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Overlapping type two-temperature drying system

A drying system and cascade technology, applied in the direction of drying solid materials, drying solid materials without heating, drying, etc., can solve the problems of high investment cost, high operating cost, and unsatisfactory effect of reducing energy consumption, etc. To achieve the effect of reducing operating costs, reducing energy waste, and good energy efficiency

Inactive Publication Date: 2017-09-01
UNIV OF SHANGHAI FOR SCI & TECH
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

However, in the practical application of freeze-drying, the investment cost is high and the operating cost is high, which is 3 to 4 times the cost of air-drying, and in freeze-drying, the energy consumption of pre-freezing only accounts for 4%-14% of the energy generated by freeze-drying However, in the drying process, the total energy consumption of vacuum pumps, heating plates, and cold traps accounts for 86% to 96%, which greatly reduces the effective utilization rate of freeze-drying energy.
Although there are many ways to reduce the energy consumption of freeze-drying in recent years, such as shortening the drying time by optimizing process parameters, improving heat transfer to accelerate sublimation, and avoiding the use of cold traps, the effects of these methods on reducing energy consumption are not satisfactory

Method used

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  • Overlapping type two-temperature drying system
  • Overlapping type two-temperature drying system

Examples

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Embodiment Construction

[0016] In order to make the technical means, creative features, goals and effects of the present invention easy to understand, the following examples will specifically illustrate the cascade dual-temperature drying system of the present invention in conjunction with the accompanying drawings.

[0017] figure 1 It is a structural schematic diagram of a cascade double-temperature drying system in an embodiment of the present invention.

[0018] Such as figure 1 As shown, the cascade dual-temperature drying system 100 includes a low-pressure stage compressor 11, a first condensing evaporator 12, a first throttle valve 13, a low-temperature evaporator 14, a medium-pressure stage compressor 15, and a second condensing evaporator 16 , the second throttle valve 17, the high pressure stage compressor 18, the third throttle valve 20 and the high temperature condenser 19.

[0019] The low-pressure compressor 11 is used to compress refrigerant. In this embodiment, the refrigerant used ...

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Abstract

The invention provides an overlapping type two-temperature drying system. The overlapping type two-temperature drying system is characterized by comprising a low-pressure stage compressor, a low temperature evaporator, a first condensation evaporator, a middle-pressure stage compressor, a second condensation evaporator, a high-pressure stage compressor and a high temperature condenser; and the low-pressure stage compressor is connected with the low temperature evaporator and is connected with the middle-pressure stage compressor through the first condensation evaporator, the middle-pressure stage compressor is connected with the high-pressure stage compressor through the second condensation evaporator, and the high-pressure stage compressor is connected with the high temperature condenser. By means of the overlapping type two-temperature drying system, a high temperature heat source generated in the low temperature making process of the overlapping type system is sufficiently used, and the equipment running cost is reduced; and meanwhile, the heat energy quality can be improved to be used for drying, unfreezing and heat pump heating, the energy resource can be sufficiently used, and energy resource waste is reduced.

Description

technical field [0001] The invention relates to the field of freeze-drying, in particular to a cascade double-temperature drying system. Background technique [0002] Vacuum freeze drying is widely used in various industries due to its excellent drying effect. However, in the practical application of freeze-drying, the investment cost is high and the operating cost is high, which is 3 to 4 times the cost of air-drying, and in freeze-drying, the energy consumption of pre-freezing only accounts for 4%-14% of the energy generated by freeze-drying However, the total energy consumption of vacuum pumps, heating plates, and cold traps in the drying process accounts for 86% to 96%, which greatly reduces the effective utilization rate of freeze-drying energy. Although there are many ways to reduce the energy consumption of freeze-drying in recent years, such as shortening the drying time by optimizing process parameters, improving heat transfer to accelerate sublimation, and avoidin...

Claims

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Application Information

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IPC IPC(8): F26B5/06F25B41/06F25B7/00F25B41/31
CPCF25B7/00F26B5/06F25B41/30
Inventor 李保国罗权权张伟明白旭升
Owner UNIV OF SHANGHAI FOR SCI & TECH
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