CN202281480U - Greenhouse type double-heat-collection double-heat-insulation solar heat pump drying device - Google Patents

Greenhouse type double-heat-collection double-heat-insulation solar heat pump drying device Download PDF

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CN202281480U
CN202281480U CN2011203300955U CN201120330095U CN202281480U CN 202281480 U CN202281480 U CN 202281480U CN 2011203300955 U CN2011203300955 U CN 2011203300955U CN 201120330095 U CN201120330095 U CN 201120330095U CN 202281480 U CN202281480 U CN 202281480U
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heat pump
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刘刚
高祥虎
赵鑫
周添红
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Lanzhou Institute of Chemical Physics LICP of CAS
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    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • YGENERAL 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
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Abstract

本实用新型提供了一种利用太阳能对物料进行烘干的温室型双集热双保温太阳能热泵烘干装置,包括烘干单元、由自集热单元和外集热单元构成的太阳能集热单元、由热泵构成的辅助加热单元、冷凝除湿余热回收单元以及自动化监测控制单元。该烘干装置有效提高了太阳能的利用率,克服了太阳能的不稳定性,保证了烘干过程的连续性,并提高了烘干效率。干燥脱水过程干净、卫生、节能,可以有效克服农副产品等采用常规太阳暴晒和传统能源烘干造成的污染、脱色、变质和耗能的弊端。对于开发新能源、提高农副产品加工质量、促进循环经济和保护生态环境具有积极意义。

Figure 201120330095

The utility model provides a greenhouse type double heat collection double heat preservation solar heat pump drying device for drying materials by using solar energy, which comprises a drying unit, a solar heat collection unit composed of a self heat collection unit and an external heat collection unit, An auxiliary heating unit composed of a heat pump, a condensation and dehumidification waste heat recovery unit, and an automatic monitoring and control unit. The drying device effectively improves the utilization rate of solar energy, overcomes the instability of solar energy, ensures the continuity of the drying process, and improves the drying efficiency. The drying and dehydration process is clean, hygienic and energy-saving, and can effectively overcome the disadvantages of pollution, decolorization, deterioration and energy consumption caused by conventional sun exposure and traditional energy drying of agricultural and sideline products. It has positive significance for developing new energy, improving the processing quality of agricultural and sideline products, promoting circular economy and protecting the ecological environment.

Figure 201120330095

Description

温室型双集热双保温太阳能热泵烘干装置Greenhouse type double heat collection double heat preservation solar heat pump drying device

技术领域 technical field

本实用新型属于太阳能利用技术领域,涉及一种利用太阳能对物料进行烘干的温室型双集热双保温太阳能热泵烘干装置。 The utility model belongs to the technical field of solar energy utilization, and relates to a greenhouse type double heat collection and double heat preservation solar heat pump drying device for drying materials by using solar energy.

背景技术 Background technique

干燥作业在工农业生产的许多部门都有着广泛的应用,农副产品加工、食品工业、化工、医药等行业中,为了便于使用、运输和储存,许多产品都必须经过干燥加工,需要耗费巨大的常规能源。据有关资料报道,用在工农业生产干燥作业的能耗要占国民经济总能耗的5%--10%。通常情况下对物质的烘干方法大都采用燃煤、燃油、电力等常规能源提供热能,一方面是耗能大、烘干成本高、环境污染严重,更重要的是在当今常规能源短缺的情况下,不符合低碳经济、可持续发展的要求。利用丰富的太阳能是解决能源危机的重要途径之一。我国是个太阳能丰富的国家,有效利用太阳能对我国意义重大。近年发展起来的利用太阳能作为热源的烘干技术,普遍存在对太阳能的利用率低,效率不高,烘干周期长,投资大等问题。如专利:太阳能药材烘干装置(ZL200320105243.9)由预热室,烘干室,准备室等组成,用于海产品的太阳能烘干装置(ZL200820201812.2)由玻璃房,海产品烘干架,抽湿装置,吸热地板等组成,以上装置存在太阳能集热源单一,集热效果不理想,保温效果差,无法保证夜间或阴雨天连续烘干,余热回收利用程度不高等问题。专利:新型太阳能果品烘干室(200820105243.9)采用燃煤热风炉作为辅助热源,消耗常规能源,污染环境,不符合低碳经济的发展。因此,发展新型太阳能烘干技术,显得尤为迫切。 Drying operations are widely used in many sectors of industrial and agricultural production. In agricultural and sideline product processing, food industry, chemical industry, pharmaceutical and other industries, in order to facilitate use, transportation and storage, many products must be dried and processed, which requires a huge amount of conventional equipment. energy. According to relevant data reports, the energy consumption used in industrial and agricultural production drying operations will account for 5%-10% of the total energy consumption of the national economy. Under normal circumstances, most of the drying methods for materials use conventional energy such as coal, fuel oil, and electricity to provide heat energy. On the one hand, it consumes a lot of energy, costs high in drying, and causes serious environmental pollution. More importantly, in today's shortage of conventional energy It does not meet the requirements of low-carbon economy and sustainable development. Utilizing abundant solar energy is one of the important ways to solve the energy crisis. my country is a country rich in solar energy, and the effective use of solar energy is of great significance to our country. The drying technology developed in recent years using solar energy as a heat source generally has problems such as low utilization rate of solar energy, low efficiency, long drying cycle, and large investment. Such as the patent: solar medicinal material drying device (ZL200320105243.9) is composed of preheating room, drying room, preparation room, etc., solar drying device for seafood (ZL200820201812.2) is composed of glass room, seafood drying rack, Dehumidification device, heat-absorbing floor, etc., the above-mentioned devices have problems such as single solar heat collection source, unsatisfactory heat collection effect, poor heat preservation effect, unable to guarantee continuous drying at night or in rainy days, and low degree of waste heat recovery and utilization. Patent: A new type of solar fruit drying room (200820105243.9) uses a coal-fired hot air stove as an auxiliary heat source, which consumes conventional energy and pollutes the environment, which is not in line with the development of a low-carbon economy. Therefore, it is particularly urgent to develop new solar drying technology.

实用新型内容 Utility model content

本实用新型的目的在于克服现有技术存在的问题,提供一种太阳能利用率高、烘干速度快且能连续烘干的温室型双集热双保温太阳能热泵烘干装置。 The purpose of the utility model is to overcome the problems existing in the prior art, and to provide a greenhouse-type double heat collection and double heat preservation solar heat pump drying device with high utilization rate of solar energy, fast drying speed and continuous drying.

为实现上述目的,本实用新型采用如下技术方案: In order to achieve the above object, the utility model adopts the following technical solutions:

一种温室型双集热双保温太阳能热泵烘干装置,包括烘干单元与太阳能集热单元,其中,所述太阳能集热单元由自集热单元和外集热单元构成,所述自集热单元位于烘干单元上方,所述外集热单元位于烘干单元一侧, A greenhouse-type double heat collection and double heat preservation solar heat pump drying device, including a drying unit and a solar heat collection unit, wherein the solar heat collection unit is composed of a self heat collection unit and an external heat collection unit, and the self heat collection unit The unit is located above the drying unit, and the external heat collecting unit is located on one side of the drying unit.

所述烘干单元包括烘干室、吸光外壳及设在烘干室内的物料支架; The drying unit includes a drying chamber, a light-absorbing shell and a material support arranged in the drying chamber;

所述自集热单元包括透光板及太阳能温室,所述太阳能温室由透光板与烘干单元的吸光外壳围成; The self-heating unit includes a light-transmitting plate and a solar greenhouse, and the solar greenhouse is surrounded by a light-transmitting plate and a light-absorbing shell of a drying unit;

所述外集热单元包括太阳能集热器、水泵、保温水箱、循环泵及散热片,所述太阳能集热器、水泵及保温水箱通过水管连通并形成一闭合回路,所述循环泵、散热片及保温水箱通过水管连通并形成另一闭合回路,且所述散热片设在烘干单元的烘干室内。 The external heat collecting unit includes a solar heat collector, a water pump, a heat preservation water tank, a circulation pump and a cooling fin, and the solar heat collector, a water pump and a heat preservation water tank are connected through water pipes to form a closed loop. and the heat preservation water tank are connected through water pipes to form another closed circuit, and the heat sink is arranged in the drying chamber of the drying unit.

整个烘干装置采用狭长的温室型结构,故所述烘干室呈隧道式结构,方便了物料支架的推进和推出。 The entire drying device adopts a narrow and long greenhouse structure, so the drying chamber is in a tunnel structure, which facilitates the advancement and release of material supports.

所述外集热单元还包括控制阀,且所述控制阀连入于由太阳能集热器、水泵及保温水箱构成的闭合回路中,方便了对外集热单元的控制。 The external heat collecting unit also includes a control valve, and the control valve is connected in a closed circuit formed by the solar heat collector, the water pump and the heat preservation water tank, which facilitates the control of the external heat collecting unit.

所述保温水箱内的储热介质除水外,还可采用水与离子液体混合物、联苯混合物或导热油类等。所述太阳能集热器集热后将热量储存在保温水箱中的储热介质中,当遇到阴雨天或夜晚的时候,保温水箱可通过散热片对烘干单元继续加热,此时保温水箱即可作为烘干装置的一辅助热源。 In addition to water, the heat storage medium in the thermal insulation water tank may also use a mixture of water and ionic liquid, a biphenyl mixture, or heat-conducting oil. After the solar heat collector collects heat, it stores the heat in the heat storage medium in the heat preservation water tank. When encountering rainy days or nights, the heat preservation water tank can continue to heat the drying unit through the cooling fins. At this time, the heat preservation water tank is It can be used as an auxiliary heat source for the drying device.

所述透光板可由聚碳酸酯阳光板或双层玻璃板构成,所述吸光外壳由涂有太阳能选择性吸收涂料的铝板构成。为增加保温夜间保温效果,所述透光板顶部设有保温被。夜晚降温时可将保温被打开并覆盖于整个透光板的表面。所述烘干室的底部设置有保温地面,且所述保温地面由聚苯板构成。 The light-transmitting board can be made of polycarbonate solar board or double-layer glass board, and the light-absorbing shell is made of aluminum board coated with solar selective absorbing paint. In order to increase the thermal insulation effect at night, a thermal insulation quilt is provided on the top of the light-transmitting board. When the temperature drops at night, the insulation can be opened and covered on the surface of the entire light-transmitting panel. The bottom of the drying chamber is provided with a thermal insulation floor, and the thermal insulation floor is made of polystyrene board.

所述透光板、太阳能温室及保温被组成烘干装置的外保温层,所述吸光外壳与保温地面组成烘干装置的内保温层,它们在构成自集热单元与烘干单元的同时又一同构成本实用新型的双保温单元。 The light-transmitting board, solar greenhouse and thermal insulation are composed of the outer thermal insulation layer of the drying device, and the light-absorbing shell and the thermal insulation ground are composed of the inner thermal insulation layer of the drying device. Constitute the double insulation unit of the present utility model together.

所述温室型双集热双保温太阳能热泵烘干装置还包括辅助加热单元,所述辅助加热单元包括热泵及循环泵,所述热泵由热泵主机与热泵辅机组成,所述热泵主机、循环泵及保温水箱通过水管连通并形成闭合回路,所述热泵辅机位于烘干室内。所述热泵是以热泵主机周围空气及保温水箱中的储热介质为热源的双热源热泵,所述热泵主机吸收热源中的低品位热量,并将其转换为高品位热量,然后将热量传递到热泵辅机中,热泵辅机再通过热风的形式对烘干单元进行辅助加热。 The greenhouse type double heat collection and double heat preservation solar heat pump drying device also includes an auxiliary heating unit, the auxiliary heating unit includes a heat pump and a circulation pump, the heat pump is composed of a heat pump main unit and a heat pump auxiliary unit, the heat pump main unit, the circulation pump and the heat preservation water tank are connected through water pipes to form a closed circuit, and the heat pump auxiliary machine is located in the drying room. The heat pump is a dual heat source heat pump with the air around the heat pump host and the heat storage medium in the heat preservation water tank as the heat source. The heat pump host absorbs the low-grade heat in the heat source and converts it into high-grade heat, and then transfers the heat to the In the heat pump auxiliary machine, the heat pump auxiliary machine provides auxiliary heating to the drying unit in the form of hot air.

所述温室型双集热双保温太阳能热泵烘干装置还包括冷凝除湿余热回收单元,所述冷凝除湿余热回收单元包括排湿通道、变频排湿风机、冷凝室、热交换管道、冷凝导管及热风导管;所述冷凝室上设有循环工质入口及循环工质出口,所述热交换管道位于冷凝室内并与冷凝室底部连通,所述排湿通道一端位于烘干单元的烘干室内,另一端经变频排湿风机与热交换管道连通,所述冷凝导管从冷凝室底部伸出并与保温水箱连通,所述热风导管从冷凝室底部伸出并与烘干室连通。烘干过程中产生的湿热空气经排湿通道进入热交换管道进行冷凝,冷凝后的产生的水滴落至冷凝室底部并经冷凝导管进入保温水箱,除湿后的干热空气则经热风导管继续进入烘干室中。为提高冷凝效率,所述热交换管道在冷凝室内交错排布。所述冷凝除湿余热回收单元可及时将湿热空气进行冷凝并将除湿后的热风导入烘干室,最大程度地实现余热回收利用和物料的快速脱水。 The greenhouse-type double heat collection and double heat preservation solar heat pump drying device also includes a condensing dehumidification waste heat recovery unit, and the condensing dehumidification waste heat recovery unit includes a dehumidification passage, a frequency conversion dehumidification fan, a condensation chamber, a heat exchange pipe, a condensation conduit and a hot air Conduit; the condensing chamber is provided with a circulating working fluid inlet and a circulating working medium outlet, the heat exchange pipe is located in the condensing chamber and communicates with the bottom of the condensing chamber, one end of the dehumidification channel is located in the drying chamber of the drying unit, and the other One end communicates with the heat exchange pipe through the frequency conversion dehumidification blower, the condensation conduit protrudes from the bottom of the condensation chamber and communicates with the heat preservation water tank, and the hot air conduit protrudes from the bottom of the condensation chamber and communicates with the drying chamber. The hot and humid air generated during the drying process enters the heat exchange pipe through the dehumidification channel for condensation, and the condensed water drops to the bottom of the condensation chamber and enters the heat preservation water tank through the condensation pipe. The dry and hot air after dehumidification continues to enter through the hot air pipe in the drying room. In order to improve the condensation efficiency, the heat exchange pipes are arranged in a staggered manner in the condensation chamber. The condensing and dehumidifying waste heat recovery unit can condense the hot and humid air in time and guide the dehumidified hot air into the drying chamber, so as to maximize the recovery and utilization of waste heat and the rapid dehydration of materials.

所述冷凝室所采用的循环工质为水和乙醇的混合液或热泵主机工作时排出的冷风,且所述水和乙醇的体积配比为1:1~6。 The circulating working fluid used in the condensing chamber is a mixture of water and ethanol or the cold air discharged from the main unit of the heat pump, and the volume ratio of the water and ethanol is 1:1-6.

所述温室型双集热双保温太阳能热泵烘干装置还包括自动化监测控制单元,所述自动化监测控制单元由设在保温水箱上的温度传感器、设在烘干室内的温度传感器和湿度传感器、设在热泵主机旁边的温度传感器及总控制器组成。该自动化监测控制单元,可在线监测并记录烘干过程中的温度及湿度变化,实时掌握烘干情况,并通过设定的温度、湿度值控制变频排湿风机及辅助加热单元的工作,还可根据物料的特性设置分段烘干的工作模式,间隙排湿,优化了烘干工艺,减少了劳动力投入。 The greenhouse-type double-collector and double-insulation solar heat pump drying device also includes an automatic monitoring and control unit, the automatic monitoring and control unit is composed of a temperature sensor installed on the thermal insulation water tank, a temperature sensor and a humidity sensor installed in the drying room, and an automatic monitoring and control unit. It consists of a temperature sensor and a general controller next to the heat pump host. The automatic monitoring and control unit can monitor and record the temperature and humidity changes in the drying process online, grasp the drying situation in real time, and control the work of the frequency conversion dehumidification fan and auxiliary heating unit through the set temperature and humidity values. According to the characteristics of the material, the working mode of segmental drying is set, and the moisture is removed in the interval, which optimizes the drying process and reduces labor input.

综上,本实用新型的有益效果在于:采用双集热、双保温系统,有效提高了太阳能的利用率;采用保温水箱和双热源热泵作为辅助热源,可克服太阳能的不稳定性,保证了烘干过程的连续性并进一步提高了太阳能利用率;采用冷凝除湿余热回收单元可最大程度地实现热风继续利用,加速物料脱水,进一步减少能量损耗,提高烘干效率;采用自动化监测控制单元,可根据温度、湿度、太阳辐照、风速等的变化,对烘干过程作出实时调整,优化烘干工艺。 To sum up, the beneficial effects of the utility model are: the use of double heat collection and double heat preservation systems effectively improves the utilization rate of solar energy; the use of heat preservation water tanks and double heat source heat pumps as auxiliary heat sources can overcome the instability of solar energy and ensure the The continuity of the drying process further improves the utilization rate of solar energy; the use of condensation and dehumidification waste heat recovery unit can maximize the continuous utilization of hot air, accelerate the dehydration of materials, further reduce energy loss, and improve drying efficiency; the use of automatic monitoring control unit can be based on Changes in temperature, humidity, solar radiation, wind speed, etc. make real-time adjustments to the drying process to optimize the drying process.

此外,本实用新型主要使用太阳能提供热源,物料在密闭的烘干室内烘干脱水,适合于各种农副产品、海产品、中药材等物料的低温干燥脱水。而且所烘干的物料无论是从产品品质、色泽、有效成分等都在最大程度上进行了保留或保持。干燥脱水过程干净、卫生、节能,可以有效克服农副产品等采用常规太阳暴晒和传统能源烘干造成的污染、脱色、变质和耗能的弊端。对于开发新能源、提高农副产品加工质量、促进循环经济和保护生态环境具有积极意义。 In addition, the utility model mainly uses solar energy to provide a heat source, and the materials are dried and dehydrated in a closed drying room, which is suitable for low-temperature drying and dehydration of various agricultural and sideline products, seafood, Chinese medicinal materials and other materials. Moreover, the dried materials are retained or maintained to the greatest extent in terms of product quality, color, and active ingredients. The drying and dehydration process is clean, hygienic and energy-saving, and can effectively overcome the disadvantages of pollution, decolorization, deterioration and energy consumption caused by conventional sun exposure and traditional energy drying of agricultural and sideline products. It has positive significance for developing new energy, improving the processing quality of agricultural and sideline products, promoting circular economy and protecting the ecological environment.

附图说明 Description of drawings

图1为本实用新型的结构示意图; Fig. 1 is the structural representation of the utility model;

图2为本实用新型冷凝室的剖面示意图。 Fig. 2 is a schematic cross-sectional view of the condensation chamber of the present invention.

具体实施方式 Detailed ways

下面结合附图对本实用新型进行进一步的说明。 Below in conjunction with accompanying drawing, the utility model is further described.

如图1、图2所示,一种温室型双集热双保温太阳能热泵烘干装置,包括烘干单元、太阳能集热单元、辅助加热单元、冷凝除湿余热回收单元及自动化监测控制单元,所述太阳能集热单元由自集热单元和外集热单元构成,所述自集热单元位于烘干单元上方,所述外集热单元位于烘干单元一侧;所述烘干单元由烘干室14、吸光外壳12及设在烘干室14内的物料支架9组成,且所述烘干室14的底部设置有由聚苯板构成的保温地面11;所述自集热单元由透光板13及太阳能温室15组成,所述太阳能温室15由透光板13与烘干单元的吸光外壳12围成;所述透光板13由聚碳酸酯阳光板或双层玻璃板构成,所述吸光外壳12由涂有太阳能选择性吸收涂料的铝板构成,所述透光板顶部还设有保温被17;所述外集热单元由太阳能集热器1、水泵3、控制阀2、保温水箱4、循环泵6及散热片10组成,所述太阳能集热器1、水泵3、控制阀2及保温水箱4通过水管31连通并形成一闭合回路,所述循环泵6、散热片10及保温水箱4通过水管33连通并形成另一闭合回路,且所述散热片10设在烘干单元的烘干室14内,所述保温水箱4内的储热介质为水。所述辅助加热单元由热泵及循环泵19组成,所述热泵由热泵主机7及热泵辅机8构成,所述热泵主机7、循环泵19及保温水箱4通过水管32连通并形成闭合回路,所述热泵辅机8位于烘干室内。 As shown in Figure 1 and Figure 2, a greenhouse-type double-collection and double-insulation solar heat pump drying device includes a drying unit, a solar heat collection unit, an auxiliary heating unit, a condensing and dehumidifying waste heat recovery unit, and an automatic monitoring and control unit. The solar heat collecting unit is composed of a self heat collecting unit and an external heat collecting unit, the self heat collecting unit is located above the drying unit, and the external heat collecting unit is located on one side of the drying unit; the drying unit is composed of a drying unit Chamber 14, light-absorbing shell 12 and material support 9 arranged in the drying chamber 14, and the bottom of the drying chamber 14 is provided with a thermal insulation floor 11 made of polystyrene board; the self-heating unit is composed of light-transmitting Plate 13 and solar greenhouse 15, the solar greenhouse 15 is surrounded by the light-absorbing shell 12 of the light-transmitting plate 13 and drying unit; the light-transmitting plate 13 is made of polycarbonate solar panels or double-layer glass panels, the The light-absorbing shell 12 is composed of an aluminum plate coated with a solar selective absorbing paint, and the top of the light-transmitting plate is also provided with a thermal insulation quilt 17; the external heat collection unit is composed of a solar heat collector 1, a water pump 3, a control valve 2, and a thermal insulation water tank. 4. Circulating pump 6 and heat sink 10 are composed. The solar heat collector 1, water pump 3, control valve 2 and heat preservation water tank 4 are connected through water pipe 31 to form a closed loop. The circulation pump 6, heat sink 10 and heat preservation The water tank 4 communicates with the water pipe 33 to form another closed circuit, and the heat sink 10 is arranged in the drying chamber 14 of the drying unit, and the heat storage medium in the heat preservation water tank 4 is water. The auxiliary heating unit is composed of a heat pump and a circulation pump 19. The heat pump is composed of a heat pump main unit 7 and a heat pump auxiliary unit 8. The heat pump main unit 7, the circulation pump 19 and the heat preservation water tank 4 are connected through a water pipe 32 to form a closed loop. The heat pump auxiliary machine 8 is located in the drying chamber.

所述冷凝除湿余热回收单元由排湿通道16、变频排湿风机18、冷凝室22、热交换管道21、冷凝导管25及热风导管26组成;所述冷凝室22上设有循环工质入口23及循环工质出口20,所述热交换管道21位于冷凝室22内并与冷凝室22底部连通,且所述热交换管道21在冷凝室22内交错排布,所述排湿通道16一端位于烘干单元的烘干室14内,另一端经变频排湿风机18与热交换管道21连通,所述冷凝导管25从冷凝室22底部伸出并与保温水箱4连通,所述热风导管26从冷凝室22底部伸出并与烘干室14连通。所述冷凝除湿余热回收单元采用乙醇与水的混合液或热泵主机工作时排出的冷风作为循环工质,选用乙醇与水的混合液时,所述水和乙醇的体积配比为1:3。 The condensation and dehumidification waste heat recovery unit is composed of a dehumidification passage 16, a frequency conversion dehumidification fan 18, a condensation chamber 22, a heat exchange pipe 21, a condensation conduit 25 and a hot air conduit 26; the condensation chamber 22 is provided with a circulating working medium inlet 23 and the circulating working medium outlet 20, the heat exchange pipes 21 are located in the condensation chamber 22 and communicate with the bottom of the condensation chamber 22, and the heat exchange pipes 21 are arranged in a staggered manner in the condensation chamber 22, and one end of the dehumidification channel 16 is located at In the drying chamber 14 of the drying unit, the other end communicates with the heat exchange pipe 21 through the frequency conversion dehumidification blower 18. The condensation conduit 25 protrudes from the bottom of the condensation chamber 22 and communicates with the heat preservation water tank 4. The hot air conduit 26 connects with the The bottom of the condensation chamber 22 protrudes and communicates with the drying chamber 14 . The condensing and dehumidifying waste heat recovery unit uses the mixture of ethanol and water or the cold air discharged from the heat pump host as the circulating working medium. When the mixture of ethanol and water is used, the volume ratio of water and ethanol is 1:3.

所述温室型双集热双保温太阳能热泵烘干装置还包括自动化监测控制单元,所述自动化监测控制单元由设在保温水箱4上的温度传感器5、设在烘干室14内的温度传感器27及湿度传感器28、设在热泵主机7旁边的温度传感器24及总控制器29组成。  The greenhouse-type double-collector double-insulation solar heat pump drying device also includes an automatic monitoring control unit, the automatic monitoring control unit consists of a temperature sensor 5 located on the thermal insulation water tank 4 and a temperature sensor 27 located in the drying chamber 14. And humidity sensor 28, the temperature sensor 24 that is located at the side of heat pump main frame 7 and general controller 29 to form. the

当晴天日照正常时,太阳光穿过由聚碳酸酯阳光板或玻璃板构成的透光板13及太阳能温室15,到达由涂有太阳能选择性吸收涂料的铝板构成的吸光外壳12,实现对烘干室14的直接加热,且透光板13及太阳能温室15还构成烘干单元的外保温层。此外,外集热单元的太阳能集热器1通过水循环对保温水箱4中的水进行持续加热,保温水箱4又通过与散热片10之间的水循环对烘干室14同时进行加热。将待烘干物料30置于底部设有滑轮的物料支架9上,然后将物料支架9推入烘干室14内进行烘干。随着烘干过程的进行,整个烘干室14内的相对湿度上升,此时,根据不同的物料特性,提前在自动化监测控制单元中设定一控制变频排湿风机18工作的相对湿度值,当湿度传感器28监测到烘干室14内的湿度值高于设定值时,变频排湿风机18自动开启,从而进行冷凝除湿作业;当烘房内相对湿度低于设定值时,变频排湿风机关闭。变频排湿风机18工作时,烘干室14内的湿热空气经排湿通道16被抽离到冷凝室22内的热交换管道21中,湿热空气经过热交换管道21时与冷凝室22内的循环工质发生热交换,此时,湿热空气中的水汽冷凝下来,通过冷凝水导管25排入保温水箱4中。经过冷凝后的干热空气通过热风导管26又继续进入烘干室22内。 When the sunshine is normal on a sunny day, the sunlight passes through the light-transmitting panel 13 and the solar greenhouse 15 made of polycarbonate solar panels or glass panels, and reaches the light-absorbing shell 12 made of aluminum panels coated with solar selective absorption coatings to realize the anti-drying process. The direct heating of the drying chamber 14, and the light-transmitting plate 13 and the solar greenhouse 15 also constitute the outer insulation layer of the drying unit. In addition, the solar heat collector 1 of the external heat collecting unit continuously heats the water in the thermal insulation water tank 4 through water circulation, and the thermal insulation water tank 4 heats the drying chamber 14 through the water circulation between the cooling fins 10 at the same time. The material 30 to be dried is placed on the material support 9 provided with pulleys at the bottom, and then the material support 9 is pushed into the drying chamber 14 for drying. As the drying process progresses, the relative humidity in the entire drying chamber 14 rises. At this time, according to different material characteristics, a relative humidity value that controls the work of the frequency conversion dehumidification blower 18 is set in advance in the automatic monitoring control unit. When the humidity sensor 28 detects that the humidity in the drying chamber 14 is higher than the set value, the frequency conversion dehumidification blower 18 is automatically turned on to carry out the condensation dehumidification operation; when the relative humidity in the drying room is lower than the set value, the frequency conversion The humidifier is off. When the frequency conversion dehumidification blower 18 is working, the hot and humid air in the drying chamber 14 is extracted into the heat exchange pipe 21 in the condensation chamber 22 through the dehumidification passage 16, and the hot and humid air is mixed with the heat exchange pipe 21 in the condensation chamber 22 when passing through the heat exchange pipe 21. The circulating working fluid undergoes heat exchange. At this time, the water vapor in the hot and humid air is condensed and discharged into the heat preservation water tank 4 through the condensed water conduit 25 . The condensed hot and dry air continues to enter the drying chamber 22 through the hot air duct 26 .

另外,在自动化监测控制单元中设定一物料所需最佳烘干温度T-1,随着烘干过程的进行,当太阳光提供的能量足以使烘干室14内的温度达到或超过设定的最佳烘干温度T-1时,热泵不启动,由自集热单元及外集热单元为烘干单元提供热源,否则热泵同时启动。此外,由于热泵主机7周围空气温度过高时,易造成热泵效率不高的问题,因此在自动化监测控制单元中再设定一热泵最高工作温度T-2,当温度传感器24监测到热泵主机7所处的环境温度超过设定温度值T-2时,热泵主机7与热泵辅机8亦停止工作。 In addition, the optimal drying temperature T- 1 required by a material is set in the automatic monitoring control unit. As the drying process proceeds, when the energy provided by sunlight is sufficient to make the temperature in the drying chamber 14 reach or exceed the set When the optimum drying temperature T- 1 is set, the heat pump does not start, and the self-collecting unit and the external heat-collecting unit provide heat sources for the drying unit, otherwise the heat pump starts at the same time. In addition, since the temperature of the air around the heat pump host 7 is too high, it is easy to cause the problem of low efficiency of the heat pump. Therefore, in the automatic monitoring control unit, a maximum heat pump operating temperature T- 2 is set. When the temperature sensor 24 detects that the heat pump host 7 When the ambient temperature exceeds the set temperature value T- 2 , the heat pump main machine 7 and the heat pump auxiliary machine 8 also stop working.

当阴雨天或夜晚没有足够日照的时候,且当温度传感器27监测到烘干室14内的温度低于最佳烘干温度T-1时,热泵自动开启,并以热泵主机7周围空气及保温水箱4中的水作为热源。在自动化监测控制单元中再设定一循环泵19的最高工作温度T-3,当温度传感器5监测到保温水箱4的温度超过循环泵19的最高工作温度T-3时,循环泵19不启动并停止给热泵主机7供水,此时热泵主机7只以周围空气作为热源。在天阴或夜间的时候,保温水箱4同时也作为烘干室14的辅助热源,将储存的热量通过散热片10为烘干室14提供热量。另外,夜晚降温的时候可将大棚保温被17打开覆盖于整个透光板13表面进行保温。 When there is not enough sunlight in rainy days or at night, and when the temperature sensor 27 detects that the temperature in the drying chamber 14 is lower than the optimal drying temperature T- 1 , the heat pump is automatically turned on, and the surrounding air and heat preservation of the heat pump host 7 The water in the water tank 4 is used as heat source. In the automatic monitoring control unit, set a maximum operating temperature T- 3 of the circulating pump 19, when the temperature sensor 5 monitors the temperature of the thermal insulation tank 4 exceeding the maximum operating temperature T- 3 of the circulating pump 19, the circulating pump 19 does not start And stop the water supply to the heat pump host 7, and now the heat pump host 7 only uses the surrounding air as a heat source. When the sky is cloudy or at night, the thermal water tank 4 is also used as an auxiliary heat source for the drying chamber 14, and the stored heat is provided to the drying chamber 14 through the cooling fins 10. In addition, when the temperature is cooling down at night, the greenhouse heat preservation quilt 17 can be opened and covered on the entire surface of the light-transmitting plate 13 for heat preservation.

在所述自动化监测控制单元中,各温度传感器及湿度传感器将所测温度值及湿度值传入总控制器29中,再由总控制器29对变频排湿风机18、热泵及循环泵19发出工作指令,其设置由本领域技术人员根据现有传感技术及上述功能描述即可实现,故此处不再详述。所述自动化监测控制单元还可增加功能模块以在线监测记录太阳瞬时辐照及风速的变化,然后通过设定的温度、湿度值控制变频排湿风机18、循环泵19及热泵的工作,并根据物料的不同设置分段烘干的工作模式,进行间隙除湿。 In the automatic monitoring and control unit, each temperature sensor and humidity sensor transmit the measured temperature value and humidity value into the total controller 29, and then the total controller 29 sends out the frequency conversion dehumidification fan 18, heat pump and circulation pump 19. The setting of the work order can be realized by those skilled in the art according to the existing sensing technology and the above-mentioned function description, so it will not be described in detail here. The automatic monitoring and control unit can also add functional modules to monitor and record changes in the instantaneous solar radiation and wind speed online, and then control the frequency conversion dehumidification blower 18, the circulation pump 19 and the work of the heat pump through the set temperature and humidity values, and according to the The working mode of segmental drying for different settings of materials is used for interstitial dehumidification.

下面以2011.7.19—7.20日烘干过程为例进行说明: The following is an example of the drying process from July 19 to July 20, 2011:

时间:2011.7.19—7.20    天气:多云转晴      温度:18--34oC    Time: 2011.7.19—7.20 Weather: cloudy to sunny Temperature: 18--34 o C

地点:甘肃兰州  北纬36°03′  东经103°49′ Location: Lanzhou, Gansu, 36°03′N, 103°49′E

温室朝向:正南       烘干装置整体体积为20m3    烘干室体积为15m3 Greenhouse orientation: due south, the overall volume of the drying device is 20m 3 and the volume of the drying room is 15m 3

冷凝室中循环工质的体积为8L      The volume of circulating working medium in the condensation chamber is 8L

循环工质为水与乙醇的混合液,体积比为1:3。 The circulating working fluid is a mixture of water and ethanol with a volume ratio of 1:3.

试验材料于2011年5月采自甘肃庆阳地区新鲜红富士苹果等外果、残次果,可溶性固形物含量20.5%~24.1%,硬度8.7 ㎏/㎡~10.1㎏/㎡,含水率75%~80%。 The test materials were collected in May 2011 from fresh red Fuji apples and defective fruits in Qingyang, Gansu, with soluble solid content of 20.5%-24.1%, hardness of 8.7㎏/㎡~10.1㎏/㎡, moisture content of 75% ~80%.

工艺流程:苹果→清洗→去皮、去芯、切片→护色→沥水→上料→脱水→脱水苹果片。 Process flow: apple → cleaning → peeling, core removal, slicing → color protection → draining → feeding → dehydration → dehydrated apple slices.

试验方法:在每个物料支架上平铺10㎏苹果片进行脱水试验,直至果片含水率降为15%左右。实验过程中在自动化监测控制单元中设置相对湿度值为20%,10%,5%,自动控制变频排湿风机18的开关,从而达到分段排湿。在自动化监测控制单元中设置最佳烘干温度值T-1为45oC,当太阳能提供的热量不足以达到苹果最佳烘干温度45oC时,热泵主机7和热泵辅机8自动开启,当烘干室14内温度超过45oC时,热泵主机7和热泵辅机8自动关机。当天下午18:00的时候,打开保温被17将其覆盖于透光板13表面。夜间热泵、保温水箱4、散热片10作为辅助热源开始工作。 Test method: Spread 10kg of apple slices on each material support for dehydration test until the moisture content of the fruit slices drops to about 15%. During the experiment, the relative humidity values were set to 20%, 10%, and 5% in the automatic monitoring and control unit, and the switch of the frequency conversion dehumidification blower 18 was automatically controlled to achieve segmental dehumidification. Set the optimal drying temperature value T- 1 in the automatic monitoring control unit to 45 o C, when the heat provided by the solar energy is not enough to reach the optimum drying temperature of apples at 45 o C, the heat pump main unit 7 and heat pump auxiliary unit 8 are automatically turned on , when the temperature in the drying chamber 14 exceeds 45 o C, the heat pump main machine 7 and the heat pump auxiliary machine 8 are automatically shut down. At 18:00 in the afternoon of the same day, open the thermal insulation quilt 17 and cover it on the surface of the light-transmitting plate 13 . Night heat pump, heat preservation water tank 4, cooling fin 10 start working as auxiliary heat source.

实验结果:50kg苹果含水率从80%降到15%所需的烘干总时间为20小时,烘干后的苹果片色泽好,干湿度均匀,无污染。 Experimental results: The total drying time required to reduce the moisture content of 50kg apples from 80% to 15% is 20 hours. The dried apple slices have good color, uniform dry humidity and no pollution.

Claims (8)

1. two insulation solar heat heat pump drying units of the two thermal-arrests of a greenhouse type; Comprise drying unit and solar energy heating unit; It is characterized in that: said solar energy heating unit by from the thermal-arrest unit with outside the thermal-arrest unit constitute; The said drying unit top that is positioned at from the thermal-arrest unit, said outer thermal-arrest unit is positioned at drying unit one side
Said drying unit comprises drying chamber (14), extinction shell (12) and is located at the Material and article holding frame (9) in the drying chamber (14);
Said light-passing board (13) and the solar energy greenhouse (15) of comprising from the thermal-arrest unit, said solar energy greenhouse (15) is surrounded by the extinction shell (12) of light-passing board (13) with drying unit;
Said outer thermal-arrest unit comprises solar thermal collector (1), water pump (3), attemperater (4), circulating pump (6) and fin (10); Said solar thermal collector (1), water pump (3) and attemperater (4) are communicated with through water pipe (31) and form a closed-loop path; Said circulating pump (6), fin (10) and attemperater (4) are communicated with through water pipe (33) and form another closed-loop path, and said fin (10) is located in the drying chamber (14) of drying unit.
2. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 1; It is characterized in that: also comprise the assistant heating unit; Said assistant heating unit comprises heat pump and circulating pump (19); Said heat pump is made up of heat pump main frame (7) and heat pump subsidiary engine (8), and said heat pump main frame (7), circulating pump (19) and attemperater (4) are communicated with through water pipe (32) and form the closed-loop path, and said heat pump subsidiary engine (8) is positioned at drying chamber (14).
3. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 1 and 2; It is characterized in that: also comprise dehumidification by condensation waste heat recovery unit, said dehumidification by condensation waste heat recovery unit comprises hydrofuge passage (16), frequency conversion wet-emitting blower (18), condensation chamber (22), heat exchanging pipe (21), condensation pipe (25) and hot-blast conduit (26); Said condensation chamber (22) is provided with cycle fluid inlet (23) and cycle fluid outlet (20); Said heat exchanging pipe (21) is positioned at condensation chamber (22) and is communicated with condensation chamber (22) bottom; Said hydrofuge passage (16) one ends are positioned at the drying chamber (14) of drying unit; The other end is communicated with heat exchanging pipe (21) through frequency conversion wet-emitting blower (18); Said condensation pipe (25) stretches out from condensation chamber (22) bottom and is communicated with attemperater (4), and said hot-blast conduit (26) stretches out from condensation chamber (22) bottom and is communicated with drying chamber (14).
4. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 1, it is characterized in that: said light-passing board (13) top is provided with insulation quilt (17).
5. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 1, it is characterized in that: the bottom of said drying chamber (14) is provided with thermal-insulation floor (11).
6. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 1; It is characterized in that: said outer thermal-arrest unit also comprises control valve (2), and said control valve (2) is connected in the closed-loop path that is made up of solar thermal collector (1), water pump (3) and attemperater (4).
7. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 3, it is characterized in that: said heat exchanging pipe (21) is staggered arranging in condensation chamber (22).
8. the two insulation solar heat heat pump drying units of the two thermal-arrests of greenhouse type according to claim 2; It is characterized in that: it also comprises the automatic monitoring control module, said automatic monitoring control module by be located at temperature sensor (5) on the attemperater (4), be located at temperature sensor (27) and humidity sensor (28) in the drying chamber (14), the temperature sensor (24) and the master controller (29) that are located at heat pump main frame (7) next door form.
CN2011203300955U 2011-09-05 2011-09-05 Greenhouse type double-heat-collection double-heat-insulation solar heat pump drying device Expired - Fee Related CN202281480U (en)

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CN102393136A (en) * 2011-09-05 2012-03-28 中国科学院兰州化学物理研究所 Greenhouse-type double-heat-collecting double-heat-preserving solar-energy heat-pump drying device
CN102809267A (en) * 2012-07-16 2012-12-05 王福善 Material drying device
CN102853647A (en) * 2012-10-16 2013-01-02 罗二元 Oast dehumidifying and waste heat recovering system
CN104776693A (en) * 2015-03-20 2015-07-15 殷玉华 Intelligent drying device for traditional Chinese medicinal materials
CN105258477A (en) * 2015-11-19 2016-01-20 东莞市风火轮热能科技有限公司 Medicine sun-curing device based on double-heat collection principle and sun-curing process thereof
CN106288754A (en) * 2016-09-30 2017-01-04 中国科学院广州能源研究所 One is provided multiple forms of energy to complement each other drying unit
CN107883703A (en) * 2017-11-02 2018-04-06 中国水产科学研究院渔业机械仪器研究所 Multifunction fishing band drying device
CN114705000A (en) * 2021-06-30 2022-07-05 海南大学 A solar-microwave-vacuum freezing method and device for combined drying of sea cucumbers

Cited By (10)

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CN102393136A (en) * 2011-09-05 2012-03-28 中国科学院兰州化学物理研究所 Greenhouse-type double-heat-collecting double-heat-preserving solar-energy heat-pump drying device
CN102393136B (en) * 2011-09-05 2014-08-13 中国科学院兰州化学物理研究所 Method for drying materials by using greenhouse-type double-heat-collecting double-heat-preserving solar-energy heat-pump drying device
CN102809267A (en) * 2012-07-16 2012-12-05 王福善 Material drying device
CN102809267B (en) * 2012-07-16 2015-02-25 王福善 Material drying device
CN102853647A (en) * 2012-10-16 2013-01-02 罗二元 Oast dehumidifying and waste heat recovering system
CN104776693A (en) * 2015-03-20 2015-07-15 殷玉华 Intelligent drying device for traditional Chinese medicinal materials
CN105258477A (en) * 2015-11-19 2016-01-20 东莞市风火轮热能科技有限公司 Medicine sun-curing device based on double-heat collection principle and sun-curing process thereof
CN106288754A (en) * 2016-09-30 2017-01-04 中国科学院广州能源研究所 One is provided multiple forms of energy to complement each other drying unit
CN107883703A (en) * 2017-11-02 2018-04-06 中国水产科学研究院渔业机械仪器研究所 Multifunction fishing band drying device
CN114705000A (en) * 2021-06-30 2022-07-05 海南大学 A solar-microwave-vacuum freezing method and device for combined drying of sea cucumbers

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