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Coal drying device and drying method

A drying device and drying method technology, applied in drying solid materials, heating to dry solid materials, drying, etc., can solve the problems of catastrophic consequences, loss of coal volatiles, low gas-solid heat transfer efficiency, etc.

Active Publication Date: 2013-08-28
李秋生
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Existing methods of drying coal, such as lignite, are mostly used such as drum drying, fluidized bed drying, belt drying, vibration mixed flow drying, etc. The drying devices used in these drying methods have complex structures, low efficiency, and poor drying degrees.
For example, the particle size of coal in the fluidized bed dryer is limited, the degree of drying in the vibrating mixed flow bed is low, and the drum dryer or rotary drum dryer is used for drying raw coal, which is bulky and occupies a large area. , large dust, easy to explode, poor safety, low production capacity
[0006] In addition, the existing drying methods are all drying at a fixed temperature. During the heating process of lignite, the water vaporization inside the coal block causes the internal pressure of the coal block to rise. When the heating rate reaches a certain level, the water vaporization rate inside the coal block exceeds The diffusion speed of water vapor in the capillary from the inside to the outside, the internal pressure value is too high, resulting in the bursting of the coal block, and the bursting of the coal block brings four difficulties to the coal processing process:
[0007] ① Coal seam ventilation is difficult
The fine powder produced by lignite bursting and fragmentation deteriorates the ventilation of the coal pillar, and the airflow deviation is serious, resulting in low gas-solid heat transfer efficiency and uneven coal seam temperature.
[0008] ② The safety of the dry coal system is reduced
Lignite bursting and fragmentation produces a large amount of coal dust. During the drying process, the high concentration of coal dust is easily detonated by static sparks and open flames, resulting in disastrous consequences.
[0009] ③The difficulty of transportation increases
Therefore, the safety of lignite drying and upgrading system is reduced due to the large amount of fine powder produced by lignite explosion.
[0011] In addition, due to the limitations of existing mechanical equipment and heating capacity, large-scale production cannot

Method used

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Experimental program
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Effect test

Embodiment 1

[0033] figure 1 It is a structural schematic diagram of the coal drying device provided by Embodiment 1 of the present invention. The coal drying device provided by the present invention includes: a casing 1, at least three vibrating beds 2, and a radiant tube 3 with adjustable heating temperature; the inside of the casing 1 is isolated from the outside air; at least three vibrating beds 2 Arranged in a zigzag from top to bottom in the casing 1; each vibrating bed 2 is provided with a feeding port 4; each vibrating bed 2 is provided with the radiation tube 3 ; The heating temperature of the radiant tube 3 increases from top to bottom; wherein, the heating temperature of the radiant tube 3 at the bottom is 300°C-350°C.

[0034] In the coal drying device provided in the first embodiment, in the coal drying device provided above in the present invention, the coal drying device includes a casing 1, at least three vibrating beds 2, and a radiant tube 3 with adjustable heating temp...

Embodiment 2

[0036] see figure 1 as well as figure 2As shown, on the basis of the first embodiment above, the coal drying device provided by the second embodiment of the present invention also includes a water cooling jacket 5 and a distributor 6; the distributor 6 is located at the bottom of the vibration bed 2 Below the feeding port 4, and arranged in a zigzag shape with the vibrating bed 2 on the lowermost floor; the distributor 6 is provided with a plurality of lower leakage holes 7; the water cooling jacket 5 is located at the bottom of the distributor 6 Below, and in the water-cooling jacket 5, a plurality of cooling passages 8 extending vertically are formed; between the water-cooling jacket 5 and the distributor 6, a Sweeper 9.

[0037] In this second embodiment, since the temperature of the coal can reach 300°C-350°C when the coal is dried, in order to prevent the dry coal generated after the coal drying from burning at this temperature, it is necessary to lower the temperature...

Embodiment 3

[0042] figure 1 with image 3 It is a structural schematic diagram of the coal drying device provided by Embodiment 3 of the present invention. On the basis of the above-mentioned embodiment two, see figure 1 as well as image 3 As shown, in the coal drying device provided in the third embodiment, a water-cooled box 10 is also included; a water-cooled chamber 11 is formed in the water-cooled box 10 to communicate with the cooling channel 8 and the outside world; A screw pusher 12 for pushing the coal to the outside is also provided.

[0043] In the third embodiment, since the temperature of the dried coal needs to be rapidly lowered below the ignition point of the dried coal during the cooling process, in order to increase the cooling speed of the dried coal, a water-cooled box 10 is also added to the coal drying device. . The water-cooled box 10 forms a water-cooled chamber 11 that communicates with the cooling passage 8 and the outside world respectively. The side wall...

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Abstract

The invention relates to the field of chemical engineering, in particular to a coal drying device and drying method. The coal drying device comprises a machine casing, at least three vibration beds and radiation tubes with adjustable heating temperature. The inside of the machine casing is isolated from external air, at least three vibration beds are arranged in the machine casing from top to bottom in a zigzag type, each vibration bed is provided with a discharging port, the radiation tubes are arranged above the vibration beds, the radiation tubes are arranged from top to bottom, heating temperatures of the radiation tubes increase gradually, and the heating temperature of the radiation tube at the lowest layer is 300 DEG C to 350 DEG C. Coal can roll and fall on a plurality of layers of vibration beds in the coal drying device from top to bottom to be heated by the radiation tubes arranged on the vibration beds, the coal can increase from normal temperature to 300 DEG C-350 DEG C in a rolling and falling process, the coal can be dried in a heating process, volatile matters can be simultaneously prevented from being dissolved in quantity in a coal drying process, and the risk of coal crack is reduced.

Description

technical field [0001] The invention relates to the field of chemical industry, in particular to a coal drying device and a drying method. Background technique [0002] my country is a country with primary energy resources dominated by coal. Coal can provide more than 65% of primary energy. Coal production ranks first in the world and increases year by year. my country's recoverable reserves of coal resources rank third in the world, accounting for about 11.5% of the world's total reserves. Among them, lignite reserves account for about 16% of the world's total lignite reserves. With the increasing demand for energy and the over-exploitation of bituminous coal and anthracite resources, the development and utilization of lignite in my country will become more and more important. Compared with bituminous coal and anthracite, lignite has the advantages of low price and high reactivity, but its calorific value is relatively low, its water content is high, generally 25-60%, it ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F26B3/28F26B17/00
Inventor 李秋生
Owner 李秋生
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