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A kind of coarse coal slime sorting system and sorting method

A sorting system and technology for coarse coal slime, applied in chemical instruments and methods, solid separation, wet separation, etc., can solve the problem that the sorting method is difficult to operate, the processing capacity of the cyclone is not high, and it is not suitable for sorting treatment. and other problems, to achieve the effect of reducing the cost of coal preparation, reducing the cost of washing and reducing the number of equipment

Active Publication Date: 2015-09-23
JINYITONG SCI ANDTECH BEIJING CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, in the coarse coal slime separation methods commonly used at home and abroad, there are mainly TBS, water medium cyclone, spiral separator, etc. Among them, TBS is the most used, and the rising water flow is used as the separation power in the separation. In the water injection system, the sorting granularity is generally between 0.3 and 2 mm, and there is a high requirement for the concentration of the feed material. The conventional dehydration sieve water needs to be concentrated by the cyclone before being fed into the equipment, and the subsequent dehydration process is more complicated. Complicated, the whole system needs a certain height difference, and the system investment is large, which restricts some enterprises with small capital to choose this method, and in actual production, this sorting method is difficult to operate and the equipment is not easy to adjust; water medium swirl flow The device uses the difference in the radius of movement of slime particles of different densities under the action of centrifugal force to achieve separation. This method is relatively simple in system, less in investment, easy to operate, and has a wide separation size of 0.5-5mm. However, in practice In production, when the feed concentration is low, the separation effect is unsatisfactory, and the underflow "runs rough" often occurs, and the processing capacity of a single cyclone is not high, while the coal preparation plant with general production capacity has a large amount of slime water , which leads to the fact that when the equipment is selected, the quantity is often large, the operating power is large, and the investment is large, which is not suitable for direct separation of all the slime water in the system; the spiral separator is more commonly used in the field of domestic thermal coal separation. The separation density of this method is high, and it is difficult to achieve low-density separation, which limits the development of this method in the field of coking coal, and this method requires more auxiliary equipment in actual production, and has certain requirements for the height of the plant. Larger, in practical applications, it will also be limited by funds

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  • A kind of coarse coal slime sorting system and sorting method
  • A kind of coarse coal slime sorting system and sorting method
  • A kind of coarse coal slime sorting system and sorting method

Examples

Experimental program
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Effect test

Embodiment 1

[0023] Example 1, figure 1 Among them, a kind of coarse coal slime separation system of the present invention, it comprises hydraulic separation device 1, feeding material pump 2, hydrocyclone 3, dehydration device 4, flotation device 8, wherein said feeding material pump 2 The feed inlet of the feed pump is connected with the underflow outlet of the hydraulic separation device 1 through a pipeline, and the discharge outlet of the feed pump 2 is connected with the feed inlet of the hydrocyclone 3 through a pipeline. The overflow port of the hydrocyclone 3 is connected with the feed port of the dehydration device 4 through a pipeline, and the overflow port of the hydraulic separation device 1 is also connected with the feed port of the dehydration device 4 through a pipeline, so The bottom flow port of the dehydration device 4 is connected with the feed port of the flotation device 8 through a pipeline, and the bottom flow port of the hydrocyclone 3 is connected with the feed p...

Embodiment 2

[0025] Example 2, in figure 2 Among them, another coarse coal slime separation system of the present invention, wherein the shape, structure, and Materials, effects, etc. are as described in Example 1. The difference is that a concentrated cyclone 6 and a concentrated feed pump 5 are added in front of the dehydration device 4 in the system, and the feed inlet of the concentrated feed pump 5 is connected with the hydraulic separation device 1 and the concentrated feed pump 5 through a pipeline. The overflow port of the hydrocyclone 3 is connected, the discharge port of the concentrated feed pump 5 is connected with the feed inlet of the concentrated cyclone 6 through a pipeline, and the bottom flow port of the concentrated cyclone 6 The feed port of the dehydration device 4 is connected through a pipeline, and the overflow port of the concentration cyclone 6 is connected with the feed port of the flotation device 8 through a pipeline.

[0026] When this embodiment is working...

Embodiment 3

[0027] Example 3, in image 3 Among them, the third kind of coarse coal slime separation system, wherein the hydraulic separation device 1, feed pump 2, hydrocyclone 3, dehydration device 4, concentrated feed pump 5, concentrated cyclone 6, floating The shape, structure, material used, function, etc. of the selection device 8 are as described in Embodiment 2. The difference is that a classification device 7 is added between the bottom flow port of the hydrocyclone 3 and the flotation device 8 in the system, and the bottom flow of the classification device 7 passes through the pipeline and the feed of the flotation device 8. port connection. The classifying device 7 can be one of conventional technologies such as curved screen, linear screen, circular vibrating screen, electromagnetic screen, etc. in the prior art, or other equivalent alternative technologies and products.

[0028] When this embodiment is working, the working steps, methods, principles, etc. are as described ...

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Abstract

The invention discloses a coarse slime separating system and method, belongs to the field of coal separation, and particularly adaptable to direct separation of whole low-concentration slime water in the process of jigging coal separation. The system comprises a water power separating device, a feeding pump, a hydrocyclone, a dewatering device and a flotation device. Rough separation is performed on low-concentration slime water through the water power separating device, concentrated underflow of the water power separating device is separated through the hydrocyclone. By the aid of the coarse slime separating system and method, the whole low-concentration slime water can be separated directly, cost is reduced, system links are simplified, total system investment is reduced, and simple and practical effect that the existing coarse slime separating method cannot achieved is obtained.

Description

Technical field [0001] The invention relates to a coal slime sorting system and a sorting method, in particular to a coarse coal slime sorting system and a sorting method for sorting coarse coal slime. Background technique [0002] At present, in the coarse coal slime separation methods commonly used at home and abroad, there are mainly TBS, water medium cyclone, spiral separator, etc. Among them, TBS is the most used, and the rising water flow is used as the separation power in the separation. In the water injection system, the sorting granularity is generally between 0.3 and 2 mm, and there is a high requirement for the concentration of the feed material. The conventional dehydration sieve water needs to be concentrated by the cyclone before being fed into the equipment, and the subsequent dehydration process is more complicated. Complicated, the whole system needs a certain height difference, and the system investment is large, which restricts some enterprises with small ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B03B7/00
Inventor 常建勇
Owner JINYITONG SCI ANDTECH BEIJING CO LTD
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