plant, and wherein batch formula circular grain drying machine in rower drier is most widely used.Criticize formula circular grain drying machine and comprise tempering chamber, drying chamber, elevator and automatically controlled part, conventionally generate hot blast using burning diesel oil, coal, firewood, stalk and electrical heating etc. as thermal source, hot blast flows in drying chamber, and contact with grain in mobile process, thereby the moisture of taking away is wherein dried grain.
But existing foodstuff drying device is using hot-blast stove as thermal source, and the fuel that hot-blast stove will burn a large amount of produces power, and the energy of consumption is more, and easily to environment.Improving foodstuff drying device drying rate starts with and can have following two approach from drying carrier: one, improve dry wind-warm syndrome, two, reduce the relative humidity of dry wind.The cereal high temperature dryings such as the paddy rice quick-fried waist of easily cracking rice, therefore wind-warm syndrome is strictly controlled in certain scope, is to improve the very effective method of drying efficiency so rely on " relative humidity that reduces dry air "; Especially in the dry processing of the coastal damp-heat area seeds such as Hainan, the relative humidity of surrounding air is very large, and cereal seed is very strict to the requirement of bake out temperature, will after surrounding air low-temperature heat, be delivered directly to the non-constant of effect of drying chamber to article oven dry.In addition, the life-span of hot-blast stove only has 2 ~ 3 years, but selling price is always high, therefore also needs more economic replacement scheme badly.
Utility model content
The technical problems to be solved in the utility model is: propose a kind of air that utilizes and can carry out the high-efficiency and low-cost of dehumidifier oven dry, the foodstuff drying device of energy-conserving and environment-protective.
The utility model is that the technical scheme that solves the problems of the technologies described above proposition is: a kind of foodstuff drying device, the air inlet place of described dryer is provided with air-intake device, described air-intake device comprises the first compressor, the second compressor, intake stack and be successively set on the first evaporimeter in intake stack along intake stack airflow direction, the first condenser and the second condenser, described intake stack forms air port near one end of the second condenser and is communicated with dryer air inlet, described intake stack forms near the other end of the first evaporimeter the air inlet that is communicated with surrounding air, the air outlet place of described dryer is provided with the second evaporimeter, described the first compressor is communicated with the refrigerant exit of the first evaporimeter and the refrigerant import of the first condenser respectively, the refrigerant import of described the first evaporimeter is communicated with the refrigerant exit of the first condenser, between the refrigerant import of described the first evaporimeter and the refrigerant exit of the first condenser, is provided with the first expansion valve, described the second compressor is communicated with the refrigerant exit of the second evaporimeter and the refrigerant import of the second condenser respectively, the refrigerant import of described the second evaporimeter is communicated with the refrigerant exit of the second condenser, between the refrigerant import of described the second evaporimeter and the refrigerant exit of the second condenser, is provided with the second expansion valve, intake stack lateral wall between described evaporimeter and condenser is glued with heat absorbing sheet, and also including can be by the blower fan of natural wind or hot blast drainage process heat absorbing sheet.
Foodstuff drying device of the present utility model will be created a condition in fact exactly, allows the air stream of the proper temperature with low humidity through grain to be dried, and to take away fast moisture, its course of work is as follows:
1) under the main air blower effect of dryer, surrounding air enters intake stack, absorbs heat cooling by the first evaporimeter, and airborne part moisture condensation is separated out and obtained the air that relative humidity is low;
2) air of the low humidity of low temperature recovers room temperature under the effect of heat absorbing sheet and blower fan, obtains the air of the low humidity of room temperature;
3) exchange heat that the first compressor absorbs the first evaporimeter is given the first condenser, and the air of the low humidity of room temperature heats under the effect of the first condenser, becomes the air of the higher temperature of low humidity;
4) the second evaporimeter absorbs the airborne heat of discharging from dryer air outlet, and by the second compressor by exchange heat in the second condenser, the air of the higher temperature to low humidity further heats, and then the air of the satisfactory low humidity of temperature is delivered in dryer grain is dried.
The beneficial effect that the utility model brings is:
1) the utility model utilize the first evaporimeter, the first condenser and and the second compressor carry out heat exchange, not only can be by surrounding air cool-down dehumidification, and dehumidification rate is very high, greatly reduces the energy consumption of dehumidifying; In addition, utilize the heat that condenser obtains cool-down dehumidification fully to utilize, not only be conducive to improve the drying efficiency of dryer, and reduce the energy consumption required to atmosphere temperature rising, heat environmental protection low-carbon (LC) more with respect to hot-blast stove, be particularly suitable for the area of high humility and the season of high humility.
2), if the utility model saves heat absorbing sheet and blower fan, only can obtain the low humidity air of room temperature.The utility model creatively returns to rapidly room temperature by the surrounding air after cool-down dehumidification by heat absorbing sheet and blower fan, thereby the high heat exchanger effectiveness that utilizes compressor obtains the low humidity air of high temperature, and required energy consumption is only the power consumption of drive compression machine and blower fan.Compared with the surrounding air that only can obtain high temperature with traditional hot-blast stove heating, the utility model not only can obtain the high temperature air of low humidity, and has greatly improved Energy Efficiency Ratio.
3) the utility model arranges the second evaporimeter at the air outlet place of dryer, and the airborne waste heat of dryer being discharged by the second condenser and the second compressor further utilizes, can improve the temperature that enters the air in dryer, thereby save the hot-blast stove that the life-span is short, price is high, improve the whole service life of dryer, even in cold the Northeast, also can meet the requirement of drying grain completely.
For the moisture that prevents condensation from surrounding air to separate out is brought in dryer under the effect of air-flow, the utility model arranges water leg under the first evaporimeter.In addition, under the effect of air-flow, can form negative pressuren zone in water leg, therefore the utility model arranges draining pump and can prevent the air inversion at the water leg discharge outlet place that negative pressure causes in water leg.
For the moisture that further prevents condensation from surrounding air to separate out is brought in dryer under the effect of air-flow, the utility model can adopt one of following two kinds of technical schemes:
(1) described intake stack is horizontally disposed with, and in the intake stack between described the first evaporimeter and heat absorbing sheet, is provided with ventilative water bar, and described water bar is for preventing that the moisture in water leg is taken to condenser.As preferred version, described water bar is positioned at directly over the cell wall of water leg near the first condenser one side.Further, described water bar is one deck or the multi-layer nonwoven fabrics that is fixed on intake stack inner side.
(2) described intake stack is divided into three sections, is respectively the first pipeline, second pipe and the 3rd pipeline, and wherein the first pipeline vertically arranges, and described the first evaporimeter is placed in the first pipeline; Second pipe is horizontally disposed with, and described the first condenser and the second condenser are arranged on the inner side of second pipe, and described heat absorbing sheet is arranged on the outside of second pipe; The 3rd pipeline is positioned at the below of second pipe, and the 3rd pipeline is communicated with the outlet of the first pipeline and the import of second pipe respectively, and described water leg is positioned at the inside bottom of the 3rd pipeline.As improving further, the air outlet of described the first pipeline is lower than the bottom of second pipe.
Brief description of the drawings
Below in conjunction with accompanying drawing, foodstuff drying device of the present utility model is described further.
Fig. 1 is the principle schematic of the utility model embodiment mono-.
Fig. 2 is the principle schematic of the utility model embodiment bis-.
Detailed description of the invention
Embodiment mono-
The foodstuff drying device of the present embodiment, as shown in Figure 1, the air inlet place of dryer is provided with air-intake device, the air-intake device of the present embodiment comprises the first compressor 2, the second compressor 11, intake stack 9 and is successively set on the first evaporimeter 2, the first condenser 4 and the second condenser 14 in intake stack 9 along intake stack 9 airflow directions, intake stack 9 forms air port near one end of the second condenser 14 and is communicated with the air inlet 10 of dryer, and air outlet 13 places of dryer are provided with the second evaporimeter 12; The first compressor 1 is communicated with the refrigerant exit of the first evaporimeter 2 and the refrigerant import of the first condenser 4 respectively, the refrigerant import of the first evaporimeter 2 is communicated with the refrigerant exit of the first condenser 4, between the refrigerant import of the first evaporimeter 2 and the refrigerant exit of the first condenser 4, is provided with the first expansion valve 6; The second compressor 11 is communicated with the refrigerant exit of the second evaporimeter 12 and the refrigerant import of the second condenser 14 respectively, the refrigerant import of the second evaporimeter 12 is communicated with the refrigerant exit of the second condenser 14, between the refrigerant import of the second evaporimeter 12 and the refrigerant exit of the second condenser 14, is provided with the second expansion valve 16; Intake stack 9 outsides are provided with heat absorbing sheet 3, and heat absorbing sheet 3, between the first evaporimeter 2 and the first condenser 4, is provided with blower fan 5 near heat absorbing sheet 3, and blower fan 5 can be by natural wind (surrounding air) drainage through heat absorbing sheet 3.
The air-intake device of the foodstuff drying device of the present embodiment by surrounding air successively through the first evaporimeter 2 carry out cool-down dehumidification, through heat absorbing sheet 3 recover room temperature, after the first condenser 4 is heated, obtain middle temperature is dried air, after heating by the second condenser 14 again, obtain carrying wet very capable high temperature drying air, then high temperature drying air enters dryer, equably by grain to be dried, the moisture absorption in grain to be dried after heat energy in dry air, overflow rapidly and taken away by air-flow.
The present embodiment can also be done following improvement: under the first evaporimeter 2, be provided with water leg 7, be provided with draining pump 8 in water leg 7.Like this, can prevent that the moisture that condensation from surrounding air is separated out is brought in dryer under the effect of air-flow.
The present embodiment can also be improved further: intake stack 9 is horizontally disposed with, in intake stack 9 between the first evaporimeter 2 and heat absorbing sheet 3, be provided with ventilative baffle plate (not shown), thereby this baffle plate is taken to the first condenser 4 and the second condenser 14 humidity of heating evaporation increase air again for preventing the moisture in water leg 7.
As preferred version, the baffle plate in the present embodiment can be positioned at directly over the cell wall of water leg 7 near the first condenser one side.In the present embodiment, water bar is the nonwoven that is fixed on one or more layers waterproof and breathable of intake stack 9 inner sides.
Compared with traditional use hot-blast stove mode of heating, the foodstuff drying device of the present embodiment makes full use of the waste heat of lowering the temperature except the heat after temperature and dryer discharge air the air in intake stack 9 is heated, not only save the energy, reduce environmental pollution, and the present embodiment uses high temperature drying air instead of the larger air of humidity to dry grain, drying effect is better.
Embodiment bis-
The foodstuff drying device of the present embodiment and embodiment mono-are basic identical, its difference is: as shown in Figure 2, the intake stack 9 of the present embodiment is divided into three sections, is respectively the first pipeline, second pipe and the 3rd pipeline, wherein the first pipeline vertically arranges, and the first evaporimeter 2 is placed in the first pipeline; Second pipe is horizontally disposed with, and the first condenser 4 and the second condenser 14 are arranged on the inner side of second pipe, and heat absorbing sheet 3 is arranged on the outside of second pipe; The 3rd pipeline is positioned at the below of second pipe, and the 3rd pipeline is communicated with the outlet of the first pipeline and the import of second pipe respectively, and water leg 7 is positioned at the inside bottom of the 3rd pipeline.As preferred version, in the present embodiment, the air outlet of the first pipeline can be lower than the bottom of second pipe.
Like this, after the air inlet biasing of air-intake device, balanced windage, increases the humidity of air thereby therefore also the moisture in water leg 7 can not taken in condenser 4 to heating evaporation again.
The utility model is not limited to above-described embodiment, and all employings are equal to replaces the technical scheme forming, and all drops on the protection domain of the utility model requirement.
Claims (7)
1. a foodstuff drying device, the air inlet place of described dryer is provided with air-intake device, it is characterized in that: described air-intake device comprises the first compressor, the second compressor, intake stack and be successively set on the first evaporimeter in intake stack along intake stack airflow direction, the first condenser and the second condenser, described intake stack forms air port near one end of the second condenser and is communicated with the air inlet of dryer, described intake stack forms near the other end of the first evaporimeter the air inlet that is communicated with surrounding air, the air outlet place of described dryer is provided with the second evaporimeter,
Described the first compressor is communicated with the refrigerant exit of the first evaporimeter and the refrigerant import of the first condenser respectively, the refrigerant import of described the first evaporimeter is communicated with the refrigerant exit of the first condenser, between the refrigerant import of described the first evaporimeter and the refrigerant exit of the first condenser, is provided with the first expansion valve;
Described the second compressor is communicated with the refrigerant exit of the second evaporimeter and the refrigerant import of the second condenser respectively, the refrigerant import of described the second evaporimeter is communicated with the refrigerant exit of the second condenser, between the refrigerant import of described the second evaporimeter and the refrigerant exit of the second condenser, is provided with the second expansion valve;
Intake stack lateral wall between described evaporimeter and condenser is glued with heat absorbing sheet, and also including can be by the blower fan of natural wind or hot blast drainage process heat absorbing sheet.
2. foodstuff drying device according to claim 1, is characterized in that: under described the first evaporimeter, be provided with water leg, in described water leg, be provided with draining pump.
3. foodstuff drying device according to claim 2, it is characterized in that: described intake stack is horizontally disposed with, in intake stack between described the first evaporimeter and heat absorbing sheet, be provided with ventilative water bar, described water bar is for preventing that the moisture in water leg is taken to condenser.
4. foodstuff drying device according to claim 3, is characterized in that: described water bar is positioned at directly over the cell wall of water leg near the first condenser one side.
5. foodstuff drying device according to claim 3, is characterized in that: described water bar is one deck or the multi-layer nonwoven fabrics that is fixed on intake stack inner side.
6. foodstuff drying device according to claim 2, is characterized in that: described intake stack is divided into three sections, is respectively the first pipeline, second pipe and the 3rd pipeline, and wherein the first pipeline vertically arranges, and described the first evaporimeter is placed in the first pipeline; Second pipe is horizontally disposed with, and described the first condenser and the second condenser are arranged on the inner side of second pipe, and described heat absorbing sheet is arranged on the outside of second pipe; The 3rd pipeline is positioned at the below of second pipe, and the 3rd pipeline is communicated with the outlet of the first pipeline and the import of second pipe respectively, and described water leg is positioned at the inside bottom of the 3rd pipeline.
7. foodstuff drying device according to claim 6, is characterized in that: the air outlet of described the first pipeline is lower than the bottom of second pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420055195.5U CN203771954U (en) | 2014-01-28 | 2014-01-28 | Grain drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420055195.5U CN203771954U (en) | 2014-01-28 | 2014-01-28 | Grain drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203771954U true CN203771954U (en) | 2014-08-13 |
Family
ID=51289139
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420055195.5U Withdrawn - After Issue CN203771954U (en) | 2014-01-28 | 2014-01-28 | Grain drying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203771954U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103791712A (en) * | 2014-01-28 | 2014-05-14 | 滁州奥岚格机械有限公司 | Grain drier |
| CN106070600A (en) * | 2016-08-22 | 2016-11-09 | 安徽理工大学 | It is applied to the multilamellar heat pipe that grain heat radiation is dried |
-
2014
- 2014-01-28 CN CN201420055195.5U patent/CN203771954U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103791712A (en) * | 2014-01-28 | 2014-05-14 | 滁州奥岚格机械有限公司 | Grain drier |
| CN103791712B (en) * | 2014-01-28 | 2015-10-28 | 滁州奥岚格机械有限公司 | Foodstuff drying device |
| CN106070600A (en) * | 2016-08-22 | 2016-11-09 | 安徽理工大学 | It is applied to the multilamellar heat pipe that grain heat radiation is dried |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140813 Effective date of abandoning: 20151028 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |