CN107289767A - Tunnel type multistage series heat pump drying system - Google Patents

Tunnel type multistage series heat pump drying system Download PDF

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Publication number
CN107289767A
CN107289767A CN201710487847.0A CN201710487847A CN107289767A CN 107289767 A CN107289767 A CN 107289767A CN 201710487847 A CN201710487847 A CN 201710487847A CN 107289767 A CN107289767 A CN 107289767A
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heat pump
chamber
tunnel
drying
drying system
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苑亚
杨鲁伟
张振涛
张冲
魏娟
毛祥
肖波
谢诚
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Technical Institute of Physics and Chemistry of CAS
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Technical Institute of Physics and Chemistry of CAS
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B15/00Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
    • F26B15/10Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
    • F26B15/12Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined
    • F26B15/16Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined the objects or batches of materials being carried by wheeled trucks
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/001Drying-air generating units, e.g. movable, independent of drying enclosure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/04Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • F26B21/08Humidity
    • F26B21/086Humidity by condensing the moisture in the drying medium, which may be recycled, e.g. using a heat pump cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • F26B21/10Temperature; Pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • F26B21/12Velocity of flow; Quantity of flow, e.g. by varying fan speed, by modifying cross flow area
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/06Chambers, containers, or receptacles
    • F26B25/063Movable containers or receptacles, e.g. carts, trolleys, pallet-boxes
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

本发明涉及热泵干燥技术领域,尤其涉及一种隧道式多级串联热泵干燥系统。该系统包括太阳能系统、热泵循环系统和干燥系统,所述干燥系统包括隧道式干燥室,所述太阳能系统为太阳能新风系统,所述太阳能系统包括新风加热室,所述热泵循环系统包括多个热泵系统,各所述热泵系统的冷凝器依次串联构成多级加热室,各所述热泵系统的蒸发器依次串联构成多级除湿室,在所述多级加热室与所述多级除湿室之间设有混合室。本发明能够有效回收废热,降低系统的总能耗,采用多级除湿能够有效地除去干燥空气中的水分,采用多级加热满足了送回风温差较大情况,提高了压缩机效率,有效提高了除湿效率。

The invention relates to the technical field of heat pump drying, in particular to a tunnel type multi-stage series heat pump drying system. The system includes a solar system, a heat pump circulation system and a drying system, the drying system includes a tunnel drying room, the solar system is a solar fresh air system, the solar system includes a fresh air heating chamber, and the heat pump circulation system includes a plurality of heat pumps system, the condensers of each heat pump system are connected in series to form a multi-stage heating chamber, the evaporators of each heat pump system are connected in series to form a multi-stage dehumidification chamber, and between the multi-stage heating chamber and the multi-stage dehumidification chamber With mixing chamber. The invention can effectively recycle waste heat, reduce the total energy consumption of the system, adopt multi-stage dehumidification to effectively remove moisture in the dry air, and adopt multi-stage heating to meet the large temperature difference between the return air and improve the efficiency of the compressor. dehumidification efficiency.

Description

一种隧道式多级串联热泵干燥系统A tunnel type multi-stage series heat pump drying system

技术领域technical field

本发明涉及热泵干燥技术领域,尤其涉及一种隧道式多级串联热泵干燥系统。The invention relates to the technical field of heat pump drying, in particular to a tunnel type multi-stage series heat pump drying system.

背景技术Background technique

热泵系统在干燥领域的应用可以有效回收废热,降低干燥能耗。然而现有的热泵系统,在低温环境下性能较低,甚至不能够正常运行,且供回温差较大时,现有的单级热泵系统难以满足要求。The application of the heat pump system in the drying field can effectively recover waste heat and reduce drying energy consumption. However, the performance of the existing heat pump system is low in a low temperature environment, and even cannot operate normally, and when the temperature difference between supply and return is large, the existing single-stage heat pump system cannot meet the requirements.

发明内容Contents of the invention

(一)要解决的技术问题(1) Technical problems to be solved

本发明的目的是提供一种隧道式多级串联热泵干燥系统,解决现有热泵系统在低温环境下不能够正常运行,性能较低,供回温差较大时,单级热泵系统难以满足要求的问题。The purpose of the present invention is to provide a tunnel-type multi-stage series heat pump drying system to solve the problem that the existing heat pump system cannot operate normally in a low temperature environment, the performance is low, and the temperature difference between supply and return is large, and the single-stage heat pump system is difficult to meet the requirements. question.

(二)技术方案(2) Technical solution

为了解决上述技术问题,本发明提供了一种隧道式多级串联热泵干燥系统,至少包括从上到下依次设置的太阳能系统、热泵循环系统和干燥系统;In order to solve the above technical problems, the present invention provides a tunnel-type multi-stage series heat pump drying system, which at least includes a solar system, a heat pump circulation system and a drying system arranged sequentially from top to bottom;

所述干燥系统包括隧道式干燥室;The drying system includes a tunnel drying chamber;

所述太阳能系统为太阳能新风系统,所述太阳能新风系统包括新风加热室;The solar energy system is a solar fresh air system, and the solar fresh air system includes a fresh air heating chamber;

所述热泵循环系统包括多个热泵系统,各所述热泵系统的冷凝器依次串联构成多级加热室,各所述热泵系统的蒸发器依次串联构成多级除湿室,在所述多级加热室与所述多级除湿室之间设有混合室,所述混合室的左右两侧分别设有排风道;The heat pump circulation system includes a plurality of heat pump systems, the condensers of each heat pump system are connected in series to form a multi-stage heating chamber, the evaporators of each heat pump system are connected in series to form a multi-stage dehumidification chamber, and in the multi-stage heating chamber A mixing chamber is provided between the multi-stage dehumidification chamber, and exhaust ducts are respectively provided on the left and right sides of the mixing chamber;

所述的多级加热室、混合室和多级除湿室从前到后依次连通;所述多级加热室通过送风口与所述隧道式干燥室相连通,所述多级除湿室通过回风口与所述隧道式干燥室相连通;所述新风加热室通过热风进口与所述混合室相连通,所述混合室通过排风口与所述排风道相连通。The multi-stage heating chamber, the mixing chamber and the multi-stage dehumidification chamber are connected sequentially from front to back; The tunnel-type drying chamber is connected; the fresh air heating chamber is connected to the mixing chamber through a hot air inlet, and the mixing chamber is connected to the exhaust duct through an air outlet.

进一步地,所述太阳能新风系统包括透光隔热板、吸附结构和支撑板,其中所述支撑板设置在所述吸附结构上,所述透光隔热板设置在所述支撑板上,所述的透光隔热板、吸附结构和支撑板合围构成所述新风加热室。Further, the solar fresh air system includes a light-transmitting heat insulation board, an adsorption structure and a support plate, wherein the support plate is arranged on the adsorption structure, and the light-transmitting heat insulation board is arranged on the support board, so The fresh air heating chamber is surrounded by the above-mentioned light-transmitting heat insulation board, the adsorption structure and the support board.

具体地,所述吸附结构的内部设置蓄热材料,所述吸附结构的外表面设置太阳能吸附材料。Specifically, heat storage materials are arranged inside the adsorption structure, and solar energy adsorption materials are arranged on the outer surface of the adsorption structure.

具体地,所述支撑板上设有新风进口。Specifically, a fresh air inlet is provided on the support plate.

进一步地,所述隧道式干燥室设有进料口和出料口,其中所述出料口设置在所述隧道式干燥室上对应所述送风口的一侧,所述进料口设置在所述隧道式干燥室上对应所述回风口的一侧。Further, the tunnel-type drying chamber is provided with a material inlet and a material outlet, wherein the material outlet is set on the side of the tunnel-type drying room corresponding to the air supply port, and the material inlet is set at The side of the tunnel drying chamber corresponding to the air return port.

进一步地,在所述多级除湿室中设有储水盘,所述储水盘设置在所述蒸发器的底部,所述储水盘上设有引出管道。Further, a water storage tray is provided in the multi-stage dehumidification chamber, the water storage tray is arranged at the bottom of the evaporator, and an outlet pipe is provided on the water storage tray.

具体地,在所述多级加热室的送风口处设有主风机,所述主风机采用变频风机。Specifically, a main fan is provided at the air outlet of the multi-stage heating chamber, and the main fan is a variable frequency fan.

具体地,所述热风进口上设有新风阀,所述排风口上设有排风阀。Specifically, the hot air inlet is provided with a fresh air valve, and the air outlet is provided with an exhaust valve.

具体地,所述隧道式干燥室中设有物料推车,所述物料推车的移动方向与所述隧道式干燥室中干燥热风的流动方向相反。Specifically, a material cart is provided in the tunnel-type drying chamber, and the moving direction of the material cart is opposite to the flow direction of the drying hot air in the tunnel-type drying chamber.

具体地,所述隧道式多级串联热泵干燥系统的外部围护结构采用聚氨酯保温板。Specifically, the outer enclosure structure of the tunnel-type multi-stage series heat pump drying system adopts polyurethane insulation boards.

(三)有益效果(3) Beneficial effects

本发明的上述技术方案具有如下优点:The technical scheme of the present invention has the following advantages:

本发明采用了串联的多级热泵系统,将各热泵系统的蒸发器依次串联构成多级除湿室,将各热泵系统的冷凝器依次串联构成多级加热室,在多级加热室与多级除湿室之间设置混合室,其中,通过多级除湿室对隧道式干燥室排除的高温高湿的废气进行逐级降温除湿,在混合室中将逐级降温除湿后的空气与经过太阳能新风系统预热后的新风混合,通过多级加热室对混合后的空气进行逐级加热升温,实现多级降温除湿和等湿加热,从而有效回收废热,降低热泵系统中单级压缩机的压缩比,提高压缩机的效率。The present invention adopts a series-connected multi-stage heat pump system. The evaporators of each heat pump system are connected in series to form a multi-stage dehumidification chamber, and the condensers of each heat pump system are connected in series to form a multi-stage heating chamber. A mixing chamber is set between the chambers, in which, the high-temperature and high-humidity exhaust gas discharged from the tunnel drying chamber is gradually cooled and dehumidified through the multi-stage dehumidification chamber. The heated fresh air is mixed, and the mixed air is heated and heated step by step through the multi-stage heating chamber to realize multi-stage cooling and dehumidification and equal humidity heating, thereby effectively recovering waste heat, reducing the compression ratio of the single-stage compressor in the heat pump system, and improving compressor efficiency.

本发明采用连续的隧道式干燥室进行物料干燥,物料在隧道式干燥室中的移动方向与干燥热风的流动方向相反,保证一定的送回风温差,实现干燥过程中系统的稳定性,提高废热的回收与能效。The invention adopts a continuous tunnel-type drying chamber for material drying, and the moving direction of the material in the tunnel-type drying chamber is opposite to the flow direction of the drying hot air, so as to ensure a certain temperature difference between the sending and returning air, realize the stability of the system during the drying process, and improve the waste heat. recycling and energy efficiency.

本发明利用了太阳能系统,通过太阳能系统实现了对新风的预热处理,有效降低干燥能耗,其中通过吸附结构能够显著地吸附太阳能并储蓄,从而提高太阳能的利用率。The invention utilizes the solar energy system, realizes the preheating treatment of the fresh air through the solar energy system, effectively reduces the drying energy consumption, wherein the solar energy can be significantly absorbed and stored through the adsorption structure, thereby improving the utilization rate of the solar energy.

附图说明Description of drawings

图1是本发明实施例隧道式多级串联热泵干燥系统中空气封闭循环的示意图;Fig. 1 is the schematic diagram of air closed cycle in the tunnel type multi-stage series heat pump drying system of the embodiment of the present invention;

图2是本发明实施例隧道式多级串联热泵干燥系统中太阳能预热新风示意图;Fig. 2 is a schematic diagram of solar preheating fresh air in a tunnel type multi-stage series heat pump drying system according to an embodiment of the present invention;

图3是本发明实施例隧道式多级串联热泵干燥系统中图2的A-A向剖视图;Fig. 3 is the A-A sectional view of Fig. 2 in the tunnel type multi-stage series heat pump drying system according to the embodiment of the present invention;

图4是本发明实施例隧道式多级串联热泵干燥系统中储水盘的结构示意图。Fig. 4 is a schematic structural view of a water storage tray in a tunnel-type multi-stage series heat pump drying system according to an embodiment of the present invention.

图中:1:主风机;2:物料推车;3:出料口;4:进料口;5:新风阀;6:排风阀;7:排风道;8:吸附结构;9:透光隔热板;10:围护结构;11:储水盘;12:引出管道;13:支撑板;100:隧道式干燥室;200:新风加热室;300:多级加热室;400:多级除湿室;500:混合室。In the figure: 1: main fan; 2: material trolley; 3: discharge port; 4: feed port; 5: fresh air valve; 6: exhaust valve; 7: exhaust duct; 8: adsorption structure; 9: Light-transmitting heat insulation board; 10: enclosure structure; 11: water storage tray; 12: outlet pipe; 13: support plate; 100: tunnel drying room; 200: fresh air heating room; 300: multi-stage heating room; 400: Multi-stage dehumidification chamber; 500: mixing chamber.

具体实施方式detailed description

为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments It is a part of embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

如图1-4所示,本发明实施例提供一种隧道式多级串联热泵干燥系统,包括从上到下依次设置的太阳能系统、热泵循环系统和干燥系统。As shown in Figures 1-4, an embodiment of the present invention provides a tunnel type multi-stage series heat pump drying system, including a solar system, a heat pump circulation system and a drying system arranged in sequence from top to bottom.

干燥系统包括隧道式干燥室100,隧道式干燥室100的前后两侧分别设有进料口4和出料口3。The drying system includes a tunnel-type drying chamber 100, and the front and rear sides of the tunnel-type drying chamber 100 are respectively provided with a feed port 4 and a discharge port 3.

太阳能系统为太阳能新风系统,太阳能新风系统包括透光隔热板9、吸附结构8和支撑板13,其中支撑板13设置在吸附结构8上,透光隔热板9设置在支撑板13上,透光隔热板9、吸附结构8和支撑板13三者合围构成新风加热室200。The solar energy system is a solar fresh air system, and the solar fresh air system includes a light-transmitting heat insulation board 9, an adsorption structure 8 and a support plate 13, wherein the support plate 13 is arranged on the adsorption structure 8, and the light-transmitting heat insulation board 9 is arranged on the support plate 13, The light-transmitting heat insulation board 9 , the adsorption structure 8 and the supporting board 13 enclose the fresh air heating chamber 200 .

热泵循环系统包括n个热泵系统,其中n≥2,在本实施例中各热泵系统的冷凝器分别为C1、C2…Cn,将各冷凝器依次串联构成多级加热室300。在本实施例中各热泵系统的蒸发器分别为E1、E2…En,将各蒸发器依次串联构成多级除湿室400。在多级加热室300与多级除湿室400之间设有混合室500,混合室500的左右两侧分别设有排风道7。The heat pump cycle system includes n heat pump systems, where n≥2. In this embodiment, the condensers of each heat pump system are C1, C2...Cn, and the condensers are connected in series to form a multi-stage heating chamber 300 . In this embodiment, the evaporators of each heat pump system are respectively E1 , E2 . A mixing chamber 500 is provided between the multi-stage heating chamber 300 and the multi-stage dehumidification chamber 400, and the left and right sides of the mixing chamber 500 are respectively provided with exhaust ducts 7 .

其中,多级加热室300、混合室500和多级除湿室400从前到后依次连通。多级加热室300通过送风口与隧道式干燥室100相连通,多级除湿室400通过回风口与隧道式干燥室100相连通。新风加热室200通过热风进口与混合室500相连通,混合室500通过排风口与排风道7相连通。Wherein, the multi-stage heating chamber 300, the mixing chamber 500 and the multi-stage dehumidification chamber 400 are connected in sequence from front to back. The multi-stage heating chamber 300 communicates with the tunnel-type drying chamber 100 through the air supply port, and the multi-stage dehumidification chamber 400 communicates with the tunnel-type drying chamber 100 through the air return port. The fresh air heating chamber 200 communicates with the mixing chamber 500 through the hot air inlet, and the mixing chamber 500 communicates with the exhaust duct 7 through the air outlet.

其中,隧道式干燥室100的出料口3设置在与多级加热室300的送风口相对应的一侧,隧道式干燥室100的进料口4设置在与多级除湿室400的回风口相对应的一侧。Wherein, the discharge port 3 of the tunnel-type drying chamber 100 is arranged on the side corresponding to the air supply port of the multi-stage heating chamber 300, and the feed port 4 of the tunnel-type drying chamber 100 is arranged on the air return port of the multi-stage dehumidification chamber 400. the corresponding side.

在隧道式干燥室中设有物料推车2,物料推车2从进料口4进入到隧道式干燥室100中,再从出料口3而出,在此过程中,通过隧道式干燥室100对物料推车2中的物料进行干燥处理。A material trolley 2 is provided in the tunnel drying chamber. The material trolley 2 enters the tunnel drying chamber 100 from the feed port 4, and then exits from the discharge port 3. During this process, the material cart 2 passes through the tunnel drying chamber. 100 carries out drying process to the material in the material trolley 2.

其中,太阳能系统的支撑板13上设有新风进口,外部新风通过新风进口进口进入到新风加热室200中。透光隔热板9能够有效地透射较多的太阳光,同时具有隔热作用,用于对新风进行预加热。吸附结构8的内部设置蓄热材料,吸附结构8的外表面设置太阳能吸附材料,可以有效地吸附太阳能并储能。Wherein, the supporting plate 13 of the solar system is provided with a fresh air inlet, and the external fresh air enters the fresh air heating chamber 200 through the fresh air inlet. The light-transmitting heat-shielding plate 9 can effectively transmit more sunlight, and has a heat-insulating effect at the same time, and is used for preheating fresh air. The interior of the adsorption structure 8 is provided with a heat storage material, and the outer surface of the adsorption structure 8 is provided with a solar adsorption material, which can effectively absorb solar energy and store energy.

进一步来说,每个独立的热泵系统是由压缩机、冷凝器、节流阀、蒸发器、连接管道以及相应附件构成。其中,各压缩机分别为N1、N2…Nn,各节流阀分别为V1、V2…Vn,其中每个蒸发器通过压缩机与冷凝器相连,冷凝器再通过节流阀与蒸发器相连。其中,压缩机优选采用变频压缩机。Furthermore, each independent heat pump system is composed of a compressor, a condenser, a throttle valve, an evaporator, connecting pipes and corresponding accessories. Among them, the compressors are N1, N2...Nn, and the throttle valves are V1, V2...Vn, and each evaporator is connected to the condenser through the compressor, and the condenser is connected to the evaporator through the throttle valve. Wherein, the compressor is preferably a variable frequency compressor.

具体来说,在多级除湿室400中设有储水盘11,储水盘11设置在所述蒸发器的底部,在储水盘11上设有引出管道12。Specifically, a water storage tray 11 is provided in the multi-stage dehumidification chamber 400 , and the water storage tray 11 is arranged at the bottom of the evaporator, and an outlet pipe 12 is provided on the water storage tray 11 .

其中,在多级加热室300的送风口处设有主风机1,主风机1优选采用变频风机。Wherein, a main fan 1 is provided at the air supply port of the multi-stage heating chamber 300, and the main fan 1 is preferably a variable frequency fan.

其中,在热风进口上设有新风阀5,在排风口上设有排风阀6,其中新风阀5和排风阀6均采用开度可调节的风阀。本发明通过排风阀6和新风阀5对系统的热湿平衡进行调控,结合太阳能系统,不仅保证系统干燥过程的稳定性,且有效提高系统的能效。Wherein, a fresh air valve 5 is provided on the hot air inlet, and an exhaust valve 6 is provided on the air outlet, wherein both the fresh air valve 5 and the exhaust valve 6 are air valves with adjustable openings. The present invention regulates the heat-humidity balance of the system through the air exhaust valve 6 and the fresh air valve 5, combined with the solar energy system, not only ensures the stability of the drying process of the system, but also effectively improves the energy efficiency of the system.

其中,在本发明隧道式多级串联热泵干燥系统的围护结构10采用保温材料,该保温材料优选采用聚氨酯保温板。本发明在系统的外围采用保温材料作为围护结构,可实现半开式、闭路式单独或混合运行,可有效地适应除外界恶劣环境,提高系统的能效。Wherein, the enclosure structure 10 of the tunnel-type multi-stage series heat pump drying system of the present invention adopts thermal insulation materials, and the thermal insulation materials preferably adopt polyurethane thermal insulation boards. The invention adopts thermal insulation material as the enclosure structure on the periphery of the system, which can realize semi-open and closed-circuit separate or mixed operation, can effectively adapt to the harsh external environment, and improve the energy efficiency of the system.

此外,本发明所述的隧道式多级串联热泵干燥系统,还包括控制系统,所述控制系统包括控制开关、温度控制器、湿度控制器和PLC面板等。In addition, the tunnel-type multi-stage series heat pump drying system of the present invention also includes a control system, which includes a control switch, a temperature controller, a humidity controller, and a PLC panel.

本发明所述的隧道式多级串联热泵干燥系统,其工作原理如下:The working principle of the tunnel type multi-stage series heat pump drying system described in the present invention is as follows:

从隧道式干燥室100排出的高温高湿的废气通过回风口进入多级除湿室400,在多级除湿室400中依次从第n级蒸发器En到第1级蒸发器E1进行逐级降温除湿,逐级降温除湿后的空气进入混合室500,与经过太阳能系统预热后的新风进行混合,然后混合后的空气进入多级加热室300,在多级加热室300中依次从第1级冷凝器C1到第n级冷凝器Cn进行加热升温。经过除湿升温后的空气经过主风机1的作用下再通过送风口进入到隧道式干燥室100中对物料进行干燥处理,与湿物料进行热湿传递。在此过程中,隧道式干燥室100中物料推车2沿着与干燥热风的流动方向相反的方向逐渐移动,在移动过程中实现对物料的干燥。The high-temperature and high-humidity exhaust gas discharged from the tunnel-type drying chamber 100 enters the multi-stage dehumidification chamber 400 through the air return port, and in the multi-stage dehumidification chamber 400, the temperature and dehumidification are carried out step by step from the nth-stage evaporator En to the first-stage evaporator E1 , the dehumidified air enters the mixing chamber 500 and is mixed with the fresh air preheated by the solar system, and then the mixed air enters the multi-stage heating chamber 300, where it is sequentially condensed from the first stage From the condenser C1 to the nth stage condenser Cn, the temperature is raised by heating. The dehumidified and heated air passes through the main fan 1 and then enters the tunnel drying chamber 100 through the air supply port to dry the materials and transfer heat and moisture with the wet materials. During this process, the material trolley 2 in the tunnel-type drying chamber 100 gradually moves along the direction opposite to the flow direction of the drying hot air, and the material is dried during the moving process.

在上述过程中,根据干燥过程系统的湿热稳定,调节新风阀5和排风阀6,其中新风量和排风量由新风阀5和排风阀6的开度控制。当出现热湿不平衡现象时,开启新风阀5和排风阀6,经排风道7排除掉经多级除湿室排出的部分空气,再经新风阀5引入经太阳能系统预热的新风,如图2所示,图中的箭头方向表示空气流动方向。而在热湿平衡的情况下,则关闭新风阀5和排风阀6,此时系统中的空气为闭合循环,如图1所示,图中的箭头方向表示空气流动方向。In the above process, adjust the fresh air valve 5 and the exhaust valve 6 according to the humidity and heat stability of the drying process system, wherein the fresh air volume and exhaust air volume are controlled by the opening of the fresh air valve 5 and the exhaust valve 6 . When heat and humidity are unbalanced, open the fresh air valve 5 and the exhaust valve 6, remove part of the air discharged through the multi-stage dehumidification chamber through the exhaust duct 7, and then introduce the fresh air preheated by the solar system through the fresh air valve 5, As shown in Figure 2, the direction of the arrow in the figure indicates the direction of air flow. In the case of heat and humidity balance, the fresh air valve 5 and the exhaust valve 6 are closed, and the air in the system is in a closed cycle at this time, as shown in Figure 1, the direction of the arrow in the figure indicates the direction of air flow.

在上述过程中,根据所需循环风量调节主风机1的频率,使循环风量满足系统干燥工况要求,控制循环风量调节干燥速率。In the above process, the frequency of the main fan 1 is adjusted according to the required circulating air volume, so that the circulating air volume meets the requirements of the drying conditions of the system, and the drying rate is adjusted by controlling the circulating air volume.

在上述过程中,物料推车2的进出速率和方式可根据物料的实际情况进行调控。In the above-mentioned process, the speed and way of entering and exiting the material trolley 2 can be regulated according to the actual situation of the material.

综上所述,本发明实施例所述的隧道式多级串联热泵干燥系统,能够有效的回收废热,并通过太阳能的利用降低了系统的总能耗,而相比单级热泵干燥系统,本发明采用多级除湿能够有效地除去干燥空气中的水分,采用多级加热满足了送回风温差较大情况,提高了压缩机效率,有效提高了除湿效率。In summary, the tunnel-type multi-stage series heat pump drying system described in the embodiment of the present invention can effectively recover waste heat and reduce the total energy consumption of the system through the utilization of solar energy. Compared with the single-stage heat pump drying system, this The invention adopts multi-stage dehumidification to effectively remove moisture in the dry air, adopts multi-stage heating to meet the situation of large temperature difference between the air sent and returned, improves the efficiency of the compressor, and effectively improves the dehumidification efficiency.

需要说明的是,在本发明的描述中,除非另有说明,“多个”的含义是两个或两个以上;术语“上”、“下”、“左”、“右”、“内”、“外”、“前端”、“后端”、“头部”、“尾部”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。It should be noted that, in the description of the present invention, unless otherwise specified, the meaning of "plurality" is two or more; the terms "upper", "lower", "left", "right", "inner ", "outside", "front end", "rear end", "head", "tail", etc. indicate the orientation or positional relationship based on the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the present invention and Simplified descriptions, rather than indicating or implying that the device or element referred to must have a particular orientation, be constructed and operate in a particular orientation, and thus should not be construed as limiting the invention.

最后应说明的是:以上实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的精神和范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: it can still be Modifications are made to the technical solutions described in the foregoing embodiments, or equivalent replacements are made to some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the various embodiments of the present invention.

Claims (10)

1. a kind of tunnel type plural serial stage Analysis of Heat Pump Drying System, it is characterised in that:At least include setting gradually from top to bottom too Positive energy system, heat pump circulating system and drying system;
The drying system includes tunnel chamber for drying;
The solar energy system is solar energy VMC, and the solar energy VMC includes fresh air heating chamber;
The heat pump circulating system includes multiple heat pumps, and the condenser of each heat pump is followed in series to form multistage add Hot cell, the evaporator of each heat pump is followed in series to form multistage moist chamber, in the Multi-stage heating room and the multistage Mixing chamber is provided between moist chamber, the mixing chamber is respectively arranged on the left side and the right side exhausting duct;
Described Multi-stage heating room, mixing chamber and multistage moist chamber is sequentially communicated from front to back;The Multi-stage heating room is by sending Air port is connected with the tunnel chamber for drying, and the multistage moist chamber is connected by return air inlet with the tunnel chamber for drying It is logical;The fresh air heating chamber is connected by hot wind inlet with the mixing chamber, and the mixing chamber passes through exhaust outlet and the row Air channel is connected.
2. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 1, it is characterised in that:The solar energy fresh air System includes printing opacity thermal insulation board, adsorption structure and supporting plate, wherein the supporting plate is arranged on the adsorption structure, it is described Light thermal insulation board is arranged in the supporting plate, and described printing opacity thermal insulation board, adsorption structure and supporting plate surrounds the composition fresh air Heating chamber.
3. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 2, it is characterised in that:The adsorption structure Inside sets heat-storing material, and the outer surface of the adsorption structure sets solar energy sorbing material.
4. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 2, it is characterised in that:Set in the supporting plate There is fresh inlet.
5. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 1, it is characterised in that:The tunnel type is dried Room is provided with charging aperture and discharging opening, wherein the discharging opening is arranged on one of the correspondence air outlet in the tunnel chamber for drying Side, the charging aperture is arranged on the side of the correspondence return air inlet in the tunnel chamber for drying.
6. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 1, it is characterised in that:In the multistage dehumidifying Water storage disk is provided with room, the water storage disk is arranged on the bottom of the evaporator, and the water storage disk is provided with introduction pipe.
7. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 1, it is characterised in that:In the Multi-stage heating Main air blower is provided with the air outlet of room, the main air blower uses frequency conversion fan.
8. tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim 1, it is characterised in that:In the hot wind inlet Provided with new air-valve, the exhaust outlet is provided with exhaust valve.
9. the tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim any one of 1-8, it is characterised in that:The tunnel Material stroller, the moving direction of the material stroller and dry-heat air in the tunnel chamber for drying are provided with road formula hothouse Flow direction is opposite.
10. the tunnel type plural serial stage Analysis of Heat Pump Drying System according to claim any one of 1-8, it is characterised in that:It is described The outside building enclosure of tunnel type plural serial stage Analysis of Heat Pump Drying System uses polyurethane thermal insulation board.
CN201710487847.0A 2017-06-23 2017-06-23 Tunnel type multistage series heat pump drying system Pending CN107289767A (en)

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Publication number Priority date Publication date Assignee Title
CN108302927A (en) * 2018-04-17 2018-07-20 华北电力大学 A kind of drying system of solar energy auxiliary multi-stage heat pump and multistage air-cooled coupling
CN108528028A (en) * 2018-03-16 2018-09-14 广州黑马科技有限公司 A kind of printing ink drying system
CN109813095A (en) * 2019-03-18 2019-05-28 青岛大学 Segmented near-closed heat pump drying system
CN111288784A (en) * 2020-03-23 2020-06-16 河南海弗星换热科技有限公司 Multistage dehumidification heating switching ring integrated heat pump unit
WO2020220898A1 (en) * 2019-04-29 2020-11-05 南京研正干燥设备有限公司 Tunnel dryer

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CN106766795A (en) * 2016-11-25 2017-05-31 中国科学院理化技术研究所 Tunnel type multistage heat pump series drying and dehumidifying system

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CN106440748A (en) * 2016-10-14 2017-02-22 安徽美乐柯制冷空调设备有限公司 Heat pump type drying device
CN106766795A (en) * 2016-11-25 2017-05-31 中国科学院理化技术研究所 Tunnel type multistage heat pump series drying and dehumidifying system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108528028A (en) * 2018-03-16 2018-09-14 广州黑马科技有限公司 A kind of printing ink drying system
CN108528028B (en) * 2018-03-16 2020-08-14 广州黑马科技有限公司 A printing ink drying system
CN108302927A (en) * 2018-04-17 2018-07-20 华北电力大学 A kind of drying system of solar energy auxiliary multi-stage heat pump and multistage air-cooled coupling
CN109813095A (en) * 2019-03-18 2019-05-28 青岛大学 Segmented near-closed heat pump drying system
WO2020220898A1 (en) * 2019-04-29 2020-11-05 南京研正干燥设备有限公司 Tunnel dryer
CN111288784A (en) * 2020-03-23 2020-06-16 河南海弗星换热科技有限公司 Multistage dehumidification heating switching ring integrated heat pump unit

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