CN204104799U - With the air energy high-temperature dehumidification heat pump tobacco leaf drying system of heat sink - Google Patents
With the air energy high-temperature dehumidification heat pump tobacco leaf drying system of heat sink Download PDFInfo
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- CN204104799U CN204104799U CN201420580983.6U CN201420580983U CN204104799U CN 204104799 U CN204104799 U CN 204104799U CN 201420580983 U CN201420580983 U CN 201420580983U CN 204104799 U CN204104799 U CN 204104799U
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- gas
- liquid separator
- heat exchanger
- tobacco leaf
- heat
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- 238000001035 drying Methods 0.000 title claims abstract description 23
- 241000208125 Nicotiana Species 0.000 title claims abstract description 22
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 22
- 238000007791 dehumidification Methods 0.000 title claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 239000007921 spray Substances 0.000 claims abstract description 6
- 230000001172 regenerating effect Effects 0.000 claims description 9
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 238000001816 cooling Methods 0.000 abstract description 5
- 230000002269 spontaneous effect Effects 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 241000196324 Embryophyta Species 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 13
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- 238000004781 supercooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000243 solution Substances 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
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- Drying Of Solid Materials (AREA)
Abstract
The utility model belongs to tobacco drying plant field, is specifically related to a kind of air energy high-temperature dehumidification heat pump tobacco leaf drying system with heat sink.This system it comprise internal circulation heat-exchanging device, compressor, external circulation heat exchanger, main electric expansion valve, spray electric expansion valve and gas-liquid separator; Cross valve and changement is connected with between described internal circulation heat-exchanging device and external circulation heat exchanger; Described cross valve also has gas-liquid separator in succession.This energy saving of system environmental protection, effectively shortens baking time, substantially increases and dries efficiency and quality, have dehumidification function, effectively can remove the moisture in baking room, and the energy ezpenditure avoiding the direct hydrofuge of common baking room to bring, saves the energy further.In addition this system also has cooling function, can carry out refrigerating operaton, effective temperature control, meet the technological requirement of tobacco leaf drying in the spontaneous heating stage at tobacco leaf drying initial stage.
Description
Technical field
The utility model belongs to tobacco equipment field, is specifically related to a kind of air energy high-temperature dehumidification heat pump tobacco leaf drying system with heat sink.
Background technology
Current tobacco drying device generally all uses coal-fired barn or electric heating barn to dry.Adopt coal-fired oven dry, not only can be able to pollute air, and drying time is long, efficiency utilization rate is low, labor strength, and production efficiency is low; And it is high to adopt the oven dry of electric heating barn to there is energy consumption, dries quantity is low, adds production cost simultaneously.In addition current common baking room not there is dehumidification function, need direct hydrofuge, turn increase energy ezpenditure, lack cooling function, refrigerating operaton cannot be carried out in the spontaneous heating stage at tobacco leaf drying initial stage, effective temperature control, to meet the technological requirement of tobacco leaf drying.
Utility model content
The utility model, for the deficiencies in the prior art, provides a kind of air energy high-temperature dehumidification heat pump tobacco leaf drying system with heat sink, its compact conformation, reasonable in design, not only improve efficiency utilization rate dramatically, also effectively shorten baking time, substantially increase and dry efficiency and quality.
The technical solution of the utility model is achieved in that a kind of air energy high-temperature dehumidification heat pump tobacco leaf drying system with heat sink, comprises internal circulation heat-exchanging device, compressor, external circulation heat exchanger, main electric expansion valve, sprays electric expansion valve and gas-liquid separator; Cross valve and changement is connected with between described internal circulation heat-exchanging device and external circulation heat exchanger; Described cross valve also has gas-liquid separator in succession; Described compressor is connected with described internal circulation heat-exchanging device by pipeline one end, and the other end is connected with described gas-liquid separator; Described main electric expansion valve is arranged on the pipeline between described changement and gas-liquid separator, and described injection electric expansion valve one end is arranged between main electric expansion valve and gas-liquid separator, and the other end is arranged between cross valve and gas-liquid separator; Pipeline between described compressor and cross valve is connected with control valve.
Preferably, described internal circulation heat-exchanging device comprises Inner eycle blower fan and is arranged on interior heat exchanger and the supplementary heat exchanger of this Inner eycle blower fan side.
Preferably, described external circulation heat exchanger comprises outer circulation blower fan and is arranged on the external heat exchanger of this outer circulation blower fan side.
Preferably, described gas-liquid separator is the gas-liquid separator with regenerative apparatus.
The utility model solves the defect existed in background technology, and the utility model has beneficial effect and is:
The air energy high-temperature dehumidification heat pump tobacco leaf drying system of the band heat sink that the utility model provides, adopt heat pump principle technology, effectively being delivered to by heat energy in the surrounding air of low-temperature level needs in the baking room of high temperature, to reach the heat energy of baking needed, compare with traditional electrical heating barn, not only improve efficiency utilization rate dramatically, energy-conserving and environment-protective, also effectively shorten baking time, substantially increase and dry efficiency and quality.This device also has dehumidification function, effectively can remove the moisture in baking room, and avoid the energy ezpenditure that the direct hydrofuge of common baking room brings, comprehensive energy efficiency is higher, saves the energy further, reduces costs.In addition utility model also has cooling function, can carry out refrigerating operaton, effective temperature control, meet the technological requirement of tobacco leaf drying in the spontaneous heating stage at tobacco leaf drying initial stage.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the air energy high-temperature dehumidification heat pump tobacco leaf drying system of band heat sink;
In figure: 1-compressor, 2-internal circulation heat-exchanging device, 21-Inner eycle blower fan, 22-supplementary heat exchanger, heat exchanger in 23-, 3-control valve, 4-cross valve, 5-outer circulation air heating device, 51-outer circulation blower fan, 52-external heat exchanger, 6-sprays electric expansion valve, the main electric expansion valve of 7-, 8-gas-liquid separator, 9-changement, 10-pipeline.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
A kind of air energy high-temperature dehumidification heat pump tobacco leaf drying system with heat sink as shown in Figure 1, comprise and to be arranged in apparatus casing by air channel and baking room UNICOM internal circulation heat-exchanging device 2, compressor 1, external circulation heat exchanger 5, main electric expansion valve 7, to spray electric expansion valve 6 and gas-liquid separator 8, described device is interconnected by pipeline 10.Cross valve 4 and changement 9 is connected with between internal circulation heat-exchanging device 2 and external circulation heat exchanger 5; Cross valve 4 also has gas-liquid separator 8 in succession; Compressor 1 is connected with described internal circulation heat-exchanging device 2 by pipeline 10 one end, and the other end is connected with described gas-liquid separator 8; Main electric expansion valve 7 is arranged on the pipeline between changement 9 and gas-liquid separator 8, and spray electric expansion valve 6 one end and be arranged between main electric expansion valve 7 and gas-liquid separator 8, the other end is arranged between cross valve 4 and gas-liquid separator 8; Pipeline 10 between compressor 1 and cross valve 4 is connected with control valve 3.Internal circulation heat-exchanging device 2 comprises Inner eycle blower fan 21 and is arranged on interior heat exchanger 23 and the supplementary heat exchanger 22 of this Inner eycle blower fan side.External circulation heat exchanger 5 comprises outer circulation blower fan 51 and is arranged on the external heat exchanger 52 of this outer circulation blower fan side.Gas-liquid separator 8 is the gas-liquid separator with regenerative apparatus.
The course of work of the present utility model is: be divided into heating mode, dehumidification mode and cooling mode.In a heating mode, by the work of compressor 1, the gas of refrigerant boil down to HTHP enters the interior heat exchanger 23 in internal circulation heat-exchanging device 2, supplementary heat exchanger 22 is entered through cross valve 4, after rejecting heat to baking room by Inner eycle blower fan 21 and air channel, refrigerant condensation becomes the liquid of HTHP, through changement 9, enter the gas-liquid separator 8 with regenerative apparatus, heat exchange further with low temperature return-air, improve degree of supercooling, enter the liquid refrigerants that the throttling of main electric expansion valve 7 becomes low-temp low-pressure afterwards, enter external heat exchanger 52 again to evaporate, the gas of low-temp low-pressure is become by the heat in the effect absorbing environmental air of outer circulation blower fan 51, enter the gas-liquid separator 8 with regenerative apparatus, compressor 1 is got back to after the further heat exchange of condensed high-temperature liquid state refrigerant, complete a circulation.Along with circulation is constantly carried out, the heat in surrounding air is just continually to being discharged in baking room, and realize drying effect, not only efficiency utilization rate is high, also significantly shortens baking time, improve and dry efficiency, and dries quantity is good.
Under dehumidification mode, by the work of compressor 1, the gas of refrigerant boil down to HTHP enters interior heat exchanger 23, external heat exchanger 52 is entered through cross valve 4, refrigerant condensation becomes the liquid of HTHP, enter the gas-liquid separator 8 with regenerative apparatus, heat exchange further with low temperature return-air, improve degree of supercooling, enter the liquid refrigerants that the throttling of main electric expansion valve 7 becomes low-temp low-pressure afterwards, then enter supplementary heat exchanger 22 to evaporate, enter the gas-liquid separator 8 with regenerative apparatus again, compressor 1 is got back to after the further heat exchange of condensed high-temperature liquid state refrigerant, complete a circulation.Because supplementary heat exchanger 22 surface temperature is lower than the dew-point temperature of air in baking room, hot and humid air in baking room is lowered the temperature after supplementary heat exchanger 22, steam wherein becomes water to discharge in supplementary heat exchanger 22 surface condensation, and the heat of the release of steam condensation is simultaneously absorbed along with kind of refrigeration cycle is discharged in baking room at interior heat exchanger 23 place by refrigerant again.
Under cooling mode, by the work of compressor 1, the gas of refrigerant boil down to HTHP is through control valve 3, external heat exchanger 52 is entered through cross valve 4, refrigerant condensation becomes the liquid of HTHP, enter the gas-liquid separator 8 with regenerative apparatus, heat exchange further with low temperature return-air, improve degree of supercooling, enter the liquid refrigerants that the throttling of main electric expansion valve 7 becomes low-temp low-pressure afterwards, then enter supplementary heat exchanger 22 to evaporate, enter the gas-liquid separator 8 with regenerative apparatus again, compressor 1 is got back to after the further heat exchange of condensed high-temperature liquid state refrigerant, complete a circulation.Because supplementary heat exchanger 22 surface temperature is lower than the dew-point temperature of air in baking room, the hot and humid air in baking room is lowered the temperature after supplementary heat exchanger 22, and simultaneously steam wherein becomes water to discharge in supplementary heat exchanger 22 surface condensation.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (4)
1. the air energy high-temperature dehumidification heat pump tobacco leaf drying system with heat sink, is characterized in that: comprise internal circulation heat-exchanging device (2), compressor (1), external circulation heat exchanger (5), main electric expansion valve (7), spray electric expansion valve (6) and gas-liquid separator (8); Cross valve (4) and changement (9) is connected with between described internal circulation heat-exchanging device (2) and external circulation heat exchanger (5); Described cross valve (4) also has gas-liquid separator (8) in succession; Described compressor (1) is connected with described internal circulation heat-exchanging device (2) by pipeline (10) one end, and the other end is connected with described gas-liquid separator (8); Described main electric expansion valve (7) is arranged on the pipeline (10) between described changement (9) and gas-liquid separator (8), described injection electric expansion valve (6) one end is arranged between main electric expansion valve (7) and gas-liquid separator (8), and the other end is arranged between cross valve (4) and gas-liquid separator (8); Pipeline (10) between described compressor (1) and cross valve (4) is gone up and is connected with control valve (3).
2. the air energy high-temperature dehumidification heat pump tobacco leaf drying system of band heat sink according to claim 1, is characterized in that: described internal circulation heat-exchanging device (2) comprises Inner eycle blower fan (21) and is arranged on interior heat exchanger (23) and the supplementary heat exchanger (22) of this Inner eycle blower fan side.
3. the air energy high-temperature dehumidification heat pump tobacco leaf drying system of band heat sink according to claim 1, is characterized in that: described external circulation heat exchanger (5) comprises outer circulation blower fan (51) and is arranged on the external heat exchanger (52) of this outer circulation blower fan side.
4. the air energy high-temperature dehumidification heat pump tobacco leaf drying system of band heat sink according to claim 1, is characterized in that: described gas-liquid separator (8) is the gas-liquid separator with regenerative apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420580983.6U CN204104799U (en) | 2014-10-09 | 2014-10-09 | With the air energy high-temperature dehumidification heat pump tobacco leaf drying system of heat sink |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420580983.6U CN204104799U (en) | 2014-10-09 | 2014-10-09 | With the air energy high-temperature dehumidification heat pump tobacco leaf drying system of heat sink |
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| Publication Number | Publication Date |
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| CN204104799U true CN204104799U (en) | 2015-01-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420580983.6U Expired - Lifetime CN204104799U (en) | 2014-10-09 | 2014-10-09 | With the air energy high-temperature dehumidification heat pump tobacco leaf drying system of heat sink |
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| CN (1) | CN204104799U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105495673A (en) * | 2016-01-20 | 2016-04-20 | 曾文 | Tobacco dryer and tobacco drying room |
| CN108202076A (en) * | 2018-01-02 | 2018-06-26 | 大连理工大学 | A kind of pump coupled heat biological heat anhydration system and method |
| CN109588755A (en) * | 2018-11-28 | 2019-04-09 | 湖南科技大学 | Interior circulating dehumidification bulk curing barn baking system |
| CN109588754A (en) * | 2018-11-28 | 2019-04-09 | 湖南科技大学 | Interior circulating-heating dehumidification device for bulk curing barn transformation |
| CN110794761A (en) * | 2019-11-28 | 2020-02-14 | 安徽理工大学 | Automatic temperature control tobacco leaf dryer monitoring system |
-
2014
- 2014-10-09 CN CN201420580983.6U patent/CN204104799U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105495673A (en) * | 2016-01-20 | 2016-04-20 | 曾文 | Tobacco dryer and tobacco drying room |
| CN105495673B (en) * | 2016-01-20 | 2017-06-06 | 曾文 | Leaf drier and tobacco leaf drying room |
| CN108202076A (en) * | 2018-01-02 | 2018-06-26 | 大连理工大学 | A kind of pump coupled heat biological heat anhydration system and method |
| CN109588755A (en) * | 2018-11-28 | 2019-04-09 | 湖南科技大学 | Interior circulating dehumidification bulk curing barn baking system |
| CN109588754A (en) * | 2018-11-28 | 2019-04-09 | 湖南科技大学 | Interior circulating-heating dehumidification device for bulk curing barn transformation |
| CN110794761A (en) * | 2019-11-28 | 2020-02-14 | 安徽理工大学 | Automatic temperature control tobacco leaf dryer monitoring system |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160819 Address after: 650217, Kunming, Yunnan province by the information industry base in the spring of the diffuse Road, No. 80 Yunnan Venture Park B1 building B1422 No. 1 Patentee after: Yunnan Zhonghai Clean Technology Co., Ltd. Address before: 650217, Yunnan, Kunming, Kunming Province opened the district information industry base, No. 80, Spring Spring Road, Yunnan returnees Pioneer Park 2, 4 floor, No. 04281 Patentee before: YUNNAN ZHONGHAI LUDE TECHNOLOGY CO., LTD. |