CN214714974U - Underground coal slurry water treatment system for coal mine - Google Patents
Underground coal slurry water treatment system for coal mine Download PDFInfo
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- CN214714974U CN214714974U CN202023296205.9U CN202023296205U CN214714974U CN 214714974 U CN214714974 U CN 214714974U CN 202023296205 U CN202023296205 U CN 202023296205U CN 214714974 U CN214714974 U CN 214714974U
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Abstract
The utility model belongs to the technical field of colliery is coal muddy water treatment in the pit. A coal slurry water treatment system in a coal mine well comprises a first solid-liquid separator, a coal water concentration device, a second solid-liquid separator, a pipeline conveying system and a control system which are sequentially arranged; the first solid-liquid separator comprises a first support frame, a screen body, an excitation motor and a water tank, and a first water outlet is formed in the water tank; the coal water concentration device comprises a tank body, a filter basket net and a scraping brush assembly which are arranged in the tank body, and the second solid-liquid separator comprises a base, a bottom grid cylinder, a sieve tray and a vibrating motor. The coal water separation can be realized before the coal slime water enters the water sump; the system can realize the coal water separation of the grade particles larger than 0.05 mm; after the larger particles are treated, the settling velocity of the particles smaller than 0.05mm is low, and the particles can enter a water sump pump in a suspension form and are conveyed to the ground. Can achieve the purpose that the slime of the sedimentation tank, the ditch and the sump is not cleaned for a long time.
Description
Technical Field
The utility model belongs to the technical field of colliery underground coal muddy water is handled, concretely relates to colliery underground coal muddy water processing system.
Background
The solid-liquid mixture (after the coal and rock powder are mixed with the working water and water gushing) generated by the operations of hydraulic punching of the bottom suction roadway, the excavation working face and the like is discharged along a drainage system. The following problems may be caused due to the gradual deposition of the solid mixture:
firstly, the drainage system is blocked, and the normal operation of the drainage system is influenced;
secondly, the coal-water mixture overflows to cause the dirty and poor roadway environment;
thirdly, a large amount of sediment in the water sump is deposited in a short time, the effective volume of the water sump is reduced, and potential safety hazards exist.
According to the requirements of coal mine safety regulations (the empty bin capacity of a water bin must be kept above 50% of the total capacity, sludge in the water bin, a sedimentation tank and a ditch must be cleaned in time, and the sludge must be cleaned 1 time before rainy season every year), if the thickness of coal slime is not cleaned, the effective volume of the water bin is occupied along with the increase of the accumulation, and potential safety hazards exist.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the problems and the defects, and provides a coal slurry water treatment system in a coal mine, which has reasonable integral design and can realize coal water separation before coal slurry water enters a sump; the system can realize the coal water separation of the grade particles larger than 0.05 mm; after the larger particles are treated, the settling velocity of the particles smaller than 0.05mm is low, and the particles can enter a water sump pump in a suspension form and are conveyed to the ground. Can achieve the purpose that the slime of the sedimentation tank, the ditch and the sump is not cleaned for a long time.
In order to realize the purpose, the adopted technical scheme is as follows:
a coal slurry water treatment system in a coal mine well comprises a first solid-liquid separator, a coal water concentration device, a second solid-liquid separator, a pipeline conveying system and a control system which are sequentially arranged;
the first solid-liquid separator comprises a first support frame, a screen body supported on the first support frame through an elastic support unit, an excitation motor arranged on the screen body, and a water tank fixedly arranged on the first support frame at the lower part of the screen body, wherein a first water outlet is formed in the water tank;
the coal water concentration device comprises a tank body, a filter basket net and a scraping brush component, wherein the filter basket net and the scraping brush component are arranged in the tank body, the filter basket net is cylindrical, a water outlet cavity is formed between the outer wall of the filter basket net and the inner wall of the tank body, a second water outlet communicated with the water outlet cavity is formed in the tank body, the scraping brush component is attached to the inner wall of the filter basket net, a first feed inlet is formed in the upper portion of the tank body, a first sewage discharge port is formed in the bottom of the tank body, an electric ball valve is arranged at the first sewage discharge port, and a differential pressure transmitter is arranged between the first feed inlet and the second water outlet;
the second solid-liquid separation machine comprises a base, a bottom grid barrel, a screen grid barrel and a vibrating motor, wherein the bottom grid barrel and the screen grid barrel are sequentially arranged on the base, the bottom grid barrel and the screen tray and the vibrating motor are arranged between the screen grid barrels, the bottom grid barrel and the base are connected and supported through damping springs, a second sewage discharge outlet is formed in the side portion of the screen grid barrel, a second feed inlet is formed in the top of the screen grid barrel, a third water outlet is formed in the side portion of the bottom grid barrel, and the second feed inlet corresponds to and is communicated with the first sewage discharge outlet.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, pipeline conveying system includes pipeline and the pump body, the pump body is at least one.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, the feed end of screen frame is comparatively the discharge end of screen frame is low the discharge end of screen frame is provided with the discharge gate, the elastic support unit is supporting spring the feed end of screen frame still is provided with the cloth case.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, be 0.4mm ~0.8mm under the mesh area on the screen frame.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, scrape material brush subassembly and be in including pivot, setting scrape material drive division and setting on the jar body and be in pivot scraper blade, the inner wall laminating of scraper blade and filter basket net, the scraper blade with be provided with head rod and second connecting rod in the pivot respectively, the head rod with the second connecting rod matches sliding connection the head rod with be provided with compression spring between the second connecting rod, the compression spring top pushes away the scraper blade with the filter basket net laminating.
According to the underground coal slurry water treatment system of the coal mine, preferably, the lower part of the sieve tray of the second solid-liquid separator is provided with a net cleaning ring; when the vibrating motor is started, the screen cleaning ring is used for beating the screen disc to clean materials.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, clear net ring includes the ring body and sets up beat piece on the ring body.
According to the coal mine underground coal slurry water treatment system, preferably, the mesh size of the screen of the coal water concentration device is 0.05mm-0.2 mm; and the mesh size of the sieve tray of the second solid-liquid separator is 0.03 mm-0.08 mm.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, control system includes control box, multiloop electromagnetic starter, flow sensor and level sensor, multiloop electromagnetic starter control opening of first solid-liquid separation machine, coal water enrichment facility, second solid-liquid separation machine and pipeline conveying system stops the action, flow sensor is used for detecting the pipeline flow of different district sections, level sensor is arranged in detecting the liquid level height in the corresponding equipment.
According to the utility model discloses colliery is coal muddy water processing system in pit, preferably, still includes feeding device, feeding device is mine car or band conveyer.
By adopting the technical scheme, the beneficial effects are as follows:
the coal water separation device is reasonable in structural design, and can realize coal water separation before the coal slime water enters the water sump; the system can realize the coal water separation of the grade particles larger than 0.05 mm; after the treatment of larger particles, the settling velocity of the particles smaller than 0.05mm is low, and the particles can enter a water sump in a suspension form and are conveyed to the ground through a water pump. Can achieve the purpose that the slime of the sedimentation tank, the ditch and the sump is not cleaned for a long time.
Through the design of the first solid-liquid separator, efficient slurry and water primary separation of the coal slime can be realized, the treatment capacity is large, the working efficiency is high, and the coal slime with large particle size is effectively filtered and continuously discharged; this application passes through coal water enrichment facility, can realize the further separation to the coal slime, at this in-process, can effectually filter out muddy water, go on muddy water, discharge viscous coal slime side by side, this application can carry out last coal slime mud-water separation work to viscous coal slime through second solid-liquid separation machine, thereby the water content in the guarantee coal slime obtains effectual reduction, so that carry out the belt feeder and carry, the drainage system's of also being convenient for simultaneously underground emission, the effectual volume pressure who alleviates the sump, the security of operation has been improved greatly, help keeping the sump in the pit, the unobstructed of sedimentation tank and ditch.
This application carries out the combination of different equipment through flow and handling capacity, coal slime water content according to the difference, has realized efficient mud-water separation, and this application all reaches continuous automation operation on arranging of treatment facility and treatment facility's connection control, more is applicable to borehole operation, and the practicality is strong.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings of the embodiments of the present invention will be briefly described below. The drawings are intended to depict only some embodiments of the invention, and not all embodiments of the invention are limited thereto.
FIG. 1 is a schematic structural diagram of a coal mine underground coal mud water treatment system according to the embodiment of the utility model.
Fig. 2 is a schematic structural diagram of a first solid-liquid separator according to an embodiment of the present invention.
Fig. 3 is a schematic structural diagram of a coal water concentrating device according to an embodiment of the present invention.
Fig. 4 is a schematic structural diagram of a second solid-liquid separator according to an embodiment of the present invention.
Fig. 5 is a control schematic diagram of the underground coal mine muddy water treatment system according to the embodiment of the utility model.
Number in the figure:
100 is a first solid-liquid separator, 101 is a first support frame, 102 is a sieve body, 103 is an excitation motor, 104 is a water tank, 105 is a first water outlet, 106 is an elastic support unit, 107 is a discharge hole, and 108 is a material distribution box;
200 is a coal water concentration device, 201 is a tank body, 202 is a filter basket net, 203 is a second water outlet, 204 is a first feed inlet, 205 is an electric ball valve, 206 is a first drain outlet, 207 is a differential pressure transmitter, 208 is a rotating shaft, 209 is a scraping driving part, 210 is a scraping plate, 211 is a first connecting rod, 212 is a second connecting rod, 213 is a compression spring, and 214 is a water outlet cavity;
300 is a second solid-liquid separator, 301 is a base, 302 is a bottom grid cylinder, 303 is a sieve grid cylinder, 304 is a sieve tray, 305 is a vibration motor, 306 is a damping spring, 307 is a second sewage discharge outlet, 308 is a second feed inlet, 309 is a third water outlet, 310 is a net cleaning ring, and 311 is a beating block;
401 is a pipe, 402 is a pump body.
Detailed Description
The embodiments of the present invention will be described more fully hereinafter with reference to the accompanying drawings, in which embodiments of the invention are shown. Unless defined otherwise, technical or scientific terms used herein shall have the ordinary meaning as understood by those of ordinary skill in the art.
In the description of the present invention, it is to be understood that the terms "first," "second," and the like are used for describing various elements of the present invention, and do not denote any order, quantity, or importance, but rather are used to distinguish one element from another.
It should be noted that when an element is referred to as being "connected," "coupled," or "connected" to another element, it can be directly connected, coupled, or connected, but it is understood that intervening elements may be present therebetween; i.e., positional relationships encompassing both direct and indirect connections.
It should be noted that the use of the terms "a" or "an" and the like do not necessarily denote a limitation of quantity. The word "comprising" or "comprises", and the like, means that the element or item listed before the word covers the element or item listed after the word and its equivalents, but does not exclude other elements or items.
It should be noted that terms indicating orientation or positional relationship such as "upper", "lower", "left", "right", and the like, are used only for indicating relative positional relationship, which is for convenience of describing the present invention, and not that the indicated device or element must have a specific orientation, be constructed and operated in a specific orientation; when the absolute position of the object to be described is changed, the relative positional relationship may also be changed accordingly.
Referring to fig. 1-4, the application discloses a coal slurry water treatment system in a coal mine well, which comprises a first solid-liquid separator 100, a coal water concentration device 200, a second solid-liquid separator 300, a pipeline conveying system and a control system which are sequentially arranged; the first solid-liquid separator 100 comprises a first support frame 101, a screen body 102 supported on the first support frame 101 through an elastic support unit 106, an excitation motor 103 arranged on the screen body 102, and a water tank 104 fixedly arranged on the first support frame 101 at the lower part of the screen body 102, wherein a first water outlet 105 is arranged on the water tank 104; the coal water concentration device 200 comprises a tank body 201, a filter basket net 202 and a scraping brush assembly, wherein the filter basket net 202 is arranged in the tank body 201, the filter basket net 202 is cylindrical, a water outlet cavity 214 is formed between the outer wall of the filter basket net 202 and the inner wall of the tank body 201, a second water outlet 203 communicated with the water outlet cavity 214 is arranged on the tank body 201, the scraping brush assembly is attached to the inner wall of the filter basket net 202, a first feed inlet 204 is also arranged at the upper part of the tank body 201, a first sewage discharge port 206 is arranged at the bottom of the tank body 201, an electric ball valve 205 is arranged at the first sewage discharge port 206, and a differential pressure transmitter 207 is arranged between the first feed inlet 204 and the second water outlet 203; the second solid-liquid separator 300 comprises a base 301, a bottom grid cylinder 302 and a screen grid cylinder 303 which are sequentially arranged on the base 301, a screen tray 304 arranged between the bottom grid cylinder 302 and the screen grid cylinder 303, and a vibration motor 305, wherein the bottom grid cylinder 302 and the base 301 are connected and supported through a damping spring 306, a second sewage discharge outlet 307 is arranged on the side portion of the screen grid cylinder 303, a second feed inlet 308 is arranged at the top of the screen grid cylinder 303, a third water outlet 309 is arranged on the side portion of the bottom grid cylinder 302, and the second feed inlet 308 is correspondingly communicated with the first sewage discharge outlet 206.
The pipeline conveying system comprises a pipeline 401 and a pump body 402, and the pump body 402 is at least one.
The feeding end of the screen body 102 is lower than the discharging end of the screen body, a discharging hole 107 is arranged at the discharging end of the screen body, the elastic supporting unit 106 is a supporting spring, and a cloth box 108 is further arranged at the feeding end of the screen body 102.
The mesh belt on the screen body 102 is 0.4 mm-0.8 mm below the mesh belt.
The scraping brush component comprises a rotating shaft 208, a scraping driving part 209 arranged on the tank body 201 and a scraping plate 210 arranged on the rotating shaft 208, the scraping plate 210 is attached to the inner wall of the filter basket net 202, the scraping plate 210 and the rotating shaft 208 are respectively provided with a first connecting rod 211 and a second connecting rod 212, the first connecting rod 211 and the second connecting rod 212 are in matched sliding connection, a compression spring 213 is arranged between the first connecting rod 211 and the second connecting rod 212, and the compression spring 213 pushes the scraping plate 210 to be attached to the filter basket net 202.
A screen cleaning ring 310 is arranged at the lower part of the screen disc 304 of the second solid-liquid separator 300; when the vibration motor 305 is started, the screen cleaning ring beats the screen tray for cleaning materials. Specifically, the net clearing ring 310 in the present embodiment includes a ring body and a patting block 311 provided on the ring body.
The mesh size of the screen of the coal water concentration device 200 is 0.05mm-0.2 mm; the mesh size of the screen disc of the second solid-liquid separator is 0.03 mm-0.08 mm.
The control system comprises a control box, a multi-loop electromagnetic starter, a flow sensor and a liquid level sensor, wherein the multi-loop electromagnetic starter controls the start and stop actions of the first solid-liquid separator, the coal-water concentration device, the second solid-liquid separator and the pipeline conveying system, the flow sensor is used for detecting the pipeline flow of different sections, and the liquid level sensor is used for detecting the liquid level height in corresponding equipment.
The coal slime dewatering device is characterized by also being provided with a material conveying device, wherein the material conveying device is a mine car or a belt conveyor, and the dehydrated coal slime is conveyed through the mine car or the belt conveyor.
This application sets up one set as above-mentioned colliery underground coal slime water processing system between the sump, realizes the source and handles, handles to the coal slime water and reaches to realize the coal water separation, reduces the sump coal slime and subsides, solves or replaces artifical clearance sump, purposes such as reduction intensity of labour.
The application processes the source water level step by step. Specifically, according to the working characteristics of the equipment, the coal water separation of the particles with the grade of more than 0.5mm is realized through a first solid-liquid separator in the first step, the coal water separation of the particles with the grade of less than 0.5mm is realized through a coal water concentration device and a second solid-liquid separator in the second step, and a plurality of equipment are related to form a solid-liquid separation treatment production line; the work of coarse separation, fine separation, dehydration and the like of the coal-water mixture with high flow, low concentration and fine particles is realized.
Specifically, slime water is sequentially passed through a first solid-liquid separator to remove particles with the particle size of more than 0.5mm, a coal water concentrating device is used for concentrating undersize materials of the first solid-liquid separator, particles with the particle size of 0.05-0.5mm are removed by a second solid-liquid separator, and undersize materials of the second solid-liquid separator enter a water sump.
Further details of the structure and process are provided below with respect to specific implementations:
a shunt pipeline system: because of the gradient of the drainage tunnel, the drainage ditch naturally has a certain inclination angle, the water from the source has a certain flow velocity, the flow velocity is estimated to be 0.5-1m/s by field observation, and a DN400 pipeline is selected as a diversion pipeline according to a diameter selection table of an outdoor drainage pipeline. And (3) pumping and selecting types: the coarse particle passing performance is high, the flow rate is selected to be 200m3/h, and the head loss is small because the first solid-liquid separator and the ditch are installed nearby. The impeller adopts a wide flow passage design and has strong solid passing capacity.
A first solid-liquid separator: because the coal particle proportion of the source slime water with the diameter of more than 0.5mm reaches 82.6%, the first solid-liquid separator is selected to realize coarse separation, large-particle coal is firstly separated, the workload of a subsequent coal water concentration device is reduced, and the treatment efficiency is improved.
The working principle of the first solid-liquid separator is as follows: feeding the coal slime water to a screen, and separating the coal and the water through beating and gravity; by means of the deflection blocks at the two ends of the motor shaft, the rotary motion of the motor is converted into the horizontal and vertical motions of the screen body, and then materials on the screen move forwards to realize the functions of discharging and unloading.
The structure of the first solid-liquid separator is as follows: as shown in fig. 2, the screen comprises a cloth box, an excitation motor, a screen body, a first support frame, a water tank and the like. The coal particles are conveyed to a first solid-liquid separator by a diversion pipeline or a pump, the equipment precision is 0.5mm, namely the screening of the coal particles with the size of more than 0.5mm is realized by the equipment, and the screened coal particles are vibrated to a transfer belt conveyor or a mine car; and separating out coal slime mixed liquid with the diameter of less than 0.5mm, entering an undersize water tank or a buffer pool at the lower part of the coarse separator, and pumping the coal slime mixed liquid to a coal water concentration device by a residue slurry pump.
The working parameters of the first solid-liquid separator are as follows:
processing capacity: 250m3/h；
Screen mesh precision: 0.5 mm;
motor power: 2X 2.2 kw.
A pump body: the slurry pump is used for pumping coarsely divided slurry (the particle size is less than 0.5 mm) into a coal water concentration device, the flow rate of screened slurry is 190m3/h, the concentration is 0.55%, based on coal water and coal slurry particles at the source of a coal mine, the abrasion is large, the slurry pump selects Cr28 as a material of a flow passage piece, the abrasion resistance is excellent, the hardness is HRC55-60, the slurry is highly abraded by coarse particle strong abrasion resistance, the flow rate is more than 200m3/h, as a first solid-liquid separator and a ditch are installed nearby, and the coal water concentration device needs excess pressure to press filtered materials out of equipment, the pump lift at the position is more than 40 m.
Pump body parameters:
flow rate: 200m3/h；
Lift: 60 m;
the material of the flow passage piece: cr 28;
motor power: 55 kw.
Coal water enrichment facility: because the coal content of the coal slime water after coarse separation is less, the coal particle size is smaller (the particle size is less than 0.5 mm), and common screening is difficult, a coal water concentration device with fine particle screening capacity is designed and selected to concentrate coal particles with the particle size of less than 0.5 mm. The device is used for filtering particulate matters in the coal water, and achieves the purpose of concentration. The concentrating device can filter raw coal water and clean and discharge the filter screen, the system supplies water continuously when cleaning and discharging the sewage, and the filtering process is carried out continuously.
The working principle of the coal water concentration device is as follows: when the coal slurry filter works, low-concentration coal water enters from the medium inlet and passes through the coal slurry particles through the stainless steel filter basket net. The water purification flows out from the medium outlet, when the particulate matters are gathered too much on the inner wall of the filter basket net, the filtering is not smooth, the pressure of the cavity rises, when the pressure difference value of the inlet and outlet water reaches a certain value (preset), the pressure difference switch sends a signal to the controller, and the controller starts the speed reducer motor to drive the inner stainless steel scraping brush to rotate and brush off the attached particulate matters. The controller opens the electric blow-down valve at the same time to discharge particles, the cleaning time is about 1 minute, the flow cutting is not needed during the self-cleaning period, the pressure loss of blow-down is not more than 0.05MPa, and the flow loss is not more than 1%.
The coal slurry water flow roughly separated by the first solid-liquid separator is pumped to a coal water concentration device through a pump body, and the relation between the filtering precision and the treatment capacity is combined, wherein the design and the selection precision are 0.1mm, and the treatment capacity is 250m3A coal water concentration device. Coal particles with the particle size of 0.05-0.5mm can be separated to form coal slurry, the coal slurry is discharged from a sewage discharge outlet, and the sewage discharge outlet is connected to a medium inlet of mining solid-liquid separator (fine separation) equipment through a pipeline. And the coal slime mixed liquor with the particle size of less than 0.1mm is discharged from the medium outlet, and the medium outlet extends to the drainage ditch through a pipeline. The medium outlet and the sewage draining outlet discharge power which is from the pressure of the medium inlet water pump, and a sewage draining pump or a water draining pump is not required to be additionally arranged.
Parameters of the coal water concentration device:
processing capacity: 250m3/h；
And (3) processing precision: 0.1 mm;
designing pressure: 1 MPa;
power of the stirring motor: 0.75 kw.
A second solid-liquid separator: the coal slurry (with the grain diameter of 0.05-0.5 mm) discharged from the sewage outlet of the coal water concentration device has the flow rate of 40m3The water content is more than 90%, the water content is high, the belt conveyor is inconvenient to transport, and a second solid-liquid separator is needed for dehydration, so that the belt conveyor is suitable for conveying conditions of the belt conveyor.
The working principle of the second solid-liquid separator is as follows: by vertical type vibrating motor as the excitation source, eccentric excitation piece is installed at vibrating motor upper and lower both ends, changes the rotary motion of motor into the level, the cubic element motion of perpendicular and slope, forms the vibration action of three dimension, drives the screen disc vibration, drives the vibration of material and clear net ring then, and wherein the vibration of clear net ring is the reverse slapping to the screen cloth bottom surface to avoid or reduce the possibility of tiny coal slime adhesive net blocking of oil, keep the permeability of screen cloth. The moving speed and the track of the materials on the screen surface can be changed by adjusting the weight and the included angle of the upper eccentric excitation block and the lower eccentric excitation block.
The design selects a separator with the precision of 0.05mm and the processing capacity of 50m3The coal slurry (with the particle size of 0.1-0.5 mm) is dehydrated, so that the dehydration is satisfied, the coal slurry particles and the precision thereof are not affected, the water content can be reduced to 20-25%, and the dehydrated coal slurry is conveyed to a transfer belt conveyor or a mine car; the separated water enters a drainage ditch.
Parameters of the second solid-liquid separator:
processing capacity: 50m3/h；
Screen mesh precision: 0.05 mm;
motor power: 1 x 1.5 kw.
An outward transportation system: and the solid coal slime material screened by the first solid-liquid separator and the second solid-liquid separator is transferred to the existing mine car of the coal mine.
The system control basically comprises the following components:
the system control element comprises:
1.1, a multi-loop electromagnetic starter (QJZ-120/1140 (660) -4) is adopted to drag a pump body and a coal water concentration device;
1.2, dragging two solid-liquid separators by adopting a multi-loop electromagnetic starter (QJZ-60/1140 (660) -4);
1.3, a mining explosion-proof and intrinsically safe electrical control box (KXJ-5/127) is adopted, a PLC logic control device is arranged in the electrical control box, the electrical control box is the core of the whole system, and analog signals of the field sensor for detecting flow, liquid level and the like are collected; collecting operation and fault signals of field equipment; the actions of the respective devices are directed.
1.4 the action of a mining intrinsic safety type operating platform (TH series) remote control device is adopted.
1.5 detecting various kinds of information on the site by adopting flow sensors, liquid level sensors and the like.
The system control mode is as follows: the control mode of the application is divided into an automatic working mode and a manual working mode. The automatic mode is that the PLC acquires various signals, and the whole processes of pump starting, water pumping, screening and conveying are reasonably determined according to the process flow of source water treatment, and the whole process does not need manual intervention under the automatic mode. The manual mode is that any equipment is operated singly to release the locking relation among the equipment.
Thirdly, automatic configuration and functions of underground equipment:
3.1 automatic function: the inlet high-performance PLC controller is adopted, the whole processes of vacuumizing, selecting a drainage pipeline by opening a gate valve and starting a pump to pump water are automatically completed according to the water level of the water tank or the buffer pool and the drainage process flow, and automatic water pumping, screening, conveying and the like are realized.
3.2 communication function: the system has a network communication interface, can realize remote monitoring and control, and can be conveniently in barrier-free connection with the mine automatic monitoring system.
3.3 protection function: has the functions of fault alarm, automatic protection and the like. 3.3.1 Motor protection: the system is provided with electric protection faults of motor under-voltage, over-current, short circuit and the like. 3.3.2 drainage system process protection: the system is arranged according to the drainage process requirement: the water pump is protected by the vacuum degree of the water suction pipe, the flow detection of the drain pipe and the like.
3.4 function structure of each device of the control system:
the master device control system includes: the low-voltage mining flameproof and intrinsically safe low-voltage electromagnetic starter comprises a low-voltage mining flameproof and intrinsically safe low-voltage electromagnetic starter, a PLC (programmable logic controller) flameproof control box, an equipment centralized operation console, a peripheral sensor and the like.
3.5 starting control device: the main drainage equipment adopts a control mode of a low-voltage mining explosion-proof and intrinsically safe low-voltage electromagnetic starter. QJZ series mining flame-proof and intrinsically safe low-voltage electromagnetic starter: rated voltage: 660/1140V; the mining explosion-proof and intrinsically safe low-voltage electromagnetic starter has the following functions: the vacuum contactor and the voltage (current) transformer are integrally installed; the device has the functions of grounding, undervoltage, overvoltage, three-phase imbalance, overload short circuit, phase failure, insulation monitoring and the like; the monitoring system is provided with an RS-485 or CAN bus interface and CAN realize communication with an upper computer of the monitoring system.
3.6PLC explosion suppression control box: the PLC control box is of a mining explosion-proof type. The PLC control box mainly comprises a programmable controller, a signal transmitter, an intermediate relay, a safety grid and the like, mainly completes the transformation and amplification of signals, and sends out various control signals through the operation and judgment of the PLC to monitor the operation condition of the water pump. The high-performance PLC originally installed and imported is selected, and the I/O interface of the PLC should be not less than 20% of the spare amount.
The 3.7 sensors include water level sensors, flow sensors, etc.
While the above description has described in detail the preferred embodiments for carrying out the invention, it should be understood that these embodiments are presented by way of example only, and are not intended to limit the scope, applicability, or configuration of the invention in any way. The scope of the invention is defined by the appended claims and equivalents thereof. Many modifications may be made to the foregoing embodiments by those skilled in the art in light of the teachings of the present disclosure, and such modifications are intended to be within the scope of the present disclosure.
Claims (10)
1. A coal mine underground coal muddy water treatment system is characterized by comprising a first solid-liquid separator, a coal water concentration device, a second solid-liquid separator, a pipeline conveying system and a control system which are sequentially arranged;
the first solid-liquid separator comprises a first support frame, a screen body supported on the first support frame through an elastic support unit, an excitation motor arranged on the screen body, and a water tank fixedly arranged on the first support frame at the lower part of the screen body, wherein a first water outlet is formed in the water tank;
the coal water concentration device comprises a tank body, a filter basket net and a scraping brush component, wherein the filter basket net and the scraping brush component are arranged in the tank body, the filter basket net is cylindrical, a water outlet cavity is formed between the outer wall of the filter basket net and the inner wall of the tank body, a second water outlet communicated with the water outlet cavity is formed in the tank body, the scraping brush component is attached to the inner wall of the filter basket net, a first feed inlet is formed in the upper portion of the tank body, a first sewage discharge port is formed in the bottom of the tank body, an electric ball valve is arranged at the first sewage discharge port, and a differential pressure transmitter is arranged between the first feed inlet and the second water outlet;
the second solid-liquid separation machine comprises a base, a bottom grid barrel, a screen grid barrel and a vibrating motor, wherein the bottom grid barrel and the screen grid barrel are sequentially arranged on the base, the bottom grid barrel and the screen tray and the vibrating motor are arranged between the screen grid barrels, the bottom grid barrel and the base are connected and supported through damping springs, a second sewage discharge outlet is formed in the side portion of the screen grid barrel, a second feed inlet is formed in the top of the screen grid barrel, a third water outlet is formed in the side portion of the bottom grid barrel, and the second feed inlet corresponds to and is communicated with the first sewage discharge outlet.
2. The coal mine underground muddy water treatment system as claimed in claim 1, wherein said pipeline conveying system comprises at least one of a pipeline and a pump body.
3. The underground coal mine muddy water treatment system according to claim 1, wherein the feed end of the screen body is lower than the discharge end of the screen body, a discharge hole is formed in the discharge end of the screen body, the elastic support unit is a support spring, and a material distribution box is further arranged at the feed end of the screen body.
4. The underground coal mine muddy water treatment system as claimed in claim 1, wherein the mesh belt on the screen body is 0.4 mm-0.8 mm below.
5. The underground coal mine muddy water treatment system according to claim 1, wherein the scraping brush assembly comprises a rotating shaft, a scraping driving part arranged on the tank body, and a scraping plate arranged on the rotating shaft, the scraping plate is attached to the inner wall of the filter basket net, a first connecting rod and a second connecting rod are respectively arranged on the scraping plate and the rotating shaft, the first connecting rod and the second connecting rod are in matched sliding connection, a compression spring is arranged between the first connecting rod and the second connecting rod, and the compression spring pushes the scraping plate to be attached to the filter basket net.
6. The underground coal mine muddy water treatment system according to claim 1, wherein a screen cleaning ring is arranged at the lower part of the screen disc of the second solid-liquid separator; when the vibrating motor is started, the screen cleaning ring is used for beating the screen disc to clean materials.
7. The coal mine underground muddy water treatment system as claimed in claim 6, wherein said cleaning net ring comprises a ring body and a patting block arranged on said ring body.
8. The underground coal mine muddy water treatment system as claimed in claim 1, wherein the mesh size of the screen of the coal water concentration device is 0.05mm-0.2 mm; and the mesh size of the sieve tray of the second solid-liquid separator is 0.03 mm-0.08 mm.
9. The underground coal mine muddy water treatment system according to claim 1, wherein the control system comprises a control box, a multi-loop electromagnetic starter, a flow sensor and a liquid level sensor, the multi-loop electromagnetic starter controls starting and stopping actions of the first solid-liquid separator, the coal-water concentration device, the second solid-liquid separator and the pipeline conveying system, the flow sensor is used for detecting pipeline flow of different sections, and the liquid level sensor is used for detecting liquid level height in corresponding equipment.
10. The underground coal mine muddy water treatment system as claimed in claim 1, further comprising a material conveying device, wherein the material conveying device is a mine car or a belt conveyor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023296205.9U CN214714974U (en) | 2020-12-31 | 2020-12-31 | Underground coal slurry water treatment system for coal mine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023296205.9U CN214714974U (en) | 2020-12-31 | 2020-12-31 | Underground coal slurry water treatment system for coal mine |
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| CN214714974U true CN214714974U (en) | 2021-11-16 |
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| CN202023296205.9U Active CN214714974U (en) | 2020-12-31 | 2020-12-31 | Underground coal slurry water treatment system for coal mine |
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| Country | Link |
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| CN (1) | CN214714974U (en) |
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Inventor after: Liu Kaifei Inventor after: Zhao Jingmin Inventor after: Yang Qinghe Inventor after: Wang Dan Inventor after: Qin Zhiqiang Inventor after: Li Xinlei Inventor after: Chen Xiqing Inventor after: Chang Haixiao Inventor after: Ming Zhaojie Inventor after: Wang Jinfeng Inventor after: Sui Zhi Inventor after: Cai Qingfeng Inventor before: Liu Kaifei Inventor before: Zhao Jingmin Inventor before: Yang Qinghe Inventor before: Wang Dan Inventor before: Qin Zhiqiang Inventor before: Li Xinlei Inventor before: Chen Xiqing Inventor before: Chang Haixiao Inventor before: Ming Zhaojie Inventor before: Wang Jinfeng Inventor before: Sui Zhi Inventor before: Cai Qingfeng |
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