UNDERGROUND COAL SEPARATION PROCESS

Abstract

Disclosed is an underground coal preparation process adopting a water medium, comprising: feeding exploited raw coal into a Φ25 mm raw coal classifying screen for screening; performing dry coal preparation on a classifying screen oversize product with a particle size greater than 25 mm and feeding a classifying screen undersize product with a particle size less than 25 mm into a special underground compact jigging machine for sorting to obtain jigging machine overflow clean coal, jigging middling coal and jigging gangue; screening and dewatering the jigging machine overflow clean coal to obtain a clean coal product, and screening and dewatering the jigging middling coal to obtain a middling coal product, sorting slime water to be sorted and generated during sorting to obtain coarse clean coal slime and coarse middling coal slime, and performing circulating water treatment on a final liquid.

Claims

1. An underground coal separation process adopting a water medium, comprising following steps: feeding an exploited raw coal into a Φ25 mm raw coal classifying screen by a raw coal feeding chute T for screening to obtain a classifying screen oversize product with a particle size greater than 25 mm and a classifying screen undersize product with a particle size less than 25 mm; feeding the classifying screen oversize product with a particle size greater than 25 mm into a TDS intelligent dry separator to perform a dry coal preparation, and separating to respectively obtain a dry separation clean coal and a dry separation gangue to be discharged; feeding the classifying screen undersize product with a particle size less than 25 mm into a special underground compact jigging machine for separation to obtain a jigging machine overflow clean coal, a jigging middling coal and a jigging gangue, and directly discharging the jigging gangue; due to a high water content of the jigging machine overflow clean coal, feeding the jigging machine overflow clean coal into a fixed screen for predewatering to obtain a clean coal fixed screen oversize product and an undersize water which is Φ1 mm clean coal fixed screen undersize water, feeding the undersize water into a first coal slime pool, feeding the clean coal fixed screen oversize product into a Φ13 mm classifying screen for screening to obtain an oversize block clean coal with a particle size greater than 13 mm and an undersize clean coal with a particle size less than 13 mm, discharging the oversize block clean coal with a particle size greater than 13 mm serving as a clean coal product, feeding the undersize clean coal with a particle size less than 13 mm into a clean coal centrifugal dewatering machine for dewatering to obtain a centrifugal dewatering machine clean coal and a first centrifugate, discharging the centrifugal dewatering machine clean coal serving as a clean coal product, and feeding the first centrifugate into the first coal slime pool; feeding the jigging middling coal into a Φ13 mm classifying screen for separation to obtain oversize middling coal with a particle size greater than 13 mm and undersize middling coal with a particle size less than 13 mm, discharging the oversize middling coal with a particle size greater than 13 mm directly serving as a middling coal product without further dewatering, feeding the undersize middling coal with a particle size less than 13 mm into a middling coal centrifugal dewatering machine for dewatering to obtain a dewatered middling coal and a second centrifugate, discharging the dewatered middling coal serving as a middling coal product, and feeding the second centrifugate into the first coal slime pool; and mixing the undersize water, the first centrifugate and the second centrifugate in the first coal slime pool to form a to-be-separated coal slime water containing coarse coal slime, feeding the to-be-separated coal slime water containing coarse coal slime into a water medium classifying and separation cyclone by a slurry pump, after separation, performing a first-section classification by the water medium classifying and separation cyclone to obtain an overflow, enabling cyclone a first-section underflow to enter a second-section separation to obtain an overflow containing coarse clean coal slime and an underflow containing coarse middling coal slime, feeding the overflow into a stirring barrel for stirring, adding a coal slime water treatment medicament which is a sedimentation-promoting medicament such as a flocculating agent, a coagulating agent and the like into the stirring barrel by a medicament adding box, completely mixing the overflow and the coal slime water treatment medicament in the stirring barrel P to obtain coal slime water, feeding the coal slime water into a roadway high-efficiency concentrator to perform sedimentation, discharging a concentrator underflow from an outlet at the bottom of the roadway high-efficiency concentrator after sedimentation, feeding the concentrator underflow into a coal slime filter press to perform filter pressing and dewatering to respectively discharge a coal slime and a filter press filtrate, discharging the filter press filtrate into a clarifying pool, discharging a concentrator overflow from an outlet above the concentrator and feeding the concentrator overflow into the clarifying pool; feeding the overflow containing coarse clean coal slime into a coarse clean coal sieve bend for screening and feeding the underflow containing coarse middling coal slime into a coarse middling coal sieve bend for screening to generate a coarse clean coal sieve bend undersize water and a coarse middling coal sieve bend undersize water respectively, feeding the coarse clean coal sieve bend undersize water and the coarse middling coal sieve bend undersize water into the first coal slime pool again, feeding the coarse clean coal sieve bend oversize product of the coarse clean coal sieve bend L and a coarse middling coal sieve bend oversize product of the coarse middling coal sieve bend into a coarse clean coal slime centrifugal dewatering machine and a coarse middling coal slime centrifugal dewatering machine respectively for dewatering to finally generate a coarse clean coal slime, a coarse middling coal slime a third centrifugate and a fourth centrifugate, and feeding the third centrifugate and the fourth centrifugate into the first coal slime pool to continuously circulate.

2. The underground coal separation process adopting a water medium according to claim 1, wherein a circulating water is generated in the clarifying pool and is fed into the special underground compact jigging machine by a clean water pump for use.

3. The underground coal separation process adopting a water medium according to claim 1, wherein a model of the special underground compact jigging machine is JYT-J series, a model of the roadway high-efficiency concentrator is YT-N series, and specific model parameters are determined according to a field process requirements.

4. The underground coal separation process adopting a water medium according to claim 1, wherein the dry separation gangue and the jigging gangue serving as backfill materials directly fill an underground without going up to a well, thereby reducing an environmental pollution.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0015] FIG. 1 is a process flow diagram of the present invention; and

[0016] FIG. 2 is a structural diagram of equipment according to the present invention.

[0017] In FIG. 1, 1—raw coal, 2—classifying screen oversize product with a particle size greater than 25 mm, 3—classifying screen oversize product with a particle size less than 25 mm, 4—TDS intelligent dry separator clean coal, 5—dry separation gangue, 6—jigging machine overflow clean coal, 7—jigging middling coal, 8—jigging gangue, 9—clean coal fixed screen oversize product, 10—undersize water (10), 11—block clean coal with a particle size greater than 13 mm, 12—undersize clean coal with a particle size less than 13 mm, 13—an oversize middling coal with a particle size greater than 13 mm, 14—undersize middling coal with a particle size less than 13 mm, 15—centrifugal dewatering machine clean coal, 16—centrifugate I, 17—dewatering middling coal, 18—centrifugate II, 19—to-be-separated coal slime water, 20—underflow containing coarse middling coal slime, 21—overflow containing coarse clean coal slime, 22—overflow, 23—coarse middling coal slime sieve bend oversize product, 24—coarse middling coal slime arc-shaped sieve bend undersize water, 25—coarse clean coal slime sieve bend oversize product, 26—coarse clean coal slime sieve bend undersize water, 27—coal slime centrifugal dewatering machine coarse middling coal slime, 28—coal slime centrifugal dewatering machine centrifugate, 29—coal slime centrifugal dewatering machine coarse clean coal slime, 30—coal slime centrifugal dewatering machine centrifugate, 31—coal slime water treatment medicament, 32—coal slime water, 33—concentrator underflow, 34—concentrator overflow water, 35—coal slime, 36—filter press filtrate, 37—circulating water.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0018] The specific implementations of the present invention are further described below in detail with reference to the accompanying drawings.

[0019] As shown in FIG. 1 and FIG. 2, the underground coal separation process adopting a water medium according to the present invention includes the following steps:

[0020] exploited raw coal 1 is fed into a Φ25 mm raw coal classifying screen A by a raw coal feeding chute T for screening to obtain a classifying screen oversize product 2 with a particle size greater than 25 mm and a classifying screen undersize product 3 with a particle size less than 25 mm;

[0021] the classifying screen oversize product 2 with a particle size greater than 25 mm is fed into a TDS intelligent dry separator B to perform dry coal preparation, and separation is conducted to respectively obtain dry separation clean coal 4 and dry separation gangue 5 to be discharged;

[0022] the classifying screen undersize product 3 with a particle size less than 25 mm is fed into a special underground compact jigging machine C for separation to obtain jigging machine overflow clean coal 6, jigging middling coal 7 and jigging gangue 8, and the jigging gangue 8 is directly discharged; due to high water content of the jigging machine overflow clean coal 6, the jigging machine overflow clean coal 6 is fed into a fixed screen D for predewatering to obtain a clean coal fixed screen oversize product 9 and undersize water 10 which is Φ1 mm clean coal fixed screen undersize water, the undersize water 10 is fed into a coal slime pool I, the clean coal fixed screen oversize product 9 is fed into a Φ13 mm classifying screen for screening to obtain oversize block clean coal 11 with a particle size greater than 13 mm and undersize clean coal 12 with a particle size less than 13 mm, the oversize block clean coal 11 with a particle size greater than 13 mm serving as a clean coal product is discharged, the undersize clean coal 12 with a particle size less than 13 mm is fed into a clean coal centrifugal dewatering machine G for dewatering to obtain centrifugal dewatering machine clean coal 15 and centrifugate I 16, the centrifugal dewatering machine clean coal 15 serving as a clean coal product is discharged, and feeding the centrifugate I 16 is fed into the coal slime pool I; the jigging middling coal 7 is fed into a Φ13 mm classifying screen F for separation to obtain oversize middling coal 13 with a particle size greater than 13 mm and undersize middling coal 14 with a particle size less than 13 mm, the oversize middling coal 13 with a particle size greater than 13 mm directly serving as a middling coal product is discharged without further dewatering, the undersize middling coal 14 with a particle size less than 13 mm is fed into a middling coal centrifugal dewatering machine H for dewatering to obtain dewatered middling coal 17 and centrifugate II 18, the dewatered middling coal 17 serving as a middling coal product is discharged, and the centrifugate II 18 is fed into the coal slime pool I; and

[0023] the undersize water 10, the centrifugate I 16 and the centrifugate II 18 are mixed in the coal slime pool I to form to-be-separated coal slime water 19 containing coarse coal slime, the to-be-separated coal slime water 19 containing coarse coal slime is fed into a water medium classifying and separation cyclone J by a slurry pump U, after separation, first-section classification is conducted by the water medium classifying and separation cyclone J to obtain overflow 22, cyclone first-section underflow enters second-section separation to obtain overflow 21 containing coarse clean coal slime and underflow 20 containing coarse middling coal slime, the overflow 22 is fed into a stirring barrel P for stirring, a coal slime water treatment medicament 31 which is a sedimentation-promoting medicament such as a flocculating agent, a coagulating agent and the like is added into the stirring barrel P by a medicament adding box 0, the overflow 22 and the coal slime water treatment medicament 31 are completely mixed in the stirring barrel P to obtain coal slime water 32, the coal slime water 32 is fed into a roadway high-efficiency concentrator Q to perform sedimentation, concentrator underflow 33 is discharged from an outlet at the bottom of the roadway high-efficiency concentrator Q after sedimentation, the concentrator underflow 33 is fed into a coal slime filter press R to perform filter pressing and dewatering to respectively discharge coal slime 35 and filter press filtrate 36, the filter press filtrate 36 is discharged into a clarifying pool S, concentrator overflow 34 is discharged from an outlet above the concentrator Q and the concentrator overflow 34 is fed into the clarifying pool S; the overflow 21 containing coarse clean coal slime is fed into a coarse clean coal sieve bend L for screening and the underflow 20 containing coarse middling coal slime is fed into a coarse middling coal sieve bend K for screening to generate coarse clean coal sieve bend undersize water 26 and coarse middling coal sieve bend undersize water 24 respectively, the coarse clean coal sieve bend undersize water 26 and the coarse middling coal sieve bend undersize water 24 is fed into the coal slime pool I again, a coarse clean coal sieve bend oversize product 26 of the coarse clean coal sieve bend L and a coarse middling coal sieve bend oversize product 23 of the coarse middling coal sieve bend K are fed into a coarse clean coal slime centrifugal dewatering machine N and a coarse middling coal slime centrifugal dewatering machine M respectively for dewatering to finally generate coarse clean coal slime 29, coarse middling coal slime 27, centrifugate IV 30 and centrifugate III 28, and the centrifugate IV 30 and the centrifugate III 28 is fed into the coal slime pool I to continuously circulate. Circulating water 37 is generated in the clarifying pool S and is fed into the special underground compact jigging machine C by a clean water pump V for use. The model of the special underground compact jigging machine C is JYT-J series, the model of the roadway high-efficiency concentrator Q is YT-N series, and the specific model parameters are determined according to the field process requirements. The dry separation gangue 5 and the jigging gangue serving as backfill materials 8 are directly filled underground without going up to the well, thereby reducing environmental pollution.