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CN106703887A - Method of judging secondary gas explosion in mine thermodynamic disaster relief - Google Patents

Method of judging secondary gas explosion in mine thermodynamic disaster relief Download PDF

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Publication number
CN106703887A
CN106703887A CN201611043088.0A CN201611043088A CN106703887A CN 106703887 A CN106703887 A CN 106703887A CN 201611043088 A CN201611043088 A CN 201611043088A CN 106703887 A CN106703887 A CN 106703887A
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gas
concentration
time
gas explosion
area
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CN106703887B (en
Inventor
郭军
郑学召
文虎
金永飞
邓军
王亚超
刘文永
李亚清
费金彪
李海涛
张铎
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Xi'an Tianhe Mining Technology Co ltd
Xian University of Science and Technology
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Xi'an Tianhe Mining Technology Co ltd
Xian University of Science and Technology
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    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21FSAFETY DEVICES, TRANSPORT, FILLING-UP, RESCUE, VENTILATION, OR DRAINING IN OR OF MINES OR TUNNELS
    • E21F17/00Methods or devices for use in mines or tunnels, not covered elsewhere
    • E21F17/18Special adaptations of signalling or alarm devices
    • GPHYSICS
    • G16INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS
    • G16ZINFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS, NOT OTHERWISE PROVIDED FOR
    • G16Z99/00Subject matter not provided for in other main groups of this subclass

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  • Engineering & Computer Science (AREA)
  • Mining & Mineral Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Emergency Alarm Devices (AREA)

Abstract

The invention discloses a method of judging secondary gas explosion in mine thermodynamic disaster relief; the method comprises the steps of I, determining a secondary gas explosion position; II, estimating time for secondary gas explosion to occur in the monitored area, to be specific, 201, acquiring environmental parameters of the monitored area, 202, judging whether the monitored area is an area experiencing high-concentration gas explosion or not, 203, estimating time and probability for the high-concentration gas explosion to occur and 204, estimating time and probability for low-concentration gas explosion; III, estimating time for the secondary gas explosion to occur in the monitored area; IV, displaying and storing in real time, judgment results for the secondary gas explosion. The method of the invention is novel in design, can judge the three key indexes, time, probability and position, of secondary gas explosion in a coal mine, and can provide theoretical reference and guidance for commanding and decision-making for thermodynamic disaster relief.

Description

Secondary cases gas explosion decision method during mine heat power disaster assistance
Technical field
The invention belongs to mine heat power disaster assistance technical field, and in particular to a kind of mine heat power disaster assistance mistake Secondary cases gas explosion decision method in journey.
Background technology
Mine fire and the generation evolution mechanism of gas explosion are extremely complex in the heat power disaster of colliery, in rescue operations It may happen that various secondary disasters, such as fall of ground, Climatic regionalization, high-concentration fume, naked light fire, gas and dust explosion, Distinguished and admirable disorderly, a large amount of toxic and harmfuls of generation, ventilating system destruction etc..The specific implementation person worked as mine rescue and place In dangerous disaster relief forefront personnel, the Individual protection equitment of rescue team member is typically only capable to ensure it from toxic and harmful Threaten, and to gas explosion almost without protective capacities.In rescue operations, the gas explosion of burst may result in and enter calamity The personnel of area's rescue die, and seriously threaten the life security of rescue personnel, influence progress and the success or failure of rescue.Science, in time Mine heat power disaster assistance commanding and decision-making is formulated on ground, and there is the life security to ensureing rescue personnel important theoretical direction to anticipate Justice.However, the research of the mechanism and control technology of primary gas explosion is directed to existing research more, in rescue operations Occur gas explosion mechanism and the characteristic study it is relatively fewer.After occurring due to heat power catastrophe, down-hole disaster area is divulged information often It is in disturbance state due to the heating power and dynamic effect of disaster generation, the great ambiguity of the condition of a disaster and difficulty are predictive.Heat power disaster Mechanism and the characteristic study progress that gas explosion occurs in rescue operations are slower, it is difficult to science, effectively instruct heat power disaster The commanding and decision-making work of rescue.Therefore, Secondary cases gas explosion during a kind of mine heat power disaster assistance is nowadays lacked The characteristics of decision method, formation condition and mine gas explosion according to gas explosion and rule, and combine mine heat power Rule characteristic, can determine that time of origin, probability and the key index of position three of Secondary cases gas explosion, to mine heat power calamity The commanding and decision-making of evil rescue has important theory directive significance.
The content of the invention
The technical problems to be solved by the invention are for above-mentioned deficiency of the prior art, there is provided a kind of mine heat is dynamic Secondary cases gas explosion decision method during power disaster assistance, it is novel in design, it is possible to determine that heat power Post disaster relief process In, there is time, probability and the key index of position three of Secondary cases gas explosion in underground coal mine, can be heat power disaster assistance Commanding and decision-making provide theoretical reference and guidance.
In order to solve the above technical problems, the technical solution adopted by the present invention is:During mine heat power disaster assistance after Hair property gas explosion decision method, it is characterised in that the method is comprised the following steps:
Step one, determine Secondary cases gas explosion position:Distinguish installation region by multiple key positions in mine Simultaneously extremely be arranged in Control Room the temperature parameter real-time Transmission in the region by the temperature parameter of monitoring node collection corresponding region Control computer, temperature parameter threshold value is set by input through keyboard module, is demarcated using control computer and is reached temperature parameter threshold The key position of value, the position that the gas explosion of anticipation Secondary cases occurs;
Area monitoring node includes zone controller and the clock circuit and communication mould that connect with the zone controller Block, the input of zone controller is terminated with temperature sensor, air velocity transducer, gas sensor, the monitored area for gathering Gas density and gas flow gas monitor and the oxygen concentration of monitored area and oxygen flow for gathering Oxygen monito;
Step 2, the time for estimating institute's monitored area generation Secondary cases gas explosion, process is as follows:
Step 201, the ambient parameter for obtaining institute monitored area:The ventilation shape of institute monitored area is monitored by air velocity transducer State, the gas bearing capacity and oxygen content of institute monitored area are monitored by gas monitor and oxygen monito respectively;
Step 202, judge institute monitored area whether be occur high concentration gas blast region:Set by zone controller Monitoring Parameters variation time threshold is put, according to the ambient parameter that the ambient parameter and clock circuit that are obtained in step 201 are recorded Transformation period, whether institute monitored area is high concentration gas blast area after judging calamity, when gas monitor and oxygen monito Institute's monitored area gas bearing capacity and oxygen content reach the time of the gas explosion limit less than the monitoring parameter change after monitoring calamity When changing time threshold, institute monitored area is illustrated to there is high concentration gas blast area, performing step 203;Otherwise, step is performed 204;
The time Estimate that step 203, high concentration gas blast occur, process is as follows:
Step 2031, according to formulaThe differential equation is solved, high concentration gas can be obtained Oxygen concentration changes experienced time t in blast area1Change experienced time t with methane concentration2, wherein,V is high concentration gas blast area volume, q1Mixed to flow into high concentration gas blast area Close the flow of gas, q2It is the flow of mixed gas in outflow high concentration gas blast area, c1To flow into high concentration gas blast The concentration of oxygen, c in region2To flow into the concentration of methane in high concentration gas blast area, c01It is primary condition t1When=0, The initial value of oxygen concentration,It is the oxygen concentration desired value to be reached, c02It is primary condition t2When=0, methane concentration Initial value,It is the methane concentration desired value to be reached;
Step 2032, according to formulaCalculate high concentration gas blast area oxygen after calamity Gas concentration becomes the 12% time T for being experienced1, gas density reach the time T that LEL 5% is experienced21And gas is dense Degree reaches the time T that UEL 16% is experienced22
Step 2033, the time for estimating high concentration gas blast generation:When oxygen concentration becomes 12% institute in step 2032 The time T of experience1>T22When, high concentration gas blast does not occur;When oxygen concentration becomes 12% and experiences in step 2032 Between T21≤T1≤T22When, the time t that high concentration gas blast occurs meets:T1+t3≤t≤T22+t3, wherein, t3To reach gas The gas of explosion limit runs into the time of burning things which may cause a fire disaster;When oxygen concentration becomes the 12% time T for being experienced in step 20321<T21When, The time t that high concentration gas blast occurs meets:T21+t3≤t≤T22+t3
The time Estimate that step 204, low concentration gas blast occur, process is as follows:
Step 2041, according to formulaThe differential equation is solved, low concentration can be obtained Oxygen concentration changes experienced time t' in gas explosion region1Change experienced time t' with methane concentration2, wherein,V' is low concentration gas blast area volume, q'1To flow into low concentration gas blast area The flow of interior mixed gas, q'2It is the flow of mixed gas in outflow low concentration gas blast area, c'1To flow into low concentration watt The concentration of oxygen, c' in this blast area2To flow into the concentration of methane in low concentration gas blast area, c'01It is primary condition t'1When=0, the initial value of oxygen concentration, c'02It is primary condition t'2When=0, the initial value of methane concentration;
Step 2042, according to formulaCalculate low concentration gas blast area after calamity Oxygen concentration becomes the 12% time T' for being experienced1, gas density reach the time T' that LEL 5% is experienced21And watt This concentration reaches the time T' that UEL 16% is experienced22
Step 2043, the time for estimating low concentration gas blast generation:When oxygen concentration becomes 12% institute in step 2042 The time T' of experience1>T'22When, the time t' that low concentration gas blast occurs meets:T'21+t'3≤t'≤T'22+t'3;Work as step Oxygen concentration becomes the 12% time T' for being experienced in rapid 204221≤T'1≤T'22When, the time that low concentration gas blast occurs T' meets:T'21+t'3≤t'≤T'1+t'3;When oxygen concentration becomes the 12% time T' for being experienced in step 20421<T'21When, Low concentration gas blast does not occur, wherein, t'3The time of burning things which may cause a fire disaster is run into for the gas for reaching the gas explosion limit;
Step 3, the probability for estimating institute's monitored area generation Secondary cases gas explosion:Analyzed according to methods of gas explosion fault tree Method, the probability P=P of gas explosion1×P2×P3, wherein, P1For institute's monitored area gas concentration reaches the gas explosion limit after calamity Probability and P1Met according to Ke Wade explosion triangles:P1=P1i, i=1~4 and P11=1>P13>P12>P14=0, P11For watt The probability of this concentration gas explosion limit between 5%~16% and when oxygen concentration is more than 12%, P12For gas density is situated between The probability of the gas explosion limit, P between 5%~16% and when oxygen concentration is less than 12%13For gas density more than 16% it Between and oxygen concentration be less than 12% when the gas explosion limit probability, P14Gas explosion limit when being less than 5% for gas density Probability, probability P12And probability P13Use expert point rating method estimated probability value, P2For institute's monitored area presence can cause after calamity The probability of gas explosion burning things which may cause a fire disaster, P3For institute monitored area reaches the probability that the gas of the gas explosion limit and burning things which may cause a fire disaster meet after calamity;
Step 4, Secondary cases gas explosion result of determination show and real-time storage:By multiple area monitoring nodes simultaneously Under monitoring well there is time and the probability of Secondary cases gas explosion in the key position, and by the result of determination reality of corresponding position When transmit to control computer, by display can real time inspection result of determination, result of determination is preserved by memory in real time.
Secondary cases gas explosion decision method during above-mentioned mine heat power disaster assistance, it is characterised in that:Step One and step 4 described in key position include working face intake, tailentry road, working face middle part, working face return High temperature smoke affected area and close powered electricity after wind corner, main air intake belt tunnel, the generation of preceding mine heat power disaster Device and abnormal Gas affected area.
Secondary cases gas explosion decision method during above-mentioned mine heat power disaster assistance, it is characterised in that:Step Probability in threeWherein, N is expert's number, p12jFor the jth position gas density that is given of expert between 5%~ Between 16% and oxygen concentration be less than 12% when the gas explosion limit probability, δjIt is p12jCorresponding weight andp13j For the jth position gas density that is given of expert more than 16% between and oxygen concentration gas explosion limit when being less than 12% probability, δ'jIt is p13jCorresponding weight and
Secondary cases gas explosion decision method during above-mentioned mine heat power disaster assistance, it is characterised in that:Step Probability in threeWherein, probability P21For institute's monitored area burning things which may cause a fire disaster is the probability and P of continuation burning things which may cause a fire disaster after calamity21=1, generally Rate P22For institute's monitored area burning things which may cause a fire disaster is the probability and 0≤P of instantaneity burning things which may cause a fire disaster after calamity22≤1。
Secondary cases gas explosion decision method during above-mentioned mine heat power disaster assistance, it is characterised in that:Step Probability P in three3=1.
The present invention has advantages below compared with prior art:
1st, the present invention distinguishes installation region monitoring node by multiple key positions in mine, while monitoring multiple closing There is time and the probability of Secondary cases gas explosion at key position, control computer can simultaneously process multiple area monitoring nodes and adopt The data of collection, realize the purpose simultaneously to whole monitoring mining, are easy to promote the use of.
2nd, the present invention combines the characteristics of mine heat power disaster down-hole disaster area environment and gas explosion, proposes respectively highly concentrated After degree gas explosion and low concentration gas blast occur, the decision method of gas explosion time range, the degree of accuracy is high.
3rd, during decision method of the invention can be determined that heat power Post disaster relief, there is Secondary cases gas under mine quick-fried Fried time, probability and the key index of position three, significant to ensureing rescue personnel's life security, feasibility is good, Practical, popularizing application prospect is good.
In sum, the present invention is novel in design rationally, novel in design, it is possible to determine that during heat power Post disaster relief, coal There is time, probability and the key index of position three of Secondary cases gas explosion under mine, can be the finger of heat power disaster assistance Wave decision-making and theoretical reference and guidance are provided.
Below by drawings and Examples, technical scheme is described in further detail.
Brief description of the drawings
Fig. 1 is the schematic block circuit diagram that the Secondary cases gas explosion that the present invention is used judges equipment..
Fig. 2 is the schematic block circuit diagram of area monitoring node of the present invention.
Fig. 3 is the method flow block diagram of Secondary cases gas explosion decision method of the present invention.
Description of reference numerals:
1-area monitoring node;1-1-temperature sensor;1-2-air velocity transducer;
1-3-gas monitor;1-4-oxygen monito;1-5-clock circuit;
1-6-zone controller;1-7-communication module;1-8-gas sensor;
2-input through keyboard module;3-control computer;4-display;
5-memory.
Specific embodiment
As shown in figure 1, Secondary cases gas explosion decision method during mine heat power disaster assistance of the present invention, including with Lower step:
Step one, determine Secondary cases gas explosion position:Distinguish installation region by multiple key positions in mine Simultaneously extremely be arranged in Control Room the temperature parameter real-time Transmission in the region by the temperature parameter of the collection of monitoring node 1 corresponding region Control computer 3, temperature parameter threshold value is set by input through keyboard module 2, is demarcated using control computer 3 and is reached temperature parameter The key position of threshold value, the position that the gas explosion of anticipation Secondary cases occurs;
Area monitoring node 1 includes the zone controller 1-6 and clock circuit 1- connected with the zone controller 1-6 The input of 5 and communication module 1-7, zone controller 1-6 is terminated with temperature sensor 1-1, air velocity transducer 1-2, gas sensing Device 1-8, the gas monitor 1-3 of the gas density of monitored area and gas flow and monitored for gathering for gathering The oxygen concentration in region and the oxygen monito 1-4 of oxygen flow;
In the present embodiment, the key position include working face intake, tailentry road, working face middle part, Working face Air return corner, main air intake belt tunnel, a preceding mine heat power disaster high temperature smoke affected area and are leaned on after occurring Nearly powered electrical equipment and abnormal Gas affected area.
Generation gas explosion must be with the presence of burning things which may cause a fire disaster, therefore can there will be can trigger the fire location of gas explosion to see Make the position of gas explosion again, in actual shaft production, be if causing the burning things which may cause a fire disaster of preceding mine heat power disaster Continue burning things which may cause a fire disaster, that burning things which may cause a fire disaster exists certainly, and energy triggers gas explosion enough;If preceding mine heat power disaster is instantaneous Burning things which may cause a fire disaster, that preceding mine heat power disaster institute monitoring section after calamity that is possible to ignite causes calamity point or according to disaster area center certain limit Interior combustible, and turn into the burning things which may cause a fire disaster of gas explosion;Secondly, high temperature smoke felt area after preceding mine heat power disaster occurs Domain, such as caving place, blind lane near institute monitored area after calamity, if institute monitoring section or the ventilation being connected with institute monitoring section after calamity after calamity In network, there is high concentration gas storehouse, when institute's monitoring section high temperature smoke spreads to such region after calamity, still with enough temperature Degree, the possible mixing fresh air of high temperature smoke, causes gas, oxygen concentration and the burning things which may cause a fire disaster in such region all to reach gas explosion in addition Condition, it will trigger gas explosion;In addition, if there are abnormal Gas, moment in institute monitoring section after calamity in rescue operations Gush out a large amount of gas, cause disaster area gas to reach explosion limit, if these regions have powered electrical equipment, it is possible to because electrically Spark and trigger gas explosion, the life security of rescue team member to entering institute monitoring section after calamity threatens.
Step 2, the time for estimating institute's monitored area generation Secondary cases gas explosion, process is as follows:
Step 201, the ambient parameter for obtaining institute monitored area:The logical of institute monitored area is monitored by air velocity transducer 1-2 Wind state, the gas bearing capacity and oxygen for monitoring institute monitored area respectively by gas monitor 1-3 and oxygen monito 1-4 contains Amount;
It should be noted that institute monitored area is any one place at the key position, in any one place's key position One area monitoring node 1 is installed and estimates that institute monitored area occurs time and the probability of Secondary cases gas explosion, any one place closes Key position estimates that institute monitored area occurs the time of Secondary cases gas explosion and the method all same of probability, and control computer 3 can While key position quick-fried result of determination of Secondary cases gas during mine heat power disaster assistance in many places under monitoring well.
Step 202, judge institute monitored area whether be occur high concentration gas blast region:By zone controller 1- 6 set monitoring Parameters variation time threshold, according to the ring that the ambient parameter and clock circuit 1-5 that are obtained in step 201 are recorded The border Parameters variation time, whether institute monitored area is high concentration gas blast area after judging calamity, when gas monitor 1-3 and oxygen Institute's monitored area gas bearing capacity and oxygen content reach the time of the gas explosion limit less than described after gas monitor 1-4 monitoring calamities During monitoring Parameters variation time threshold, institute monitored area is illustrated to there is high concentration gas blast area, performing step 203;It is no Then, step 204 is performed;
It should be noted that it refers to institute monitored area after preceding mine heat power disaster occurs that high concentration gas explode Interior gas density and oxygen concentration is increased rapidly, gas density and oxygen concentration into incremental state;Low concentration gas explode Refer to that the gas density in institute monitored area is extremely low after preceding mine heat power disaster occurs, less than under gas density blast Limit 5%, corresponding oxygen concentration is higher, and oxygen concentration is higher than 12%, and, in slowly incremental state, oxygen concentration is in slow for gas density Slow decrement states, can be using air velocity transducer 1-2, temperature sensor 1-1 and gas sensor 1-8 collection Minepit environments Judge institute monitored area whether for the region that high concentration gas blast occurs provides reference.
The time Estimate that step 203, high concentration gas blast occur, process is as follows:
Step 2031, according to formulaThe differential equation is solved, high concentration gas can be obtained Oxygen concentration changes experienced time t in blast area1Change experienced time t with methane concentration2, wherein,V is high concentration gas blast area volume, q1Mixed to flow into high concentration gas blast area Close the flow of gas, q2It is the flow of mixed gas in outflow high concentration gas blast area, c1To flow into high concentration gas blast The concentration of oxygen, c in region2To flow into the concentration of methane in high concentration gas blast area, c01It is primary condition t1When=0, The initial value of oxygen concentration,It is the oxygen concentration desired value to be reached, c02It is primary condition t2When=0, methane concentration Initial value,It is the methane concentration desired value to be reached;
In actual production, oxygen concentration changes experienced time t in high concentration gas blast area1Become with methane concentration Change experienced time t2Recorded by the clock circuit 1-5 in institute monitored area inner region monitoring node 1, high concentration gas are quick-fried Fried region is any one place at the key position, and high concentration gas blast area volume V is empirical value, flows into high concentration watt The flow q of mixed gas in this blast area1With the flow q of mixed gas in outflow high concentration gas blast area2Use gas Body sensor 1-8 is measured, and flows into the concentration c of oxygen in high concentration gas blast area1, primary condition t1Oxygen concentration when=0 Initial value c01The desired value to be reached with oxygen concentrationMeasured by oxygen monito 1-4, flow into high concentration gas quick-fried The concentration c of methane in fried region2, primary condition t2The initial value c of methane concentration when=002The mesh to be reached with methane concentration Scale valueMeasured by Methane monitoring instrument 1-3.
Step 2032, according to formulaCalculate high concentration gas blast area oxygen after calamity Gas concentration becomes the 12% time T for being experienced1, gas density reach the time T that LEL 5% is experienced21And gas is dense Degree reaches the time T that UEL 16% is experienced22
Step 2033, the time for estimating high concentration gas blast generation:When oxygen concentration becomes 12% institute in step 2032 The time T of experience1>T22When, high concentration gas blast does not occur;When oxygen concentration becomes 12% and experiences in step 2032 Between T21≤T1≤T22When, the time t that high concentration gas blast occurs meets:T1+t3≤t≤T22+t3, wherein, t3To reach gas The gas of explosion limit runs into the time of burning things which may cause a fire disaster;When oxygen concentration becomes the 12% time T for being experienced in step 20321<T21When, The time t that high concentration gas blast occurs meets:T21+t3≤t≤T22+t3
In actual production, set by zone controller 1-6 in the high concentration gas blast area inner region monitoring node 1 The temperature sensor 1-1 temperature thresholds and rate temperature change threshold value of the high concentration gas blast area, reach gas explosion The gas of the limit runs into the time t of burning things which may cause a fire disaster3By the record of clock circuit 1-5 in temperature sensor 1-1 temperature data change procedures Time measures, and when the temperature data growth rate that the temperature sensor 1-1 of the high concentration gas blast area is gathered is slow, reaches The gas of the gas explosion limit runs into temperature sensor 1-1 temperature threshold of the time of burning things which may cause a fire disaster by setting and determines, reaches temperature biography During sensor 1-1 temperature thresholds, the rescue team member into institute monitoring section after calamity is reminded to take care in time;When the high concentration gas are quick-fried When the temperature data growth rate of the temperature sensor 1-1 collections in fried region is very fast, the gas for reaching the gas explosion limit runs into The time of burning things which may cause a fire disaster is determined by the temperature sensor 1-1 rate temperature change threshold values for setting, should reminded into institute monitoring section after calamity Rescue team member carry out at once it is hidden save oneself, hide the harm that Secondary cases gas explosion brings.
The time Estimate that step 204, low concentration gas blast occur, process is as follows:
Step 2041, according to formulaThe differential equation is solved, low concentration can be obtained Oxygen concentration changes experienced time t' in gas explosion region1Change experienced time t' with methane concentration2, wherein,V' is low concentration gas blast area volume, q'1To flow into low concentration gas blast area The flow of interior mixed gas, q'2It is the flow of mixed gas in outflow low concentration gas blast area, c'1To flow into low concentration watt The concentration of oxygen, c' in this blast area2To flow into the concentration of methane in low concentration gas blast area, c'01It is primary condition t'1When=0, the initial value of oxygen concentration, c'02It is primary condition t'2When=0, the initial value of methane concentration;
In actual production, oxygen concentration changes experienced time t' in low concentration gas blast area1And methane concentration The experienced time t' of change2Recorded by the clock circuit 1-5 in institute monitored area inner region monitoring node 1, low concentration watt This blast area is any one place at the key position, and low concentration gas blast area volume V is empirical value, is flowed into low dense The flow q' of mixed gas in degree gas explosion region1With the flow q' of mixed gas in outflow low concentration gas blast area2 Measured using gas sensor 1-8, flow into low concentration gas blast area in oxygen concentration c '1With primary condition t'1When=0 Oxygen concentration initial value c'01Measured by oxygen monito 1-4, flow into the concentration of methane in low concentration gas blast area c'2With primary condition t'2The initial value c' of methane concentration when=002Measured by Methane monitoring instrument 1-3.
Step 2042, according to formulaCalculate low concentration gas blast area after calamity Oxygen concentration becomes the 12% time T' for being experienced1, gas density reach the time T' that LEL 5% is experienced21And watt This concentration reaches the time T' that UEL 16% is experienced22
Step 2043, the time for estimating low concentration gas blast generation:When oxygen concentration becomes 12% institute in step 2042 The time T' of experience1>T'22When, the time t' that low concentration gas blast occurs meets:T'21+t'3≤t'≤T'22+t'3;Work as step Oxygen concentration becomes the 12% time T' for being experienced in rapid 204221≤T'1≤T'22When, the time that low concentration gas blast occurs T' meets:T'21+t'3≤t'≤T'1+t'3;When oxygen concentration becomes the 12% time T' for being experienced in step 20421<T'21When, Low concentration gas blast does not occur, wherein, t'3The time of burning things which may cause a fire disaster is run into for the gas for reaching the gas explosion limit;
In actual production, set by zone controller 1-6 in the low concentration gas blast area inner region monitoring node 1 The temperature sensor 1-1 temperature thresholds and rate temperature change threshold value of the low concentration gas blast area, reach gas explosion The gas of the limit runs into the time t' of burning things which may cause a fire disaster3By the record of clock circuit 1-5 in temperature sensor 1-1 temperature data change procedures Time measures, and when the temperature data growth rate that the temperature sensor 1-1 of the low concentration gas blast area is gathered is slow, reaches The gas of the gas explosion limit runs into temperature sensor 1-1 temperature threshold of the time of burning things which may cause a fire disaster by setting and determines, reaches temperature biography During sensor 1-1 temperature thresholds, the rescue team member into institute monitoring section after calamity is reminded to take care in time;When the low concentration gas are quick-fried When the temperature data growth rate of the temperature sensor 1-1 collections in fried region is very fast, the gas for reaching the gas explosion limit runs into The time of burning things which may cause a fire disaster is determined by the temperature sensor 1-1 rate temperature change threshold values for setting, should reminded into institute monitoring section after calamity Rescue team member carry out at once it is hidden save oneself, hide the harm that Secondary cases gas explosion brings.
Step 3, the probability for estimating institute's monitored area generation Secondary cases gas explosion:Analyzed according to methods of gas explosion fault tree Method, the probability P=P of gas explosion1×P2×P3, wherein, P1For institute's monitored area gas concentration reaches the gas explosion limit after calamity Probability and P1Met according to Ke Wade explosion triangles:P1=P1i, i=1~4 and P11=1>P13>P12>P14=0, P11For watt The probability of this concentration gas explosion limit between 5%~16% and when oxygen concentration is more than 12%, P12For gas density is situated between The probability of the gas explosion limit, P between 5%~16% and when oxygen concentration is less than 12%13For gas density more than 16% it Between and oxygen concentration be less than 12% when the gas explosion limit probability, P14Gas explosion limit when being less than 5% for gas density Probability, probability P12And probability P13Use expert point rating method estimated probability value, P2For institute's monitored area presence can cause after calamity The probability of gas explosion burning things which may cause a fire disaster, P3For institute monitored area reaches the probability that the gas of the gas explosion limit and burning things which may cause a fire disaster meet after calamity;
In the present embodiment, probability in step 3Wherein, N is expert's number, p12jIt is jth position expert The probability of the gas density for being given gas explosion limit between 5%~16% and when oxygen concentration is less than 12%, δjIt is p12j Corresponding weight andp13jFor the jth position gas density that is given of expert more than 16% between and oxygen concentration be less than The probability of the gas explosion limit, δ when 12%j' it is p13jCorresponding weight and
In the present embodiment, probability in step 3Wherein, probability P21For institute's monitored area burning things which may cause a fire disaster is lasting after calamity The probability and P of property burning things which may cause a fire disaster21=1, probability P22For institute's monitored area burning things which may cause a fire disaster is the probability and 0≤P of instantaneity burning things which may cause a fire disaster after calamity22≤1。
In actual production, continuation burning things which may cause a fire disaster refers to after triggering heat power disaster for the first time, exist for a long time and can draw The burning things which may cause a fire disaster of energy, such as naked light fire etc., the disaster caused by this burning things which may cause a fire disaster, it is believed that secondary burning things which may cause a fire disaster is deposited needed for hair gas explosion Probability be 1, i.e. probability P21=1;Instantaneity burning things which may cause a fire disaster refers to the burning things which may cause a fire disaster of pop-off after triggering heat power disaster for the first time, Such as electric spark.
In the present embodiment, probability P in step 33=1.
In actual production, due to the complexity and ambiguity of heat power disaster, rescue personnel often cannot accurately grasp very Real the condition of a disaster information, therefore, it is impossible to judge that detonable mixed gas have much with the probability of burning things which may cause a fire disaster, in actual rescue work In, consider from maximum security, it is believed that it necessarily occurs, i.e. probability P3=1, for on-the-spot rescue team member's life security Consider, in order to prevent the further expansion of accident, in rescue, as long as we are generally acknowledged that disaster area, gas reaches explosion limit, Just be bound to probability P=P that gas explosion, i.e. gas explosion occur1
Step 4, Secondary cases gas explosion result of determination show and real-time storage:By multiple area monitoring nodes 1 simultaneously Under monitoring well there is time and the probability of Secondary cases gas explosion in the key position, and by the result of determination reality of corresponding position When transmit to control computer 3, by display 4 can real time inspection result of determination, by memory 5 in real time preserve judge knot Really.
In the present embodiment, communication module 1-7 in multiple area monitoring nodes 1 by the way of wired or wireless with control Computer 3 communicates, and the time of underground many places key position generation Secondary cases gas explosion and probability results can be uploaded into calculating Machine 3, memory 5 preserves result of determination for the commanding and decision-making of heat power disaster assistance provides theoretical reference and guidance in real time.
The above, is only presently preferred embodiments of the present invention, and not the present invention is imposed any restrictions, every according to the present invention Any simple modification, change and equivalent structure change that technical spirit is made to above example, still fall within skill of the present invention In the protection domain of art scheme.

Claims (5)

1.矿井热动力灾害救援过程中继发性瓦斯爆炸判定方法,其特征在于该方法包括以下步骤:1. The method for judging the secondary gas explosion in the mine thermodynamic disaster rescue process is characterized in that the method comprises the following steps: 步骤一、确定继发性瓦斯爆炸位置:通过在矿井中多个关键位置处分别安装区域监测节点(1)采集对应区域的温度参数并将该区域的温度参数实时传输至安装在监控室内的控制计算机(3),通过键盘输入模块(2)设置温度参数阈值,采用控制计算机(3)标定达到温度参数阈值的所述关键位置,预判继发性瓦斯爆炸发生的位置;Step 1. Determine the location of the secondary gas explosion: install regional monitoring nodes (1) at multiple key locations in the mine to collect the temperature parameters of the corresponding areas and transmit the temperature parameters of the area to the control panel installed in the monitoring room in real time. The computer (3) sets the temperature parameter threshold value through the keyboard input module (2), adopts the control computer (3) to calibrate the described key position reaching the temperature parameter threshold value, and predicts the position where the secondary gas explosion occurs; 区域监测节点(1)包括区域控制器(1-6)以及与所述区域控制器(1-6)相接的时钟电路(1-5)和通信模块(1-7),区域控制器(1-6)的输入端接有温度传感器(1-1)、风速传感器(1-2)、气体传感器(1-8)、用于采集所监测区域的瓦斯浓度和瓦斯流量的瓦斯监测仪(1-3)以及用于采集所监测区域的氧气浓度和氧气流量的氧气监测仪(1-4);The regional monitoring node (1) includes a regional controller (1-6) and a clock circuit (1-5) and a communication module (1-7) connected with the regional controller (1-6), and the regional controller ( The input terminal of 1-6) is connected with a temperature sensor (1-1), a wind speed sensor (1-2), a gas sensor (1-8), a gas monitor ( 1-3) and an oxygen monitor (1-4) for collecting oxygen concentration and oxygen flow in the monitored area; 步骤二、估计所监测区域发生继发性瓦斯爆炸的时间,过程如下:Step 2. Estimate the time of the secondary gas explosion in the monitored area, the process is as follows: 步骤201、获取所监测区域的环境参数:通过风速传感器(1-2)监测所监测区域的通风状态,通过瓦斯监测仪(1-3)和氧气监测仪(1-4)分别监测所监测区域的瓦斯含量和氧气含量;Step 201, obtain the environmental parameters of the monitored area: monitor the ventilation status of the monitored area through the wind speed sensor (1-2), monitor the monitored area through the gas monitor (1-3) and the oxygen monitor (1-4) respectively gas content and oxygen content; 步骤202、判断所监测区域是否为发生高浓度瓦斯爆炸的区域:通过区域控制器(1-6)设置监测参数变化时间阈值,根据步骤201中获取的环境参数以及时钟电路(1-5)记录的环境参数变化时间,判断灾后所监测区域是否为高浓度瓦斯爆炸区域,当瓦斯监测仪(1-3)和氧气监测仪(1-4)监测灾后所监测区域瓦斯含量和氧气含量达到瓦斯爆炸极限的时间小于所述监测参数变化时间阈值时,说明所监测区域为发生高浓度瓦斯爆炸区域,执行步骤203;否则,执行步骤204;Step 202, judging whether the monitored area is an area where high-concentration gas explosions occur: set the monitoring parameter change time threshold through the area controller (1-6), and record according to the environmental parameters obtained in step 201 and the clock circuit (1-5) The change time of the environmental parameters in the post-disaster monitoring area is used to determine whether the monitored area is a high-concentration gas explosion area. When the limit time is less than the monitoring parameter change time threshold, it means that the monitored area is an area where a high-concentration gas explosion occurs, and step 203 is performed; otherwise, step 204 is performed; 步骤203、高浓度瓦斯爆炸发生的时间估计,过程如下:Step 203, estimate the time when the high-concentration gas explosion occurs, the process is as follows: 步骤2031、根据公式求解微分方程,可获取高浓度瓦斯爆炸区域内氧气浓度变化所经历的时间t1和甲烷浓度变化所经历的时间t2,其中,V为高浓度瓦斯爆炸区域体积,q1为流入高浓度瓦斯爆炸区域内混合气体的流量,q2为流出高浓度瓦斯爆炸区域内混合气体的流量,c1为流入高浓度瓦斯爆炸区域内氧气的浓度,c2为流入高浓度瓦斯爆炸区域内甲烷的浓度,c01为初始条件t1=0时,氧气浓度的初始值,为氧气浓度所要达到的目标值,c02为初始条件t2=0时,甲烷浓度的初始值,为甲烷浓度所要达到的目标值;Step 2031, according to the formula By solving the differential equation, the time t 1 and the time t 2 for the change of the oxygen concentration and the change of the methane concentration in the high-concentration gas explosion area can be obtained, where, V is the volume of the high-concentration gas explosion area, q 1 is the flow rate of the mixed gas flowing into the high-concentration gas explosion area, q 2 is the flow rate of the mixed gas flowing out of the high-concentration gas explosion area, and c 1 is the oxygen flow into the high-concentration gas explosion area c 2 is the concentration of methane flowing into the high-concentration gas explosion area, c 01 is the initial value of oxygen concentration when the initial condition t 1 =0, is the target value of the oxygen concentration to be achieved, c 02 is the initial value of the methane concentration when the initial condition t 2 =0, is the target value to be achieved by the methane concentration; 步骤2032、根据公式计算灾后高浓度瓦斯爆炸区域氧气浓度变成12%所经历的时间T1、瓦斯浓度达到爆炸下限5%所经历的时间T21以及瓦斯浓度达到爆炸上限16%所经历的时间T22Step 2032, according to the formula Calculate the time T 1 for the oxygen concentration to become 12% in the post-disaster high-concentration gas explosion area, the time T 21 for the gas concentration to reach the lower explosion limit of 5%, and the time T 22 for the gas concentration to reach the upper explosion limit of 16 %; 步骤2033、估计高浓度瓦斯爆炸发生的时间:当步骤2032中氧气浓度变成12%所经历的时间T1>T22时,高浓度瓦斯爆炸不发生;当步骤2032中氧气浓度变成12%所经历的时间T21≤T1≤T22时,高浓度瓦斯爆炸发生的时间t满足:T1+t3≤t≤T22+t3,其中,t3为达到瓦斯爆炸极限的气体遇到火源的时间;当步骤2032中氧气浓度变成12%所经历的时间T1<T21时,高浓度瓦斯爆炸发生的时间t满足:T21+t3≤t≤T22+t3Step 2033, estimate the time when the high-concentration gas explosion occurs: when the oxygen concentration becomes 12% in step 2032, the elapsed time T 1 >T 22 , the high-concentration gas explosion does not occur; when the oxygen concentration becomes 12% in step 2032 When the elapsed time T 21 ≤ T 1 ≤ T 22 , the high-concentration gas explosion occurs at a time t that satisfies: T 1 + t 3 ≤ t ≤ T 22 + t 3 , where t 3 is the gas that reaches the gas explosion limit Time to the fire source; when the time T 1 <T 21 for the oxygen concentration to become 12% in step 2032, the time t for the explosion of high-concentration gas satisfies: T 21 +t 3 ≤t≤T 22 +t 3 ; 步骤204、低浓度瓦斯爆炸发生的时间估计,过程如下:Step 204, estimate the time when the low-concentration gas explosion occurs, the process is as follows: 步骤2041、根据公式求解微分方程,可获取低浓度瓦斯爆炸区域内氧气浓度变化所经历的时间t'1和甲烷浓度变化所经历的时间t'2,其中,V'为低浓度瓦斯爆炸区域体积,q'1为流入低浓度瓦斯爆炸区域内混合气体的流量,q'2为流出低浓度瓦斯爆炸区域内混合气体的流量,c'1为流入低浓度瓦斯爆炸区域内氧气的浓度,c'2为流入低浓度瓦斯爆炸区域内甲烷的浓度,c'01为初始条件t'1=0时,氧气浓度的初始值,c'02为初始条件t'2=0时,甲烷浓度的初始值;Step 2041, according to the formula By solving the differential equation, the time t' 1 and the time t' 2 for the change of the oxygen concentration and the change of the methane concentration in the low-concentration gas explosion area can be obtained, where, V' is the volume of the low-concentration gas explosion area, q' 1 is the flow rate of the mixed gas flowing into the low-concentration gas explosion area, q' 2 is the flow rate of the mixed gas flowing out of the low-concentration gas explosion area, c' 1 is the flow rate of the low-concentration gas explosion area The concentration of oxygen in the explosion area, c' 2 is the concentration of methane flowing into the low-concentration gas explosion area, c' 01 is the initial value of oxygen concentration when the initial condition t' 1 =0, c' 02 is the initial condition t' 2 = 0, the initial value of methane concentration; 步骤2042、根据公式计算灾后低浓度瓦斯爆炸区域氧气浓度变成12%所经历的时间T'1、瓦斯浓度达到爆炸下限5%所经历的时间T'21以及瓦斯浓度达到爆炸上限16%所经历的时间T'22Step 2042, according to the formula Calculate the time T' 1 for the oxygen concentration in the low-concentration gas explosion area to become 12% after the disaster, the time T' 21 for the gas concentration to reach 5% of the lower explosion limit, and the time T' 22 for the gas concentration to reach 16% of the upper limit of the explosion ; 步骤2043、估计低浓度瓦斯爆炸发生的时间:当步骤2042中氧气浓度变成12%所经历的时间T'1>T'22时,低浓度瓦斯爆炸发生的时间t'满足:T'21+t'3≤t'≤T'22+t'3;当步骤2042中氧气浓度变成12%所经历的时间T'21≤T'1≤T'22时,低浓度瓦斯爆炸发生的时间t'满足:T'21+t'3≤t'≤T'1+t'3;当步骤2042中氧气浓度变成12%所经历的时间T'1<T'21时,低浓度瓦斯爆炸不发生,其中,t'3为达到瓦斯爆炸极限的气体遇到火源的时间;Step 2043. Estimate the occurrence time of the low-concentration gas explosion: when the time T' 1 >T' 22 when the oxygen concentration becomes 12% in step 2042, the occurrence time t' of the low-concentration gas explosion satisfies: T' 21 + t' 3 ≤ t' ≤ T' 22 + t'3; when the time T' 21 ≤ T' 1 ≤ T' 22 elapsed when the oxygen concentration becomes 12% in step 2042, the time t when the low-concentration gas explosion occurs 'Satisfy: T' 21 +t' 3 ≤ t' ≤ T' 1 + t'3; when the time T' 1 <T' 21 elapsed when the oxygen concentration becomes 12% in step 2042, the low-concentration gas explosion will not Occurrence, wherein, t' 3 is the time when the gas reaching the limit of gas explosion encounters the fire source; 步骤三、估计所监测区域发生继发性瓦斯爆炸的概率:根据瓦斯爆炸事故树分析法,瓦斯爆炸的概率P=P1×P2×P3,其中,P1为灾后所监测区域气体浓度达到瓦斯爆炸极限的概率且P1根据科瓦德爆炸三角形满足:P1=P1i,i=1~4且P11=1>P13>P12>P14=0,P11为瓦斯浓度介于5%~16%之间且氧气浓度大于12%时瓦斯爆炸极限的概率,P12为瓦斯浓度介于5%~16%之间且氧气浓度小于12%时瓦斯爆炸极限的概率,P13为瓦斯浓度大于16%之间且氧气浓度小于12%时瓦斯爆炸极限的概率,P14为瓦斯浓度小于5%时瓦斯爆炸极限的概率,概率P12和概率P13均采用专家评分法估计概率值,P2为灾后所监测区域存在可以引起瓦斯爆炸火源的概率,P3为灾后所监测区域达到瓦斯爆炸极限的气体与火源相遇的概率;Step 3. Estimate the probability of secondary gas explosion in the monitored area: According to the gas explosion accident tree analysis method, the probability of gas explosion P=P 1 ×P 2 ×P 3 , where P 1 is the gas concentration in the monitored area after the disaster The probability of reaching the gas explosion limit and P 1 satisfies according to the Kovad explosion triangle: P 1 =P 1i , i=1~4 and P 11 =1>P 13 >P 12 >P 14 =0, P 11 is the gas concentration Probability of the gas explosion limit when the gas concentration is between 5% and 16% and the oxygen concentration is greater than 12%, P 12 is the probability of the gas explosion limit when the gas concentration is between 5% and 16% and the oxygen concentration is less than 12%, P 13 is the probability of the gas explosion limit when the gas concentration is greater than 16% and the oxygen concentration is less than 12%, and P 14 is the probability of the gas explosion limit when the gas concentration is less than 5%. Both the probability P 12 and the probability P 13 are estimated by the expert scoring method Probability value, P 2 is the probability that there is a fire source that can cause a gas explosion in the monitored area after the disaster, and P 3 is the probability that the gas that reaches the gas explosion limit in the monitored area after the disaster meets the fire source; 步骤四、继发性瓦斯爆炸判定结果显示及实时存储:通过多个区域监测节点(1)同时监测井下所述关键位置发生继发性瓦斯爆炸的时间及概率,并将对应位置处的判定结果实时传输至控制计算机(3),通过显示器(4)可实时查看判定结果,通过存储器(5)实时保存判定结果。Step 4. Display and real-time storage of secondary gas explosion determination results: Simultaneously monitor the time and probability of secondary gas explosions at the key positions in the underground through multiple regional monitoring nodes (1), and store the determination results at the corresponding positions Real-time transmission to the control computer (3), the judgment result can be viewed in real time through the display (4), and the judgment result is saved in real time through the memory (5). 2.按照权利要求1所述的矿井热动力灾害救援过程中继发性瓦斯爆炸判定方法,其特征在于:步骤一和步骤四中所述关键位置包括工作面进风巷道、工作面回风巷道、工作面中部、工作面回风隅角、主进风皮带巷道、前一次矿井热动力灾害发生后高温烟流波及区域和靠近带电电器且异常瓦斯涌出波及区域。2. The method for judging secondary gas explosions in the mine thermodynamic disaster rescue process according to claim 1, characterized in that: the key positions in step 1 and step 4 include the air inlet tunnel of the working face and the return air tunnel of the working face , the middle of the working face, the return air corner of the working face, the main air inlet belt roadway, the area affected by high-temperature smoke flow after the previous mine thermodynamic disaster, and the area near live electrical appliances and affected by abnormal gas gushing. 3.按照权利要求1所述的矿井热动力灾害救援过程中继发性瓦斯爆炸判定方法,其特征在于:步骤三中概率其中,N为专家人数,p12j为第j位专家给出的瓦斯浓度介于5%~16%之间且氧气浓度小于12%时瓦斯爆炸极限的概率,δj为p12j对应的权重且p13j为第j位专家给出的瓦斯浓度大于16%之间且氧气浓度小于12%时瓦斯爆炸极限的概率,δ'j为p13j对应的权重且 3. According to the method for judging the secondary gas explosion in the mine thermodynamic disaster rescue process according to claim 1, it is characterized in that: in step 3, the probability Among them, N is the number of experts, p 12j is the probability of the gas explosion limit given by the jth expert when the gas concentration is between 5% and 16% and the oxygen concentration is less than 12%, δ j is the weight corresponding to p 12j and p 13j is the probability of the gas explosion limit given by the jth expert when the gas concentration is greater than 16% and the oxygen concentration is less than 12%, δ' j is the weight corresponding to p 13j and 4.按照权利要求1所述的矿井热动力灾害救援过程中继发性瓦斯爆炸判定方法,其特征在于:步骤三中概率其中,概率P21为灾后所监测区域火源为持续性火源的概率且P21=1,概率P22为灾后所监测区域火源为瞬时性火源的概率且0≤P22≤1。4. According to the method for judging the secondary gas explosion in the mine thermodynamic disaster rescue process according to claim 1, it is characterized in that: in step 3, the probability Among them, the probability P 21 is the probability that the fire source in the monitored area after the disaster is a persistent fire source and P 21 =1, and the probability P 22 is the probability that the fire source in the monitored area after the disaster is a transient fire source and 0≤P 22 ≤1. 5.按照权利要求1所述的矿井热动力灾害救援过程中继发性瓦斯爆炸判定方法,其特征在于:步骤三中概率P3=1。5. The method for judging secondary gas explosions in mine thermodynamic disaster rescue process according to claim 1, characterized in that in step 3, the probability P 3 =1.
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