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Operation method of liquid-solid fluidized bed coarse slime separation device with adjustable water velocity in height direction

A technology of height direction and separation device, applied in chemical instruments and methods, solid separation, wet separation, etc., can solve the problems of high ash fine mud pollution to clean coal, affecting separation effect, etc., and prolong separation time. , the effect of strong adaptability

Active Publication Date: 2017-12-12
LUOYANG MINING MACHINERY ENG DESIGN & RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the characteristics of the separation principle of the liquid-solid fluidized bed coarse coal slime separator, the high-ash fine mud in the feed will seriously pollute the clean coal. Desliming devices such as high-frequency screens and slime centrifuges, some high-ash fine mud still exists in the final clean coal, which affects the separation effect

Method used

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  • Operation method of liquid-solid fluidized bed coarse slime separation device with adjustable water velocity in height direction
  • Operation method of liquid-solid fluidized bed coarse slime separation device with adjustable water velocity in height direction

Examples

Experimental program
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Effect test

Embodiment 1

[0022]The outer wall of the fluidized bed cylinder 1 is provided with at least five sets of water discharge pipes 3 from top to bottom, and the conical water filling tank 2 is arranged under the fluidized bed cylinder 1, and the discharge valve 2-4 is arranged on one side of the outer wall of the water filling tank 2, and the water filling tank 2 The water distribution pipe 2-2 is arranged inside, and the trumpet-shaped sieve plate type fluid distributor 2-3 is arranged above the water distribution pipe 2-2; the feeding well 5 is arranged in the center above the fluidized bed cylinder 1, and the conical spreading material is arranged below the feeding well 5 A pair of feeding pipes 7 are arranged symmetrically on both sides of the disk 6 and the upper side of the feeding shaft 5. The overflow port of the fluidized bed cylinder 1 is equipped with an overflow concentrate collection mechanism 4 inclined at the bottom. The overflow concentrate collection mechanism 4 The concentrate...

Embodiment 2

[0028] The coarse coal slime classified in the previous process of the coal washing plant enters the feeding well 5 through the feeding pipe 7. The particle size of the coarse coal slime particles meets the effective particle size range of fluidized bed separation, and the coarse coal slime passes through the spreading plate 6. Evenly enter the fluidized bed cylinder 1, and at the same time, the frequency converter controls the pump to control the water speed entering the water inlet pipe 2-23. The water speed is a fixed value. After entering the water inlet pipe 2-23, the water passes through the annular water pipe 2-22 The hole on the upper surface enters the water-filled tank 2, and then enters the fluidized bed cylinder 1 through the fluid distributor 2-3 to form a stable upward water flow. The coarse coal slime particles in the fluidized bed cylinder 1 are mixed with water, due to the free settlement of the particles The speed is relatively large, and the coarse coal slime...

Embodiment 3

[0030] The water discharge valve 3-2 of the water discharge pipeline 3 is opened, and the high ash fine mud that is less than the effective particle size range value of the coarse coal slime particle fluidized bed sorting enters the water discharge pipeline 3 through the screen of the water inlet along the water flow, and the sieve The diameter of the net is 0.25mm, and the flow sensor 3-3 shows the amount of water flowing out, which is discharged through the water discharge main pipe 3-4. Due to the reduction of the water amount in the fluidized bed cylinder 1, the coarse coal slime particles in the fluidized bed cylinder 1 The concentration gradually increases from top to bottom along the height of the fluidized bed, the equal sedimentation ratio between particles increases, and the separation of coarse coal slime particles according to density is strengthened; the water discharge valve 3-2 of the water discharge pipe 3 is fine-tuned to control the water discharge and adjust t...

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Abstract

The operation method of the liquid-solid fluidized bed coarse coal slime separation device with adjustable water velocity in the height direction, the coarse coal slime enters the fluidized bed cylinder evenly through the spreading plate, and the coarse coal slime particles are gradually layered according to the final settlement velocity. The low-density coarse slime particles move upward into the overflow concentrate collection mechanism and are discharged from the concentrate discharge pipe to become concentrate. The high-density coarse slime particles move downward and enter the bottom of the fluidized bed cylinder. At the same time, the fluidization is adjusted through the water discharge pipe. The concentration of coarse slime particles in the bed cylinder increases the iso-sediment ratio between coarse slime particles; the controller controls the ore discharge actuator to automatically discharge ore; the frequency converter controls the pump to control the water speed entering the water inlet pipe, and adjusts the liquid-solid flow Sorting density of coarse coal slime by fluidized bed; prolonging the separation time of coarse coal slime in fluidized bed, strengthening coarse coal slime to be sorted according to density on the whole bed height, for difficult and extremely difficult separation Coal slime has obvious advantages over traditional fluidized bed coarse slime separator.

Description

technical field [0001] The invention relates to a high-efficiency separation device for coarse coal slime, in particular to an operation method of the coarse coal slime separation device for a liquid-solid fluidized bed with adjustable water velocity in the height direction. Background technique [0002] With the increasingly severe environmental situation in our country, more and more attention has been paid to the efficient and clean separation of coal. With the further improvement of coal mining mechanization, the fine-grained coal content in raw coal is increasing, and the upper limit of fine-grained coal separation particle size is reduced with the popularization and application of flotation columns. Crude. The sorting density of lump coal increases gradually with the decrease of particle size. Low-density fine-grained coal directly enters the clean coal without sorting, resulting in the back ash of the clean coal. In this way, the coarse coal between gravity separatio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B03B5/66
Inventor 谢彦君张平王艳梅张树辉马艳梅魏永杰姚敏娟张春艳王新博李思拓苏华伟刘明亮杨洪波阮健郝宏涛
Owner LUOYANG MINING MACHINERY ENG DESIGN & RES INST
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