CN201364007Y - Air source high-temperature heat pump dryer - Google Patents
Air source high-temperature heat pump dryer Download PDFInfo
- Publication number
- CN201364007Y CN201364007Y CNU2009200520072U CN200920052007U CN201364007Y CN 201364007 Y CN201364007 Y CN 201364007Y CN U2009200520072 U CNU2009200520072 U CN U2009200520072U CN 200920052007 U CN200920052007 U CN 200920052007U CN 201364007 Y CN201364007 Y CN 201364007Y
- Authority
- CN
- China
- Prior art keywords
- heat pump
- fin
- temperature heat
- condenser
- evaporator
- 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 32
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 abstract description 17
- 239000003570 air Substances 0.000 abstract description 15
- 239000012080 ambient air Substances 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 6
- 238000007791 dehumidification Methods 0.000 description 6
- 239000003507 refrigerant Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000005485 electric heating Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种空气源高温热泵烘干机。The utility model relates to an air source high temperature heat pump dryer.
背景技术 Background technique
用热泵除湿干燥其能耗远低于燃料加热、电加热等除湿干燥方式,因此在低温干燥(如物料所需干燥温度低于55℃)中往往采用热泵除湿干燥。但当物料要求干燥温度高(如要求干燥温度60~90℃)时,普通热泵干燥无法实现;高温热泵因缺少高温热源,往往也无法实现;二氧化碳热泵可实现高温干燥,但因其成本高,目前推广应用困难;因此,在需要高温除湿干燥的场所,目前一般为燃料加热、电加热等高耗能的方式。The energy consumption of heat pump dehumidification and drying is much lower than fuel heating, electric heating and other dehumidification and drying methods. Therefore, heat pump dehumidification and drying are often used in low-temperature drying (such as the drying temperature required for materials is lower than 55°C). However, when the material requires a high drying temperature (such as a drying temperature of 60-90°C), ordinary heat pump drying cannot be realized; high-temperature heat pumps often cannot be realized due to the lack of high-temperature heat sources; carbon dioxide heat pumps can achieve high-temperature drying, but because of their high cost, At present, it is difficult to popularize and apply; therefore, in places that require high temperature dehumidification and drying, fuel heating, electric heating and other high energy consumption methods are generally used at present.
实用新型内容Utility model content
针对现有技术的缺点,本实用新型的目的是提供一种降低高温干燥的能耗及运行成本的空气源高温热泵烘干机。Aiming at the shortcomings of the prior art, the purpose of this utility model is to provide an air source high temperature heat pump dryer which reduces the energy consumption and operating cost of high temperature drying.
为实现上述目的,本实用新型的技术方案为:一种空气源高温热泵烘干机,其包括低温热泵系统及高温热泵系统,该低温热泵系统包括构成一循环回路的低温热泵压缩机、第一气液分离器、第一翅片蒸发器、第一节流装置及第一翅片冷凝器,该高温热泵系统包括构成一循环回路的高温热泵压缩机、第二气液分离器、第二翅片蒸发器、第二节流装置及第二翅片冷凝器,In order to achieve the above purpose, the technical solution of this utility model is: an air source high temperature heat pump dryer, which includes a low temperature heat pump system and a high temperature heat pump system, the low temperature heat pump system includes a low temperature heat pump compressor forming a circulation loop, a first A gas-liquid separator, a first finned evaporator, a first throttling device, and a first finned condenser, the high-temperature heat pump system includes a high-temperature heat pump compressor, a second gas-liquid separator, and a second finned sheet evaporator, second throttling device and second finned condenser,
该第二翅片蒸发器及第一翅片蒸发器构成逐级降温系统,该第一翅片冷凝器及第二翅片冷凝器构成逐级加热升温系统,来自干燥室的湿热气体经第二翅片蒸发器及第一翅片蒸发器的逐级降温后排到外界环境空气中,外界环境空气经过第一翅片冷凝器及第二翅片冷凝器的逐级加热升温后进入烘干室。The second fin evaporator and the first fin evaporator constitute a step-by-step cooling system, the first fin condenser and the second fin condenser constitute a step-by-step heating system, and the hot and humid gas from the drying chamber passes through the second The finned evaporator and the first finned evaporator are cooled step by step and discharged into the external ambient air, and the external ambient air enters the drying chamber after being heated step by step by the first finned condenser and the second finned condenser .
该低温热泵系统还包括连接于第一节流装置及第一翅片冷凝器之间的第一过滤器,该高温热泵系统还包括连接于第二节流装置及第二翅片冷凝器之间的第二过滤器。The low-temperature heat pump system also includes a first filter connected between the first throttling device and the first fin condenser, and the high-temperature heat pump system also includes a filter connected between the second throttling device and the second fin condenser the second filter.
该低温热泵系统还包括连接于第一过滤器与第一翅片冷凝器之间的第一储液器,该高温热泵系统还包括连接于第二过滤器与第二翅片冷凝器之间的第二储液器。The low temperature heat pump system also includes a first liquid reservoir connected between the first filter and the first fin condenser, and the high temperature heat pump system also includes a liquid reservoir connected between the second filter and the second fin condenser Second reservoir.
另外,本实用新型还提供了一种空气源高温热泵烘干机,其包括多级温度热泵系统,每一级温度热泵系统包括构成循环回路的热泵、气液分离器、翅片蒸发器、节流装置及翅片冷凝器,In addition, the utility model also provides an air source high-temperature heat pump dryer, which includes a multi-stage temperature heat pump system, and each stage temperature heat pump system includes a heat pump, a gas-liquid separator, a finned evaporator, a section Flow device and finned condenser,
该翅片蒸发器根据热泵系统的温度级别构成逐级降温系统,该翅片冷凝器根据热泵系统的温度级别构成逐级加热升温系统,来自干燥室的湿热气体经逐级降温系统的逐级降温后排出烘干室,外界环境空气经过逐级加热升温系统的逐级加热升温后进入干燥室。The fin evaporator forms a step-by-step cooling system according to the temperature level of the heat pump system, and the fin condenser forms a step-by-step heating and heating system according to the temperature level of the heat pump system. Finally, it is discharged from the drying room, and the ambient air enters the drying room after being heated step by step by the step-by-step heating system.
每一级温度热泵系统包括连接于节流装置与翅片冷凝器之间的过滤器及储液器。Each temperature heat pump system includes a filter and a liquid reservoir connected between the throttling device and the fin condenser.
本实用新型与现有技术相比具有如下优点和有益效果:Compared with the prior art, the utility model has the following advantages and beneficial effects:
用空气源高温热泵实现高温烘干,即避免了废热排出造成的热污染,又充分利用了废热,同时由于热泵固有的高能效比特点,可使高温烘干能耗大幅度降低,相对于一般燃料加热、电加热等高温烘干方法,烘干能耗降低幅度可达60%以上。The air source high temperature heat pump is used to achieve high temperature drying, which avoids the thermal pollution caused by waste heat discharge and makes full use of waste heat. At the same time, due to the inherent high energy efficiency ratio of the heat pump, the energy consumption of high temperature drying can be greatly reduced. Fuel heating, electric heating and other high-temperature drying methods can reduce drying energy consumption by more than 60%.
附图说明 Description of drawings
图1为本实用新型实施例1的结构示意图。Fig. 1 is a schematic structural view of Embodiment 1 of the present utility model.
具体实施方式 Detailed ways
以下结合附图对本实用新型进行详细的描述。Below in conjunction with accompanying drawing, the utility model is described in detail.
实施例1Example 1
如图1所示,一种空气源高温热泵烘干机,其包括低温热泵系统及高温热泵系统,该低温热泵系统包括构成一循环回路的低温热泵压缩机11、第一气液分离器17、第一翅片蒸发器16、第一节流装置15及第一翅片冷凝器12,该高温热泵系统包括构成一循环回路的高温热泵压缩机21、第二气液分离器27、第二翅片蒸发器26、第二节流装置25及第二翅片冷凝器22,As shown in Figure 1, an air source high-temperature heat pump dryer includes a low-temperature heat pump system and a high-temperature heat pump system. The low-temperature heat pump system includes a low-temperature
该第二翅片蒸发器26及第一翅片蒸发器16构成逐级除湿降温系统,该第一翅片冷凝器12及第二翅片冷凝器22构成逐级加热升温系统,来自干燥室的湿热气体经第二翅片蒸发器26及第一翅片蒸发器16的逐级除湿降温后排到外界环境空气中,外界环境空气经过第一翅片冷凝器12及第二翅片冷凝器22的逐级加热升温后进入烘干室。The
空气源高温热泵烘干机包括两级除湿降温系统与两级加热升温系统,两级系统分别采用不同的制冷剂以满足相应的工作条件要求。该低温热泵系统可采用普通的制冷剂,如R22、R407C等,该高温热泵系统采用高温制冷剂。The air source high temperature heat pump dryer includes a two-stage dehumidification and cooling system and a two-stage heating and heating system. The two-stage systems use different refrigerants to meet the corresponding working conditions. The low-temperature heat pump system can use common refrigerants, such as R22, R407C, etc., and the high-temperature heat pump system can use high-temperature refrigerants.
该低温热泵系统还包括连接于第一节流装置15及第一翅片冷凝器12之间的第一过滤器14,该高温热泵系统还包括连接于第二节流装置25及第二翅片冷凝器22之间的第二过滤器24。The low-temperature heat pump system also includes a
该低温热泵系统还包括连接于第一过滤器14与第一翅片冷凝器12之间的第一储液器13,该高温热泵系统还包括连接于第二过滤器24与第二翅片冷凝器22之间的第二储液器23。The low-temperature heat pump system also includes a first
该低温热泵系统的制冷剂冷凝温度为20℃~65℃,该高温热泵系统的制冷剂冷凝温度为40℃~110℃。The condensing temperature of the refrigerant in the low-temperature heat pump system is 20°C-65°C, and the condensing temperature of the refrigerant in the high-temperature heat pump system is 40°C-110°C.
本实用新型空气源高温热泵烘干机的运行方式如下:The operation mode of the utility model air source high temperature heat pump dryer is as follows:
外界环境空气,如25℃的空气进入设备后经过第一翅片冷凝器12被初步加热,如加热到55℃;被初步加热后的空气然后通过第二翅片冷凝器22二次加热,如加热到90℃;被二次加热后的高温干燥空气进入烘干室烘干物料。External ambient air, such as air at 25°C enters the equipment and is initially heated through the first
烘干物料后的空气温度降低,如降低到70℃,并排出烘干室;烘干室排气先经过第二翅片蒸发器26一次降温,如降低到40℃,然后再经过第一翅片蒸发器16二次降温,如降低到20℃,二次降温后的烘干室排气排出设备。The temperature of the air after drying the material is lowered, for example, to 70°C, and discharged out of the drying chamber; the exhaust gas from the drying chamber first passes through the
实施例2Example 2
本实施例是在实施例1的基础上实现将低温及高温两级热泵系统扩展到多级的情况。具体为,一种空气源高温热泵烘干机,其包括多级温度热泵系统,每一级温度热泵系统包括构成循环回路的热泵压缩机、气液分离器、翅片蒸发器、节流装置及翅片冷凝器,In this embodiment, on the basis of Embodiment 1, the low-temperature and high-temperature two-stage heat pump system is extended to multiple stages. Specifically, it is an air source high temperature heat pump dryer, which includes a multi-stage temperature heat pump system, and each stage temperature heat pump system includes a heat pump compressor, a gas-liquid separator, a finned evaporator, a throttling device and a circulation loop. finned condenser,
该翅片蒸发器根据热泵系统的温度级别构成逐级降温系统,该翅片冷凝器根据热泵系统的温度级别构成逐级加热升温系统,来自干燥室的湿热气体经逐级降温系统的逐级降温后排出烘干室,外界环境空气经过逐级加热升温系统的逐级加热升温后进入干燥室。The fin evaporator forms a step-by-step cooling system according to the temperature level of the heat pump system, and the fin condenser forms a step-by-step heating and heating system according to the temperature level of the heat pump system. Finally, it is discharged from the drying room, and the ambient air enters the drying room after being heated step by step by the step-by-step heating system.
每一级温度热泵系统包括连接于节流装置与翅片冷凝器之间的过滤器及储液器。Each temperature heat pump system includes a filter and a liquid reservoir connected between the throttling device and the fin condenser.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009200520072U CN201364007Y (en) | 2009-03-02 | 2009-03-02 | Air source high-temperature heat pump dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009200520072U CN201364007Y (en) | 2009-03-02 | 2009-03-02 | Air source high-temperature heat pump dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201364007Y true CN201364007Y (en) | 2009-12-16 |
Family
ID=41474677
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2009200520072U Expired - Fee Related CN201364007Y (en) | 2009-03-02 | 2009-03-02 | Air source high-temperature heat pump dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201364007Y (en) |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102519139A (en) * | 2012-01-14 | 2012-06-27 | 湖南省浏阳市择明热工器材有限公司 | Air source heat pump system for providing direct high temperature air |
| CN103017503A (en) * | 2012-12-28 | 2013-04-03 | 广州德能热源设备有限公司 | Split type heat pump drying machine set |
| CN103307866A (en) * | 2013-06-05 | 2013-09-18 | 广州德能热源设备有限公司 | High-temperature heat pump drying unit for heat recovery and automatic dehumidification |
| CN104236287A (en) * | 2014-10-15 | 2014-12-24 | 广州德能热源设备有限公司 | Special heat pump drying unit for northern area in China |
| CN105004149A (en) * | 2015-06-24 | 2015-10-28 | 农业部规划设计研究院 | Intermittent cooling heat pump drying device and method |
| CN105671904A (en) * | 2014-12-08 | 2016-06-15 | Lg电子株式会社 | Condensing type clothes dryer and controling method for same |
| WO2017036280A1 (en) * | 2015-08-31 | 2017-03-09 | 青岛海尔滚筒洗衣机有限公司 | Vented heat pump dryer |
| CN106984142A (en) * | 2017-04-21 | 2017-07-28 | 深圳市捷晶能源科技有限公司 | A kind of removal moisture drying system and removal moisture drying method |
| CN107642925A (en) * | 2016-12-27 | 2018-01-30 | 中国科学院理化技术研究所 | Multistage heat pump drying and dehumidifying system with bypass pipeline |
| CN107830697A (en) * | 2017-11-30 | 2018-03-23 | 湖南埃瓦新能源科技有限公司 | Air energy heat pump drying system |
| CN108224915A (en) * | 2018-01-29 | 2018-06-29 | 南京航空航天大学 | A kind of superhigh temperature single system dual temperature area heat pump dryer system and application method |
| CN109876517A (en) * | 2019-02-22 | 2019-06-14 | 高云芝 | A kind of low temperature multistage filtering stream cuts unit |
| CN110068219A (en) * | 2019-03-15 | 2019-07-30 | 南京航空航天大学 | Analysis of Heat Pump Drying System and its working method with heat-storing device |
| CN110849098A (en) * | 2019-12-02 | 2020-02-28 | 佛山铠耐空调设备有限公司 | Two-stage heat exchange drying unit |
| CN113009947A (en) * | 2021-03-04 | 2021-06-22 | 河南省奥瑞环保科技股份有限公司 | Temperature control device and system for independent double-path zero-gas generator |
| CN114294943A (en) * | 2021-12-23 | 2022-04-08 | 珠海格力电器股份有限公司 | Heat pump drying assembly and heat pump drying system |
| CN114294942A (en) * | 2021-12-23 | 2022-04-08 | 珠海格力电器股份有限公司 | Heat pump drying system and control method thereof |
| CN116045626A (en) * | 2022-12-27 | 2023-05-02 | 安徽欧瑞达电器科技有限公司 | Directly-heated air source heat pump dryer |
-
2009
- 2009-03-02 CN CNU2009200520072U patent/CN201364007Y/en not_active Expired - Fee Related
Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102519139A (en) * | 2012-01-14 | 2012-06-27 | 湖南省浏阳市择明热工器材有限公司 | Air source heat pump system for providing direct high temperature air |
| CN102519139B (en) * | 2012-01-14 | 2014-11-19 | 湖南省浏阳市择明热工器材有限公司 | Air source heat pump system for providing direct high temperature air |
| CN103017503A (en) * | 2012-12-28 | 2013-04-03 | 广州德能热源设备有限公司 | Split type heat pump drying machine set |
| CN103307866A (en) * | 2013-06-05 | 2013-09-18 | 广州德能热源设备有限公司 | High-temperature heat pump drying unit for heat recovery and automatic dehumidification |
| CN104236287A (en) * | 2014-10-15 | 2014-12-24 | 广州德能热源设备有限公司 | Special heat pump drying unit for northern area in China |
| CN105671904A (en) * | 2014-12-08 | 2016-06-15 | Lg电子株式会社 | Condensing type clothes dryer and controling method for same |
| CN105004149A (en) * | 2015-06-24 | 2015-10-28 | 农业部规划设计研究院 | Intermittent cooling heat pump drying device and method |
| US10662573B2 (en) | 2015-08-31 | 2020-05-26 | Qingdao Haier Drum Washing Machine Co., Ltd. | Vented heat pump dryer |
| WO2017036280A1 (en) * | 2015-08-31 | 2017-03-09 | 青岛海尔滚筒洗衣机有限公司 | Vented heat pump dryer |
| CN107642925A (en) * | 2016-12-27 | 2018-01-30 | 中国科学院理化技术研究所 | Multistage heat pump drying and dehumidifying system with bypass pipeline |
| CN107642925B (en) * | 2016-12-27 | 2019-12-17 | 中国科学院理化技术研究所 | A multi-stage heat pump drying and dehumidification system with bypass pipeline |
| CN106984142A (en) * | 2017-04-21 | 2017-07-28 | 深圳市捷晶能源科技有限公司 | A kind of removal moisture drying system and removal moisture drying method |
| CN107830697A (en) * | 2017-11-30 | 2018-03-23 | 湖南埃瓦新能源科技有限公司 | Air energy heat pump drying system |
| CN108224915A (en) * | 2018-01-29 | 2018-06-29 | 南京航空航天大学 | A kind of superhigh temperature single system dual temperature area heat pump dryer system and application method |
| CN108224915B (en) * | 2018-01-29 | 2024-02-13 | 南京航空航天大学 | An ultra-high-temperature single-system dual-temperature zone heat pump dryer system and its use method |
| CN109876517A (en) * | 2019-02-22 | 2019-06-14 | 高云芝 | A kind of low temperature multistage filtering stream cuts unit |
| CN109876517B (en) * | 2019-02-22 | 2021-11-09 | 高云芝 | Low-temperature multistage filtering flow cutting unit |
| CN110068219A (en) * | 2019-03-15 | 2019-07-30 | 南京航空航天大学 | Analysis of Heat Pump Drying System and its working method with heat-storing device |
| CN110849098A (en) * | 2019-12-02 | 2020-02-28 | 佛山铠耐空调设备有限公司 | Two-stage heat exchange drying unit |
| CN113009947A (en) * | 2021-03-04 | 2021-06-22 | 河南省奥瑞环保科技股份有限公司 | Temperature control device and system for independent double-path zero-gas generator |
| CN114294943A (en) * | 2021-12-23 | 2022-04-08 | 珠海格力电器股份有限公司 | Heat pump drying assembly and heat pump drying system |
| CN114294942A (en) * | 2021-12-23 | 2022-04-08 | 珠海格力电器股份有限公司 | Heat pump drying system and control method thereof |
| CN114294942B (en) * | 2021-12-23 | 2022-12-20 | 珠海格力电器股份有限公司 | Heat pump drying system and control method thereof |
| CN116045626A (en) * | 2022-12-27 | 2023-05-02 | 安徽欧瑞达电器科技有限公司 | Directly-heated air source heat pump dryer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201364007Y (en) | Air source high-temperature heat pump dryer | |
| CN201364008Y (en) | Temperature-adjustable air source heat pump dehumidification drying equipment | |
| CN201364009Y (en) | Air source high-temperature heat pump dehumidification drying equipment | |
| CN106016989B (en) | A kind of tobacco drying apparatus | |
| CN104048447B (en) | A kind of refrigeration system that is core with Michel Knuysen compressor | |
| CN100538208C (en) | A dual temperature cold water/air cooler unit | |
| WO2015058462A1 (en) | Gas turbine intake air cooling device using waste heat as driving force | |
| CN101504247A (en) | Air source high-temperature heat pump dehumidification equipment | |
| CN101363682A (en) | Energy-conserving drying system | |
| CN205191964U (en) | Multistage condensation refrigerating plant | |
| CN116336795A (en) | An energy-efficient dehumidification method with internal energy transfer via a dual compression system | |
| CN201297829Y (en) | Energy-saving drying system | |
| CN203100029U (en) | Machine room air conditioner | |
| CN203284304U (en) | Device of drying sludge through solar energy-heat pump coupled liquid desiccating | |
| CN106288097B (en) | Trans critical cycle and the compound air treatment system of solution dehumidification system | |
| CN202792879U (en) | Total heat recovery type air source dehumidifying and drying integrated machine | |
| CN202942799U (en) | Structurally improved freezing drier | |
| CN205332764U (en) | Overlapping formula heat pump drying -machine | |
| CN206724662U (en) | A frequency conversion air source high temperature drying system | |
| CN108518886B (en) | White smoke-eliminating high-efficiency smoke hot water type lithium bromide absorption type cold and hot water unit | |
| CN206207964U (en) | A split-type high-efficiency heat recovery heat pump dryer | |
| CN212894416U (en) | Sludge drying heat pump system | |
| CN203980717U (en) | A kind of low-temperature air-cooling heat pump unit | |
| CN205225349U (en) | Condensing system of condensing formula screw rod expander | |
| CN205007848U (en) | Efficient organic waste gas processing system |
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: 20091216 Termination date: 20140302 |