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Microwave multistage fluidized bed drying device and drying method thereof

A fluidized bed drying, fluidized bed technology, applied in the direction of drying gas arrangement, heating device, drying solid materials, etc., can solve the problems of high drying efficiency, overheating, uneven drying, etc., and achieve novel and reliable structure, easy manufacturing, and equipment simple effect

Active Publication Date: 2014-08-27
JINING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the traditional fluidized bed drying equipment has the following disadvantages: 1. Most of the currently used fluidized bed drying equipment is a single-stage fluidized bed. Uneven drying or overheating occurs; 2. The use of hot air in traditional fluidized bed drying media has the danger of oxidation, fire and explosion of the dried material, while the use of superheated steam will bring problems such as high energy consumption and water shortage; 3. The fluidized bed equipment with a built-in heat exchanger hinders the normal fluidization of the material due to the unreasonable setting of the buried pipe, especially when the material with high humidity just enters the dryer, it is easy to cause the accumulation and blockage of the material between the pipes. In addition, Fluidized bed drying technology with built-in heat exchanger still has problems such as serious wear of heat exchange tubes
However, the above equipment is not conducive to controlling the residence time of materials, prone to uneven drying or overheating, and it is difficult to achieve continuous drying
[0006] To sum up, there is currently no good coupling technology for microwave drying and fluidized bed drying, which can control the residence time of materials, continuously and uniformly enter and exit materials, low drying energy consumption, high drying efficiency, and high material quality. can guarantee

Method used

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  • Microwave multistage fluidized bed drying device and drying method thereof
  • Microwave multistage fluidized bed drying device and drying method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Embodiment 1, with reference to Figure 1-2 , a kind of microwave multi-stage fluidized bed drying device described in this specific embodiment, comprises silo 1, screw feeder 2 and fluidized bed drier 3, is provided with screw feeder 2 below feeder 1, and screw feeder 2 The feeder 2 communicates with the feed inlet 23 on the upper part of the fluidized bed drier 3. The fluidized bed drier 3 includes a fluidized bed body 4 and a gas distribution plate 5. On the outer wall of the fluidized bed body 4 A microwave generator 6 is provided, and three layers of gas distribution plates 5 with adjustable angles are arranged from top to bottom inside the fluidized bed body 4 .

[0033] The adjustment range of the angle between the gas distribution plate 5 and the inner wall of the fluidized bed body 4 is 0-60 degrees.

[0034] The outer wall of the fluidized bed body 4 is provided with three microwave generators 6, and the gas distribution plate 5 is located at the correspondin...

Embodiment 2

[0047] The material to be dried is lignite with an initial water content of 35%. The lignite is crushed and transported into the silo 1 with a particle size of 8mm. The raw material enters the fluidized bed dryer 3 through the screw feeder 2; the fluidized medium air passes through the gas flow The meter 8 and the gas preheater 10 enter the fluidized bed dryer 3 from the air inlet 16, and three layers of gas distribution plates 5 are laid in the fluidized bed dryer 3, and the opening rate of the gas distribution plate 5 is 4%; the microwave generator is turned on 6. The power is 2500W. The temperature of the material in the fluidized bed dryer 3 is measured by the infrared temperature measuring probe 24, and the power of the microwave generator 6 is adjusted according to the surface temperature of the raw material to keep the temperature in the fluidized bed dryer 3 at 180°C; through the gas flow meter 8 Adjust the gas velocity to about 1.6 m / s, control the residence time of th...

Embodiment 3

[0049] The material to be dried is lignite with an initial water content of 55%. The lignite is crushed and transported into the silo 1 with a particle size of 7mm. The raw material enters the fluidized bed dryer 3 through the screw feeder 2; the fluidized medium air passes through the gas flow The meter 8 and the gas preheater 10 enter the fluidized bed dryer 3 from the air inlet 16, and three layers of gas distribution plates 5 are laid in the fluidized bed dryer 3, and the opening rate of the gas distribution plate 5 is 4%; The power of the microwave generator 6 is 3000W, the temperature of the material in the fluidized bed dryer 3 is measured by the infrared temperature measuring probe 24, the power of the microwave generator 6 is adjusted according to the surface temperature of the raw material, and the temperature in the fluidized bed dryer 3 is kept at 195°C; 8. Adjust the gas velocity to about 1.8 m / s. After controlling the material residence time for 5 minutes, adjust ...

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Abstract

The invention relates to a microwave multistage fluidized bed drying device and a drying method of the microwave multistage fluidized bed drying device. A fluidized bed dryer comprises a fluidized bed body and gas distribution plates, a microwave generator is arranged on the outer wall of the fluidized bed body, three layers of the gas distribution plates with adjustable angles are arranged in the fluidized bed body from top to bottom, the microwave generator is started, microwaves are used as a heat source, the inclination angle and the microwave power of the gas distribution plates are adjusted according to the surface temperature of detection materials, the aperture ratio of the gas distribution plates ranges from three percent to five percent, the adjustment air speed ranges from 1 m / s to 2 m / s, the raw material standing time is controlled to be within one min to five min, the water content in raw materials is smaller than 15 percent, and the dried materials enter a product drying tank from a discharge port. The microwave multistage fluidized bed drying device and the drying method of the microwave multistage fluidized bed drying device have the advantages that the standing time of the materials in a fluidized bed drying reactor is controlled by adjusting the inclination angles of the multistage distribution plates, and the materials with different water contents can be dried; maximum utilization of microwave energy is achieved by changing the microwave drying power at feed ports of the multistage distribution plates.

Description

[0001] technical field [0002] The invention and a drying device and method are especially suitable for materials with high water content, easy oxidation and spontaneous combustion, and especially relate to a microwave multi-stage fluidized bed drying device and a drying method thereof. Background technique [0003] Fluidized bed drying equipment is widely used in chemical industry, petroleum, food, biomedicine and other industries, and is suitable for drying various granular, flake and heat-sensitive materials. However, the traditional fluidized bed drying equipment has the following disadvantages: 1. Most of the currently used fluidized bed drying equipment is a single-stage fluidized bed. Uneven drying or overheating occurs; 2. The use of hot air in traditional fluidized bed drying media has the danger of oxidation, fire and explosion of the dried material, while the use of superheated steam will bring problems such as high energy consumption and water shortage; 3. The ...

Claims

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Application Information

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IPC IPC(8): F26B3/08F26B21/00F26B23/08
Inventor 司崇殿王宇光刘国栋张功国苑壮东陈万东
Owner JINING UNIV
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