CN212228665U - Device for simulating agglomeration and dispersion behaviors of coal powder in supporting crack - Google Patents
Device for simulating agglomeration and dispersion behaviors of coal powder in supporting crack Download PDFInfo
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- CN212228665U CN212228665U CN202020424434.5U CN202020424434U CN212228665U CN 212228665 U CN212228665 U CN 212228665U CN 202020424434 U CN202020424434 U CN 202020424434U CN 212228665 U CN212228665 U CN 212228665U
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Abstract
The utility model provides a coal powder reunion and dispersion behavior's analogue means in supporting the crack, analogue means includes injection system, visual support crack system, discharge system, computer analytic system, and wherein, injection system and visual support crack system are connected, and visual support crack system is connected with discharge system, and discharge system and visual support crack system are connected with computer analytic system respectively. The utility model has the advantages that: the simulation device can simulate the dispersion and agglomeration behaviors of the coal powder in the supporting cracks under the conditions of different formation pressures, different flow rates, different coal powder contents, different supporting crack forms, different inclination angles and the like, and evaluate the influence of the coal powder on the flow conductivity of the supporting cracks and the disturbance of the coal powder movement on the fluid pressure in the supporting cracks; the simulation is strong, the integration level is high, and the simulation result can effectively guide the production practice of the coal-bed gas well.
Description
Technical Field
The utility model relates to a simulation device especially relates to a coal dust reunion and dispersion behavior's simulation device in supporting crack.
Background
China has huge reserves of coal bed gas resources and is the third place in the world. The coal bed gas is a clean energy, and the development and utilization of the coal bed gas are beneficial to environmental protection, can supplement energy gaps in China and guarantee the safe production of coal mines. At present, two industrial bases of the coal bed gas in the east of the Qin basin and the Ordos basin are built in China, and meanwhile, the coal bed gas development potential in areas such as Xinjiang southwest and inner Mongolia two-connected basins is huge, so that the method is a strategic take-over area for future coal bed gas development in China. Due to deposition and construction reasons, coal reservoirs in partial regions have large inclination angle changes and exist from horizontal to nearly vertical.
In the process of developing the coal bed gas, fracturing modification needs to be carried out on a coal reservoir, a diversion crack (a supporting crack for short) supported by a propping agent such as quartz sand or ceramsite and the like is formed in the coal reservoir, then fracturing fluid and formation water are returned to the ground from the supporting crack through a shaft, and along with the discharge of fluid, the coal bed gas is desorbed and produced after the fluid pressure of the reservoir is reduced to the coal bed gas critical desorption pressure. In the initial stage of drainage and production, the flow-back fluid is a single-phase flow, namely almost all the drained and produced liquid is fracturing fluid and formation water; in the middle period of drainage and mining, along with the production of the coal bed gas, the fluid is changed into gas-liquid two-phase flow, and the formation water and the coal bed gas are jointly mined; in the later stage of drainage and production, formation water is reduced, the gas phase content of the coal bed gas is dominant, but coal dust can be generated by mechanical polishing of a drilling tool, a propping agent and the like on a coal reservoir, and the coal reservoir contains natural coal dust, so that in the drainage and production process, the coal dust enters a propping fracture under the carrying action of fracturing fluid or formation water in different states (dispersion and aggregation) to block a propping agent gap, thereby inhibiting fluid output, causing reservoir damage and severely restricting and influencing the productivity of a coal bed gas well. Therefore, the simulation of the agglomeration and dispersion state of the coal powder and the evaluation of the influence of the coal powder on the supporting fracture are particularly important.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model provides a coal powder reunion and dispersion action's analogue means in supporting crack for the simulation is under different lamination pressure, flow, buggy content, supporting crack form and inclination, the dispersion-reunion action of buggy in supporting crack, and the disturbance of the fluid pressure in the supporting crack of water conservancy diversion ability and the coal powder motion of evaluation supporting crack.
The utility model provides a coal powder agglomeration and dispersion behavior simulation device in a supporting crack, which comprises an injection system, a visual supporting crack system, a discharge system and a computer analysis system, wherein the visual supporting crack system is communicated with the injection system and the discharge system through a connecting pipeline (3), and the computer analysis system is used for acquiring and analyzing the data of the agglomeration and dispersion behavior of the coal powder in the visual supporting crack system;
the injection system comprises a water tank (1), a water pump (2), a three-way connector (8) and an air source (13), wherein a dispersion system formed by mixing pure liquid and pulverized coal is filled in the water tank (1); the water pump (2), the air source (13) and the visual supporting crack system are communicated together through the three-way connector (8) and the connecting pipeline (3), the water pump (2) is placed in the water pool (1), and the dispersion system in the water pool (1) is pressed into the connecting pipeline (3);
the visual supporting fracture system comprises a supporting fracture simulation device (16), a support (17) used for lifting and fixing the supporting fracture simulation device (16), a simulation propping agent (38) used for filling the supporting fracture simulation device (16), a first camera (18) and a second camera (19) which are arranged on the outer surface of the supporting fracture simulation device (16), and a first pressure sensor (20) and a second pressure sensor (21) which are arranged on the inner wall of the supporting fracture simulation device (16), wherein the front end of the supporting fracture simulation device (16) is connected with the injection system, and the rear end of the supporting fracture simulation device is connected with the discharge system; the support (17) is movably arranged at the middle section of the supporting crack simulating device (16), the height of the support (17) is adjustable, and the supporting crack simulating device (16) can rotate around the support (17) by 0-180 degrees;
the discharge system comprises a solid-liquid separator (30), a high-precision electronic scale (32) and a liquid collecting tank (35), wherein the solid-liquid separator (30) is used for filtering and retaining coal dust produced after passing through the supporting crack simulation device (16), and an upper end port of the solid-liquid separator (30) is communicated with the rear end of the supporting crack simulation device (16) through a connecting pipeline (3); the liquid collecting pool (35) is arranged below the solid-liquid separator (30) and is used for collecting liquid separated by the solid-liquid separator (30); and the high-precision electronic scale (32) is used for weighing the mass of the pulverized coal filtered out by the solid-liquid separator (30).
Further, the injection system further comprises a first regulating valve (4), a first pressure gauge (5), a first flow meter (6), a first one-way valve (7), a second one-way valve (9), a second flow meter (10), a second pressure gauge (11), a second regulating valve (12), a third flow meter (14) and a third pressure gauge (15), wherein a liquid phase outlet end of the water pump (2) is connected with the first regulating valve (4), one end of the three-way connector (8) communicated with the water pump (2) is connected with the first one-way valve (7), and the first pressure gauge (5) and the first flow meter (6) are installed on a connecting pipeline (3) between the first regulating valve (4) and the first one-way valve (7);
the air source (13) is connected with the second regulating valve (12), one end of the three-way connector (8) communicated with the air source (13) is connected with the second one-way valve (9), and the second flowmeter (10) and the second pressure gauge (11) are arranged on the connecting pipeline (3) between the second regulating valve (12) and the second one-way valve (9);
the third flow meter (14) and the third pressure meter (15) are arranged on a connecting pipeline (3) of the three-way connector (8) and the visual support fracture system.
Further, the discharge system further comprises a fourth flow meter (26), a fourth pressure gauge (27), a third regulating valve (28) and a third one-way valve (29), wherein an upper end port of the solid-liquid separator (30) is sequentially connected with the third one-way valve (29), the third regulating valve (28), the fourth pressure gauge (27), the fourth flow meter (26) and the rear end of the support fracture simulation device (16) through a connecting pipeline (3).
Further, the computer analysis system comprises a first external memory (22) connected with the first pressure sensor (20) through a data cable (24), a second external memory (23) connected with the second pressure sensor (21) through the data cable (24), and a computer (25) installed with particle image analysis software, wherein the first external memory (22), the second external memory (23), the first camera (18) and the second camera (19) are all connected with the computer (25) through the data cable (24).
Further, the computer analysis system also comprises a slide (33) and a microscope (34), wherein the slide (33) comprises a glass slide and a cover glass and is used for placing the coal dust sample filtered out from the solid-liquid separator (30), and the microscope (34) is connected with a computer (25) through a data cable (24) and is used for observing the coal dust sample in the slide (33) and displaying imaging information in the computer (25).
Further, the gas source (13) is a high-pressure gas cylinder or an air compressor.
Further, the supporting crack simulation device (16) is of a cuboid or cylindrical sealable structure and is made of colorless and transparent high-strength plastic.
Further, the simulated propping agent (38) is colorless or light-colored and transparent round ball shape, and the particle size is between 1mm and 1 cm.
The utility model provides a beneficial effect that technical scheme brought is: the device can simulate the dispersion or agglomeration behaviors of pulverized coal in the running process under the actual stratum condition, such as different stratum pressures, flow rates and pulverized coal content, and particularly the inclination angle of the support fracture is variable within the range of 0-180 degrees; the injection system comprises a liquid injection device and a gas injection device, the dispersion behaviors of the pulverized coal at different stages (such as single-phase flow and gas-liquid two-phase flow) in the coal bed gas extraction process are simulated, and the visual evaluation method is more visual and comprises visualization of supporting cracks and visualization of products; a pressure sensor is arranged in the supporting crack, so that the disturbance of the pulverized coal to the fluid pressure at different positions in the supporting crack in the simulation process can be monitored.
Drawings
FIG. 1 is a schematic diagram of a simulation apparatus for supporting coal powder agglomeration and dispersion behavior in a fracture according to an embodiment of the present invention;
FIG. 2 is a schematic diagram of a simulation of the coal fines agglomeration and dispersion behavior in propped fractures provided by an embodiment of the present invention;
description of the drawings: 1-a water pool, 2-a water pump, 3-a connecting pipeline, 4-a first regulating valve, 5-a first pressure meter, 6-a first flow meter, 7-a first one-way valve, 8-a three-way connector, 9-a second one-way valve, 10-a second flow meter, 11-a second pressure meter, 12-a second regulating valve, 13-an air source, 14-a third flow meter, 15-a third pressure meter, 16-a support crack simulator, 17-a support, 18-a first camera, 19-a second camera, 20-a first pressure sensor, 21-a second pressure sensor, 22-a first external memory, 23-a second external memory, 24-a data cable, 25-a computer, 26-a fourth flow meter, 27-a fourth pressure meter, 28-third regulating valve, 29-third one-way valve, 30-solid-liquid separator, 31-coal powder, 32-high precision electronic scale, 33-glass slide, 34-microscope, 35-liquid collecting tank, 36-disperse system, 37-liquid and 38-simulation propping agent.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, embodiments of the present invention will be further described below with reference to the accompanying drawings.
Referring to fig. 1, an embodiment of the present invention provides a simulation apparatus for coal powder agglomeration and dispersion behavior in a supporting fracture, including an injection system, a visual supporting fracture system, a discharge system, and a computer analysis system, where the injection system is used to simulate a single-phase flow and a gas-liquid two-phase flow environment in a coal bed methane mining process, the visual supporting fracture system is used to simulate a supporting fracture formed in a coal bed methane mining process, the discharge system is used to collect coal powder passing through the supporting fracture, and the computer analysis system is used to obtain and analyze agglomeration and dispersion behavior data of coal powder. The visual supporting fracture system is communicated with the injection system and the discharge system through a connecting pipeline 3.
The injection system comprises a water tank 1, a water pump 2, a first regulating valve 4, a first pressure gauge 5, a first flow meter 6, a first one-way valve 7, a three-way connector 8, a second one-way valve 9, a second flow meter 10, a second pressure gauge 11, a second regulating valve 12, an air source 13, a third flow meter 14 and a third pressure gauge 15. A dispersion system 36 formed by mixing pure liquid and pulverized coal is filled in the water pool 1, the water pump 2 is placed in the water pool 1, and the dispersion system 36 in the water pool 1 is pressed into the connecting pipeline 3; the gas source 13 provides gas phase pressure for simulating gas phase flow in the coal bed methane mining process, and preferably, the gas source 13 is a high-pressure gas cylinder or an air compressor.
The water pump 2, the air source 13 and the visual supporting crack system are communicated together through a three-way connector 8 and a connecting pipeline 3; one end of the three-way connector 8, which is communicated with the water pump 2, is connected with the first one-way valve 7, one end of the three-way connector, which is communicated with the air source 13, is connected with the second one-way valve 9, and the first one-way valve 7 and the second one-way valve 9 are utilized to respectively control the input of the water pump 2 and the air source 13 to the visual supporting crack system; and a third flow meter 14 and a third pressure meter 15 are arranged on one section of the connecting pipeline 3 which is communicated with the visual support fracture system by the three-way connector 8 and used for checking the inlet flow and the inlet pressure of the visual support fracture system.
The liquid phase outlet end of the water pump 2 is connected with a first regulating valve 4, the first regulating valve 4 is used for controlling the pressure and the flow of the liquid phase output by the water pump 2, and a first pressure gauge 5 and a first flow meter 6 are arranged on a connecting pipeline 3 between the first regulating valve 4 and a first one-way valve 7 and used for checking the pressure and the flow of the liquid phase output by the water pump 2; the gas source 13 is connected with the second regulating valve 12, the second regulating valve 12 is used for controlling the pressure and the flow of the gas phase output by the gas source 13, and the connecting pipeline 3 between the second regulating valve 12 and the second one-way valve 9 is provided with the second flow meter 10 and the second pressure gauge 11 for checking the flow and the pressure of the gas phase output by the gas source 13.
The visual propped fracture system includes a propped fracture simulation device 16, a scaffold 17, a first camera 18, a second camera 19, a first pressure sensor 20, a second pressure sensor 21, and a simulated proppant 38. The supporting crack simulator 16 is a cuboid or cylindrical sealable structure and is made of colorless and transparent high-strength plastic, the front end of the supporting crack simulator is connected with the injection system, and the rear end of the supporting crack simulator is connected with the discharge system; a first camera 18 and a second camera 19 are arranged on the outer surface of the supporting fracture simulation device 16, a first pressure sensor 20 and a second pressure sensor 21 are arranged on the inner wall of the supporting fracture simulation device, preferably, the first camera 18 and the second camera 19 are respectively arranged at two ends of the supporting fracture simulation device 16, and the first pressure sensor 20 and the second pressure sensor 21 are also respectively arranged at two ends of the supporting fracture simulation device 16; the inside of the supported fracture simulation device 16 is tightly filled with simulation propping agents 38, and the simulation propping agents 38 are colorless or light-colored transparent spherical shapes, are made of hard plastics or glass, and have the grain diameter of 1mm-1 cm.
The support 17 is movably arranged at the middle section of the supporting crack simulation device 16 and plays a role in lifting and fixing the supporting crack simulation device 16, the height of the support 17 is adjustable, and the supporting crack simulation device 16 can rotate around the support 17, so that the inclination angle of the supporting crack simulation device 16 is changed within the range of 0-180 degrees.
The discharge system includes a fourth flow meter 26, a fourth pressure gauge 27, a third regulator valve 28, a third check valve 29, a solid-liquid separator 30, a high precision electronic scale 32, and a sump 35. The solid-liquid separator 30 is used for filtering and retaining pulverized coal 31 produced after passing through the supporting fracture simulation device 16, and an upper end interface of the solid-liquid separator is sequentially connected with a third one-way valve 29, a third regulating valve 28, a fourth pressure gauge 27, a fourth flowmeter 26 and the rear end of the supporting fracture simulation device 16 through a connecting pipeline 3; a liquid collecting tank 35 disposed below the solid-liquid separator 30 for collecting a liquid 37 separated by the solid-liquid separator 30; the high-precision electronic scale 32 is used for weighing the mass of the pulverized coal filtered out by the solid-liquid separator 30.
It should be noted that the joints of the connecting pipeline 3 and other devices are all threaded connections, so that the sealing performance of the whole device is ensured, and the device is easy to disassemble and clean.
The computer analysis system comprises a first external memory 22, a second external memory 23, a computer 25, a slide 33, a microscope 34. The first external memory 22 is connected to the first pressure sensor 20 through a data cable 24 for storing data of the first pressure sensor 20, and is connected to the computer 25 through the data cable 24 for transmitting data of the first pressure sensor 20 to the computer 25; the second external memory 23 is connected on the one hand to the second pressure sensor 21 via a data cable 24 for storing data of the second pressure sensor 21 and on the other hand to a computer 25 via the data cable 24 for transmitting data of the second pressure sensor 21 to the computer 25. Preferably, two pressure sensors are placed at the propped fracture simulator 16 with openings at corresponding locations for the data cables 24 to extend out of the propped fracture simulator 16 and be sealed with glue.
The computer 25 is provided with particle image analysis software for displaying and processing data, and the computer 25 is connected with the first camera 18 and the second camera 19 through a data cable 24 to acquire image information in the shot supporting crack simulation device 16; the slide glass 33 comprises a glass slide and a cover glass and is used for placing a sample of the coal dust 31 filtered out from the solid-liquid separator 30; the microscope 34 is connected to the computer 25 through the data cable 24 for observing the coal dust sample in the slide glass and displaying the imaging information of the coal dust sample in the slide glass 33 in the computer 25.
When the simulation device is used for carrying out a simulation experiment of coal powder agglomeration and dispersion behaviors in a supporting crack, the simulation device comprises the following steps:
s1, assembling a simulation device for supporting the agglomeration and dispersion behaviors of the coal powder in the cracks, and ensuring that all equipment, control valves and one-way valves are in a closed state; the simulation propping agent 38 is filled in the propping crack simulator 16, the simulation propping agent is arranged densely, the mutual slippage among particles does not occur, and the bracket 17 is adjusted to ensure that the propping crack simulator 16 keeps the set inclination angle.
S2, filling liquid into the water pool 1, adding a certain amount of coal powder, and uniformly stirring to form a dispersion system 36; the water pump 2 is put into the dispersion system 36 and maintained at a certain submergence, and the first check valve 7, the third check valve 29, the high-precision electronic scale 32, the first camera 18, the second camera 19, the first pressure sensor 20, the second pressure sensor 21, the computer 25, and the microscope 34 are opened.
S3, performing motion simulation of the coal powder in the single-phase flow: starting the water pump 2 to enable the uniformly mixed dispersion system 36 to enter the supporting crack simulation device 16 through the water pump 2 and the connecting pipeline 3, referring to fig. 2, after the dispersion system 36 is agglomerated and dispersed in the supporting crack simulation device 16, the solid-phase pulverized coal finally stays in the solid-liquid separator 30 through the solid-liquid separator 30, and the liquid enters the liquid collecting tank 35; meanwhile, controlling a first regulating valve 4 to regulate inlet pressure and flow, and reading the inlet pressure and the inlet flow through a first pressure gauge 5 and a first flow meter 6, wherein the reading of the inlet pressure and the reading of the inlet flow are respectively the same as the reading of a third pressure gauge 15 and the reading of a third flow meter 14; the third regulating valve 28 is controlled to regulate the outlet pressure and flow and the outlet pressure and outlet flow are read by the fourth pressure gauge 27 and the fourth flow meter 26.
S4, evaluating the agglomeration and dispersion behaviors of the coal powder in the single-phase flow, specifically, the method comprises the following evaluation methods:
s41, introducing the high-definition pictures shot by the first camera 18 and the second camera 19 into the computer 25, and calculating the granularity, the number and the fractal dimension of the coal dust in the pictures by using particle image analysis software, so as to evaluate the granularity, the number and the self-similarity of the coal dust in the gaps of the propped fracture; if the granularity of the coal powder is smaller, the number in a unit area is smaller, and the fractal dimension is smaller, the coal powder in the supporting fracture is more dispersed, and the particle morphology is more regular, otherwise, the coal powder in the supporting fracture is more agglomerated, and the particle morphology is more complex;
s42, weighing the coal dust filtered out from the solid-liquid separator 30 by using the high-precision electronic scale 32 to obtain the mass of the discharged coal dust, and comparing the mass with the mass of the coal dust injected into the water pool 1, thereby evaluating the mass of the coal dust discharged from the supporting crack; if the ratio of the mass of the discharged coal dust to the mass of the injected coal dust is larger, the coal dust is easier to disperse, the supporting cracks are less prone to being blocked, and the damage to the flow conductivity of the supporting cracks is smaller;
s43, randomly extracting coal powder with a certain mass from the solid-liquid separator 30, paving the coal powder on a glass slide, dripping the coal powder into liquid in the liquid collecting tank 35, and covering the glass slide with a cover glass to form a glass slide 33; the glass slide 33 is placed under a microscope 34 for observation, is imaged in a computer 25, and is used for calculating the granularity of the coal dust discharged from the supporting fracture by using particle image analysis software, so that the granularity of the coal dust discharged from the supporting fracture is evaluated, wherein the smaller the granularity of the discharged coal dust is, the easier the coal dust is to disperse, and the easier the coal dust is to agglomerate.
S5, evaluating agglomeration and dispersion behaviors of the pulverized coal in the gas-liquid two-phase flow, specifically, on the basis of the step S3, opening a second one-way valve 9 and a gas source 13, controlling a second regulating valve 12 to regulate the pressure and flow of gas entering, reading the pressure and flow of gas entering through a second pressure gauge 11 and a second flow meter 10, and reading the injection pressure and injection flow of the gas-liquid mixed fluid through a third pressure gauge 15 and a third flow meter 14; after that, evaluation was performed in accordance with the method in step S4.
S6, evaluating the disturbance of the movement of the pulverized coal on the fluid pressure in the supporting fracture simulator, specifically, in step S3 and step S5, the flow of the pulverized coal in the supporting fracture simulator 16 respectively passes through the first pressure sensor 20 and the second pressure sensor 21, the pressure data are respectively stored in the first external memory 22 and the second external memory 23, and after the pressure data are led into the computer 25, the change rule of the fluid pressure at different positions in the supporting fracture due to the disturbance of the pulverized coal along with the time is analyzed.
In this document, the terms front, back, upper and lower are used to define the components in the drawings and the positions of the components relative to each other, and are used for clarity and convenience of the technical solution. It is to be understood that the use of the directional terms should not be taken to limit the scope of the claims.
The features of the embodiments and embodiments described herein above may be combined with each other without conflict.
The above description is only for the preferred embodiment of the present invention, and is not intended to limit the present invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included within the protection scope of the present invention.
Claims (8)
1. The device for simulating the agglomeration and dispersion behaviors of the coal dust in the supporting fracture is characterized by comprising an injection system, a visual supporting fracture system, a discharge system and a computer analysis system, wherein the visual supporting fracture system is communicated with the injection system and the discharge system through a connecting pipeline (3), and the computer analysis system is used for acquiring and analyzing the data of the agglomeration and dispersion behaviors of the coal dust in the visual supporting fracture system;
the injection system comprises a water tank (1), a water pump (2), a three-way connector (8) and an air source (13), wherein a dispersion system formed by mixing pure liquid and pulverized coal is filled in the water tank (1); the water pump (2), the air source (13) and the visual supporting crack system are communicated together through the three-way connector (8) and the connecting pipeline (3), the water pump (2) is placed in the water pool (1), and the dispersion system in the water pool (1) is pressed into the connecting pipeline (3);
the visual supporting fracture system comprises a supporting fracture simulation device (16), a support (17) used for lifting and fixing the supporting fracture simulation device (16), a simulation propping agent (38) used for filling the supporting fracture simulation device (16), a first camera (18) and a second camera (19) which are arranged on the outer surface of the supporting fracture simulation device (16), and a first pressure sensor (20) and a second pressure sensor (21) which are arranged on the inner wall of the supporting fracture simulation device (16), wherein the front end of the supporting fracture simulation device (16) is connected with the injection system, and the rear end of the supporting fracture simulation device is connected with the discharge system; the support (17) is movably arranged at the middle section of the supporting crack simulating device (16), the height of the support (17) is adjustable, and the supporting crack simulating device (16) can rotate around the support (17) by 0-180 degrees;
the discharge system comprises a solid-liquid separator (30), a high-precision electronic scale (32) and a liquid collecting tank (35), wherein the solid-liquid separator (30) is used for filtering and retaining coal dust produced after passing through the supporting crack simulation device (16), and an upper end port of the solid-liquid separator (30) is communicated with the rear end of the supporting crack simulation device (16) through a connecting pipeline (3); the liquid collecting pool (35) is arranged below the solid-liquid separator (30) and is used for collecting liquid separated by the solid-liquid separator (30); and the high-precision electronic scale (32) is used for weighing the mass of the pulverized coal filtered out by the solid-liquid separator (30).
2. The simulation device for coal dust agglomeration and dispersion behavior in a propped fracture as claimed in claim 1, characterized in that the injection system also comprises a first regulating valve (4), a first pressure gauge (5), a first flowmeter (6), a first one-way valve (7), a second one-way valve (9), a second flowmeter (10), a second pressure gauge (11), a second regulating valve (12), a third flowmeter (14) and a third pressure gauge (15), wherein the liquid phase outlet end of the water pump (2) is connected with the first regulating valve (4), one end of the three-way connector (8) communicated with the water pump (2) is connected with the first one-way valve (7), the first pressure gauge (5) and the first flow meter (6) are arranged on a connecting pipeline (3) between the first regulating valve (4) and the first one-way valve (7);
the air source (13) is connected with the second regulating valve (12), one end of the three-way connector (8) communicated with the air source (13) is connected with the second one-way valve (9), and the second flowmeter (10) and the second pressure gauge (11) are arranged on the connecting pipeline (3) between the second regulating valve (12) and the second one-way valve (9);
the third flow meter (14) and the third pressure meter (15) are arranged on a connecting pipeline (3) of the three-way connector (8) and the visual support fracture system.
3. The simulation device for coal powder agglomeration and dispersion behavior in a propped fracture as claimed in claim 1, wherein the discharge system further comprises a fourth flow meter (26), a fourth pressure gauge (27), a third regulating valve (28) and a third one-way valve (29), wherein the upper port of the solid-liquid separator (30) is connected with the third one-way valve (29), the third regulating valve (28), the fourth pressure gauge (27), the fourth flow meter (26) and the rear end of the propped fracture simulation device (16) in sequence through a connecting pipeline (3).
4. The simulation apparatus for supporting coal dust agglomeration and dispersion behavior in fractures according to claim 1, wherein the computer analysis system comprises a first external memory (22) connected with the first pressure sensor (20) through a data cable (24), a second external memory (23) connected with the second pressure sensor (21) through a data cable (24), and a computer (25) installed with particle image analysis software, wherein the first external memory (22), the second external memory (23), the first camera (18), and the second camera (19) are all connected with the computer (25) through a data cable (24).
5. The simulation apparatus for propping up coal fines agglomeration and dispersion behavior within fractures according to claim 4, characterized in that the computer analysis system further comprises a slide (33) and a microscope (34), wherein the slide (33) comprises a glass slide and a cover glass for placing the coal fines sample filtered out from the solid-liquid separator (30), and the microscope (34) is connected with a computer (25) through a data cable (24) for observing the coal fines sample in the slide (33) and displaying imaging information in the computer (25).
6. The simulation device for the agglomeration and dispersion behavior of the pulverized coal in the propped fracture as claimed in claim 1, wherein the gas source (13) is a high-pressure gas cylinder or an air compressor.
7. The simulation device for coal powder agglomeration and dispersion behavior in a propping fracture as claimed in claim 1, characterized in that said propping fracture simulation device (16) is a cuboid or cylindrical sealable structure made of colorless and transparent high-strength plastic.
8. The simulation device for the agglomeration and dispersion behavior of the coal dust in the propped fracture as recited in claim 1, characterized in that the simulated proppant (38) is in the shape of colorless or light-colored transparent spheres with a particle size of 1mm-1 cm.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111307670A (en) * | 2020-03-27 | 2020-06-19 | 中国地质大学（武汉） | Device and method for simulating agglomeration and dispersion behaviors of coal dust in supporting fracture |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111307670A (en) * | 2020-03-27 | 2020-06-19 | 中国地质大学（武汉） | Device and method for simulating agglomeration and dispersion behaviors of coal dust in supporting fracture |
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