CN203053173U - Carbon fiber far infrared/ air energy drying device - Google Patents
Carbon fiber far infrared/ air energy drying device Download PDFInfo
- Publication number
- CN203053173U CN203053173U CN 201320064813 CN201320064813U CN203053173U CN 203053173 U CN203053173 U CN 203053173U CN 201320064813 CN201320064813 CN 201320064813 CN 201320064813 U CN201320064813 U CN 201320064813U CN 203053173 U CN203053173 U CN 203053173U
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- drying
- heat
- air
- carbon fiber
- far infrared
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Abstract
The utility model relates to a drying device, in particular to a carbon fiber far infrared/ air energy drying device. A tunnel material conveyor is installed on an interior bottom of a drying tunnel kiln, heat energy superconduction radiators are placed on a left side wall and a right side wall inside the drying tunnel kiln and are connected with an air energy and heat energy storage device, a carbon fiber far infrared electric hot plate is arranged on the top side inside the drying tunnel kiln, a tunnel interior air circulation centrifugal fan and a dehumidification and air exhaust axial flow fan are installed on the top outside the drying tunnel kiln, superconduction heat exchangers are placed in a tunnel exhaust duct outlet and an air energy heat pump compressor air inlet, and an electrical equipment controlling cabinet is placed outside the drying funnel kiln. The carbon fiber far infrared/ air energy drying device has the advantages of being simple in structure, high in heat energy utilization efficiency, low in running cost, fast in dehydration and drying, good in drying article quality effect and easy to operate and control. The carbon fiber far infrared/ air energy drying device is very suitable for drying and processing products of pyrolysis industries, agriculture, animal husbandry, fishery and various forest subsidiary businesses.
Description
(1) technical field
The utility model relates to a kind of drying plant, specifically a kind of carbon fiber far infrared/air energy drying equipment.
(2) background technology
In the worker who relates generally to, agricultural oven dry production practices, the capital equipment device that heating, drying adopts has at present: fire coal, the conduction of gas fired-boiler thermal medium, electric heating hot-air seasoning equipment and high temperature microwave, far infrared radiation control drying technology equipment.Fire coal, combustion gas and boiler, the oven dry of electric heating wind, its operation principle are medium heat conduction intensification technology, and its energy resource consumption is big, and thermal conversion efficiency is low, and the heat energy utilization rate is little, the heating and temperature control technical sophistication.The production cycle of oven dry product is long, and carbon emission etc. are all kinds of seriously polluted.Microwave or high temperature far infrared are controlled technical equipment cost of goods manufactured height, energy consumption is big, radiation proof control technology, operating temperature control technology complexity, and extensive, large tracts of land is promoted the use of comprehensively.
(3) utility model content
It is a kind of simple in structure that the purpose of this utility model is to provide, and production and operation cost is low, energy-conserving and environment-protective, and the drying and dewatering mass effect is good, and is safe and reliable, a kind of carbon fiber far infrared/air energy drying equipment of easy operating control.
The utility model is made of air energy heat pump unit, heat energy accumulator, the Drying tunnel that has heat-insulation layer, electrical control cabinet, carbon fiber Far-infrared Heating plate, tunnel material conveyer.At the Drying tunnel kiln inner bottom surface that has heat-insulation layer the tunnel material conveyer is housed; The and arranged on left and right sides wall is provided with the heat energy superconducting radiator in the Drying tunnel kiln; Superconducting radiator, heat energy accumulator heat conduction pump are connected with the heat conduction pipeline and form a closed-loop path; Be connected with exhaust duct on the circular centrifugal blower fan, the inner top side of Drying tunnel kiln is provided with carbon fiber far infrared electric heating plate, the outer top of Drying tunnel kiln is equipped with tunnel air circular centrifugal blower fan and tunnel dehumidifying air draft axial flow blower, is provided with superconduction hot blast heat exchanger in the exhaust duct outlet with air energy heat pump compressor inlet place; Electric control cabinet is located at outside the Drying tunnel kiln that has heat-insulation layer.
Advantage of the present utility model is that device structure is simple, the utilization efficiency of heat energy height, and the operation cost expense is low, and dehydration, drying rate is fast, and the dry goods mass effect is good, easy operating control.Its is fit to pyrolysis industry, farming very much, herd, the oven dry processing of fishing and all kinds of woods sideline products.
(4) description of drawings
Accompanying drawing is structural representation of the present utility model:
1-electric control cabinet 2-temperature, humidity controller 3-heat conduction pump 4-air can controller 5-material conveyer 6-Drying tunnel kiln 7-air energy heat pump 8-superconduction hot blast heat exchanger 9-exhaust duct 10-accumulator 11-heat conduction pipeline 12-circular centrifugal blower fan 13-carbon fiber far infrared electric heating plate 14-superconducting radiator 15-dehumidifying air draft axial flow blowers
(5) specific embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail:
The utility model is made of air energy heat pump unit (7), heat energy accumulator (10), electric control box (1), the Drying tunnel kiln (6) that is laid with heat-insulation layer, tunnel material conveyer (5), and the utility model is at Drying tunnel kiln (6) inner bottom surface that has heat-insulation layer tunnel material conveyer (5) to be housed; The interior and arranged on left and right sides wall of Drying tunnel kiln (6) is provided with heat energy superconducting radiator (14); Superconducting radiator (14), heat energy accumulator (10) heat conduction pump (3) and heat conduction pipeline (11) are connected and form a closed-loop path; Be connected with exhaust duct (9) on the circular centrifugal blower fan (12), the inner top side of Drying tunnel kiln (6) is provided with carbon fiber far infrared electric heating plate (13), the outer top of Drying tunnel kiln (6) is equipped with tunnel air circular centrifugal blower fan (12) and tunnel dehumidifying air draft axial flow blower (15), is provided with superconduction hot blast heat exchanger (8) in exhaust duct (9) outlet with air energy heat pump (7) compressor inlet place; Electric control cabinet (1) is located at outside the Drying tunnel kiln (6) that has heat-insulation layer.
Electric control cabinet has in (1): temperature, humidity controller (2), air energy heat conduction pump (3), material conveyer (5), air energy controller (4), its temperature, humidity controller (2) are connected with circular centrifugal blower fan (12), heat conduction pump (3) and dehumidifying air draft axial flow blower (15), carbon fiber far infrared electric heating plate (13) respectively.
During the utility model work: when the electric control box power connection is started working, according to volume and the moisture content of difference oven dry material, set, start the speed of service of operation material conveyer (5) at electric control cabinet (1); Startup is according to different product manufacturing requirements temperature, the design coupling is installed in the carbon fiber far infrared electric heating plate (13) of Drying tunnel kiln (6) inner top, the far infrared that produces during its work, directly radiation effects heats up it in the inner heating of material on the oven dry material; Automatically control startup heat energy heat conduction pump (3) simultaneously, under the effect of heat conduction pump (3), the thermal energy by air energy heat pump (7) work generation of air energy accumulator (10) storage conducts to superconducting radiator (14) by heat conduction pipeline (11).Circular centrifugal blower fan (12) startup work simultaneously.Under the effect of circular centrifugal blower fan (12), through wind direction control, to be installed in the thermal energy diffusion conduction that the superconducting radiator (14) of the interior two sides of Drying tunnel kiln (6) distributes, the interior air dielectric of Drying tunnel kiln (6) is heated up, recirculated hot air also constantly melts the moisture of walking the material surface when adding thermal material from the surface and making its intensification.The air dielectric temperature reaches the production technical conditions temperature value of temperature, humidity controller (2) setting in Drying tunnel kiln (6), and the control automatically of carbon fiber Far-infrared Heating plate (13), circular centrifugal blower fan (12), heat conduction pump (3) quits work; Dehumidifying air draft axial flow blower (15) is controlled startup work automatically, discharges the hot and humid air in the tunnel cave.When temperature, the humidity of air dielectric in the tunnel reached the falling setting value of controller (2), controller was controlled dehumidifying air draft axial flow blower (15) automatically and is quit work.The work of resetting automatically of carbon fiber Far-infrared Heating plate (13), circular centrifugal blower fan (12), heat conduction pump (3).The reciprocation cycle action reaches the product drying technical standard requirement of oven dry material always.Material conveyer (5) discharging opening is derived qualified oven dry product.The damp and hot waste gas of discharging through tunnel exhaust duct (9) in the Drying tunnel kiln (6), by the compressor air inlet of superconduction hot blast heat exchanger (8) heat exchange to air energy heat pump (7), provide high heat energy air for air energy heat pump (7) heats accumulation of energy, thereby realize the article dewatered drying purpose of fast energy-saving, environmental protection.
Claims (1)
1. carbon fiber far infrared/air energy drying equipment, constituted by air energy heat pump unit, heat energy accumulator, hot blast superconduction heat exchanger, the Drying tunnel that has heat-insulation layer, electrical control cabinet, tunnel material conveyer, it is characterized in that at Drying tunnel kiln (6) inner bottom surface tunnel material conveyer (5) being housed; The interior and arranged on left and right sides wall of Drying tunnel kiln (6) is provided with heat energy superconducting radiator (14); Superconducting radiator (14), heat energy accumulator (10) heat conduction pump (3) and heat conduction pipeline (11) are connected and form the loop; Be connected with exhaust duct (9) on the circular centrifugal blower fan (12), the inner top side of Drying tunnel kiln (6) is provided with carbon fiber far infrared electric heating plate (13), the outer top of Drying tunnel kiln (6) is equipped with tunnel air circular centrifugal blower fan (12) and tunnel dehumidifying air draft axial flow blower (15), is provided with superconduction hot blast heat exchanger (8) at the compressor inlet place of exhaust duct (9) and air energy heat pump (7); Electric control cabinet (1) is located at outside the Drying tunnel kiln (6) that has heat-insulation layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 201320064813 CN203053173U (en) | 2013-01-04 | 2013-01-04 | Carbon fiber far infrared/ air energy drying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN 201320064813 CN203053173U (en) | 2013-01-04 | 2013-01-04 | Carbon fiber far infrared/ air energy drying device |
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CN203053173U true CN203053173U (en) | 2013-07-10 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201320064813 Expired - Fee Related CN203053173U (en) | 2013-01-04 | 2013-01-04 | Carbon fiber far infrared/ air energy drying device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108120278A (en) * | 2016-11-28 | 2018-06-05 | 登封市宏远电热元件有限公司 | A kind of double push plate continuous tunnel furnaces of single channel |
CN108120261A (en) * | 2016-11-28 | 2018-06-05 | 登封市宏远电热元件有限公司 | A kind of single channel double push plate continuous tunnel furnaces drying control device |
CN109141999A (en) * | 2018-08-23 | 2019-01-04 | 李二猛 | One kind is based on ground quality detection soil screening plant |
-
2013
- 2013-01-04 CN CN 201320064813 patent/CN203053173U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108120278A (en) * | 2016-11-28 | 2018-06-05 | 登封市宏远电热元件有限公司 | A kind of double push plate continuous tunnel furnaces of single channel |
CN108120261A (en) * | 2016-11-28 | 2018-06-05 | 登封市宏远电热元件有限公司 | A kind of single channel double push plate continuous tunnel furnaces drying control device |
CN109141999A (en) * | 2018-08-23 | 2019-01-04 | 李二猛 | One kind is based on ground quality detection soil screening plant |
CN109141999B (en) * | 2018-08-23 | 2021-05-04 | 山东省鲁南地质工程勘察院(山东省地勘局第二地质大队) | Soil screening plant for geological detection |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20150914 Address after: 710200, Shaanxi province Gaoling County small and medium enterprises gathered in the park (Yu Zhen Chu village) Patentee after: Xi'an Yude electrical switch manufacturing Co. Ltd. Address before: 712000 Shaanxi Xianyang Dongfeng Road Railway four company family hospital Patentee before: Song Qiangyi |
|
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130710 Termination date: 20160104 |