煤自燃发火潜伏期不同温度下耗氧特性的研究

为了探究地层温度的升高对采空区自燃倾向性的影响,对处于自燃潜伏期的煤展开耗氧特性和CO释放特性的研究。通过对长平矿3#煤分别进行20~60℃的封闭耗氧实验,得到了自燃潜伏期不同温度下煤的氧浓度以及CO浓度随时间变化的曲线。对氧浓度变化曲线和CO浓度变化曲线进行拟合分析得到了不同温度下煤的氧气消耗和CO生成速度,同时得到了氧浓度衰减系数和CO浓度增长系数。封闭耗氧实验结果表明:从20~60℃氧气消耗速度逐渐增大并且氧浓度衰减系数呈指数增长,CO浓度增长系数也逐渐增大并且同样呈指数增长,煤的窒熄带氧浓度临界值从20~60℃逐渐由16.8%降低到12.4%。为探究不同温度下采空区煤的自燃发火危险性,将封闭耗氧实验结果的参数应用到采空区CFD数值模拟仿真中,模拟得到随着温度升高采空区窒熄带临界氧浓度位置由200 m增长到380 m。结果表明:常温下不易自燃的煤在较高的环境温度下表现出了较强的氧气消耗和CO释放能力,并且采空区自然氧化带随着温度的升高动态变宽,增大了采空区的自燃发火危险性。     

凯达煤矿采空区煤自燃极限参数分析*

为更加精准地判定采空区自燃危险区域,对煤自燃极限参数的计算方法进行改进,采用能量守恒微分方程的分析解计算煤自燃所需必要条件的极限值;以内蒙古凯达煤矿为例对该方法进行验证,根据浮煤的物性参数以及采空区环境条件,计算分析46205工作面回风侧采空区煤的自燃危险性;根据采空区漏风条件以及煤自燃所需要的氧浓度值,分析在遗煤较厚的条件下采空区可能发生的煤自燃危险性,划分不同遗煤条件下采空区自燃危险区域。结果表明:采空区实际遗煤厚度无法满足浮煤持续升温的要求,通过分析煤自燃极限参数可知,自然条件下浮煤在升温达到约30 ℃时其温度不再增加,因此不具有自燃危险性。     

基于非线性渗流模型采空区漏风流场数值模拟

针对采空区非线性渗流模型中颗粒平均粒径的取值问题,利用专业的流体力学软件fluent对刘庄矿151305工作面采空区不同颗粒粒径下的漏风流场进行了模拟,以此确定合适的平均粒径,并利用该采空区颗粒平均粒径对工作面供风量及采空区漏风的影响进行了模拟与分析。结果表明,采空区内平均粒径的取值对工作面风量分布影响较大,瓦斯抽采负压也相差一个数量级;通过与实测工作面风量及实际的瓦斯抽采负压作对比,当采空区颗粒平均粒径取0.1 m时,模拟结果与现场实际最为吻合;工作面供风量越大,采空区的漏风量也越大,两者为二次函数关系。该研究方法为工作面采空区漏风流场数值模拟提供了理论指导。     

不同粒径易自燃煤常温氧化实验研究*

为探究易自燃煤在常温条件下的氧化特性,自行设计煤常温封闭氧化实验装置,采用实验研究与回归分析2种方法,分析易自燃煤发生氧化反应的气体变化过程,探究3种粒径煤样在20 ℃有限空间内的耗氧与产气特征。结果表明:易自燃煤样在16 d常温封闭氧化过程中,容器内O2体积浓度呈指数衰减、CO和CO2体积浓度呈指数增长的变化规律;在0.06~0.83 mm范围内,粒径越大,易自燃煤耗氧速率越大,CO和CO2产生速率则先增大后减小;介于中间的粒径为0.13~0.25 mm易自燃煤氧化反应最强烈,更容易发生氧化。研究结果对揭示生产环境温度下煤粒粒径对煤自燃的影响有一定的意义。     

基于“O”型冒落的Y型通风采空区气体分布特征

为了掌握Y型通风采空区气体的分布规律,进一步为采空区瓦斯及火灾防治工作提供理论依据,基于采空区“O”型冒落压实和遗煤耗氧的非均匀性,针对Y型通风系统建立非均质采空区内气体渗流数值模型,采用Fluent数值模拟软件对采空区漏风流场和各组分气体浓度场进行模拟分析。结果显示:瓦斯和氧气浓度场在Y型通风采空区内大致呈“L”形分布;风流集中由工作面上、下隅角进入采空区;沿空留巷侧的瓦斯浓度高于运输巷侧,而氧气浓度却恰恰相反;两进一回的Y型通风方式能有效解决瓦斯在工作面上隅角积聚的问题;在采空区深部靠沿空留巷侧存在一个扇形的高瓦斯浓度区域,而该区域氧气浓度较低;采空区自燃危险区域在运输巷侧分布更广,应适当采取防火措施。     

基于IIAHP-Entropy-ssd的采空区遗煤自燃危险性评价模型及应用

为了能够对煤矿采空区遗煤自燃危险性进行准确判定,提出基于IIAHP-Entropy-ssd最优综合赋权模糊评价模型。首先,结合影响采空区遗煤的自燃性及环境影响因素,建立危险性评价指标体系,并确定各评价指标的分级准则;其次,利用区间数代替数值评价打分,并运用可能度互补矩阵进行修正的改进区间数层次分析法（IIAHP）,结合熵权法（Entropy）,根据现场实测数据,得出各评价指标的主、客观权重,并运用离差平方和（ssd）的最大化思想进行最优综合赋权,克服评价过程中主、客观因素对评价结果的影响,运用属性数学理论,建立各评价指标的隶属函数;最后,运用该模型对忻州窑矿8914综放工作面采空区遗煤自燃危险性进行评价,并与现场实际情况进行对比,结果表明:该模型的评价结果与实际情况基本一致,验证了该评价模型的准确性,为采空区遗煤自燃危险性评价提供参考和借鉴思路。     

贫氧环境对煤低温氧化特性影响研究

浅埋藏煤层开采过程中,由于地表裂隙导致的漏风,使其经常处于变化的氧浓度场中。针对这一实际情况,利用煤氧化动力学测定系统,对煤样在21%,18%,14%,10.5%,5%,3%氧浓度下,进行程序升温试验。测得了不同温度下指标气CO,C2H4,C2H6,C3H8浓度,并分析了其随温度变化规律,测量并计算了不同氧浓度下交叉点温度以及升温速率;对氧浓度大小影响指标气产量和其随温度变化幅度原因,以及温度特征影响效果进行必要的机理分析。结果表明:不同氧浓度下指标气CO,C2H4,C2H6在70 ℃左右有明显产量变化,分别在120 ℃,125 ℃,120 ℃处开始大量释放,C3H8则在温度达到125 ℃左右开始大量释放;120 ℃前,各氧浓度下煤样温度按相同规律变化,120 ℃后,氧浓度越大则对应的升温速率越大,温度也越高;氧浓度不同影响了煤中脂肪烃侧链氧化产生-OH的过程,继而造成指标气产量与温度变化差异。     

氧浓度对煤低温氧化热效应影响规律研究

为了准确掌握氧浓度对煤低温氧化热效应的影响,采用C80微量量热仪研究低温阶段煤氧化的自热过程,根据单升温速率的非等温动力学分析方法,得到不同氧浓度下煤样的活化能。研究结果表明:氧浓度对实验初始阶段的热流曲线和放热量的影响较小,随着温度的升高,氧浓度对热流曲线和放热量影响逐渐变得明显,放热趋势随着氧浓度的增大而增强;煤样的初始放热温度随着氧浓度的增大而降低;活化能随着氧气浓度的降低呈阶梯式上升;总放热量和氧浓度服从线性方程y=ax+b;与21%（空气气氛）氧浓度相比,15%,10%和5%氧浓度下煤的放热量分别降低了约19%,33%和46%,表明降低氧浓度对煤样的氧化放热具有明显的减缓作用。因此可以加强采空区的密闭性检测、注入惰性气体,使采空区的氧浓度尽可能地低,对采空区煤自热升温的防治有着理论指导意义。     

Low-temperature oxidation of coal at elevated pressures

A mathematical model is presented to describe steady-state mass transfer and oxidation processes in coal at low temperatures in a fixed-bed flow reactor. The model incorporates the effects of partial pressure of oxygen, temperature and coal particle size, and accounts for the rate of coal oxidation and the composition of oxygenated products at high pressures. This is an important development since previous models did not include the effect of pressure in their formulation. It is found that, when the partial pressure of oxygen increases the rate of oxygen consumption increases accordingly. However, the influence of partial pressure of oxygen on the rate of oxidation is less pronounced when the pressure surpasses 1 MPa. In addition the model predicts that, for a constant partial pressure of oxygen, higher rates of oxygen consumption occur at lower total pressures. The same trends are also found for the concentration of oxygenated products at the reactor outlet. It is suggested that, the variation of partial pressure of oxygen leads to different concentration levels of oxygen at the surface and within the pores of coal particles, substantially affecting the rate of oxidation.     

炮采放顶煤采空区自然发火的数值模拟应用

针对炮采放顶煤开采采空区容易发生自燃问题，基于漏风渗流方程、气体渗流一扩散-氧消耗方程，建立了采空区自然发火非稳定数值模型，采空区按非均质考虑，耗氧汇按煤矸氧化和瓦斯涌出稀释两方面综合考虑，用有限元数值方法联立求解模型。结合羊草沟矿实例，通过该矿自然发火后来的测试区的现场实测结果，拟合反演得到采空区煤的耗氧速度、瓦斯涌出强度和渗透特征参数，用确定的模型分析了前段出现自然发火的原因；描绘了炮采放顶煤开采时采空区冷却带、自燃带和窒息带等三带的形状，指出冒落压实的不均衡的非均质采空区，自燃点在偏人风一侧。用三带划分理论讨论了工作面参数（风量、推进度、控顶距）同自燃的量化关系，提出了从根本上预防采空区自然发火的途径与方法。     

The relationship between oxygen consumption rate and temperature during coal spontaneous combustion

Spontaneous combustion is a major natural disaster in coal production. In the process of exploring coal self-ignition, a series of hypotheses have been put forward, most scholars agree that the current coal-oxygen compound theory. Oxygen consumption rate reflects the status of coal spontaneous combustion, and it is also one of the parameters necessary for numerical simulation of coal spontaneous combustion. In this paper, a coal heating and oxidation experiment was designed, Experimental device consists of heating and oxidation furnace, gas chromatograph, temperature control and data acquisition systems and other equipment components. Three coal samples whose weight each is 5 g were selected for the study. By experiment, oxygen concentration at the inlet and outlet of temperature oxidation furnace was measured. Oxygen consumption rate is calculated in the heating process of coal according to air flow. In the Cartesian coordinate system, the temperature as abscissa and the oxygen consumption rate for the longitudinal coordinates, drawing the relationship between oxygen consumption rate and temperature plot. And then regression analysis was used to analyze the relationship between oxygen consumption rate and coal temperature during the heating and oxidation process of coal. The results show that the oxygen consumption rate and temperature of coal were linear relationships both before and after the critical temperature when the coal temperature is less than 180 °C. Before the critical temperature oxygen consumption rate is low, however it increases rapidly when coal temperature reaches a critical temperature. The result is important for the prevention and treatment of spontaneous combustion of coal.     

Evaluation of the spontaneous combustion characteristics of coal of different metamorphic degrees based on a temperature-programmed oil bath experimental system

Research on the micro- and macrocharacteristics of different metamorphic degrees of coal helps improve the control and protection techniques used during spontaneous combustion. Nine coals with different properties were thoroughly investigated in this study. Fourier transform infrared spectroscopy and a self-designed temperature-programmed oil bath experimental system were adopted to analyze the molecular structure and macrocharacteristic parameters of the spontaneous combustion of coal. Additionally, the influence of particle size on spontaneous combustion was considered. Various functional groups were employed as microcharacteristic parameters to capture the principal active groups in oxidation. The gas production rate, oxygen consumption rate, gas concentration, heat energy release rate, and characteristic temperatures were evaluated as macrocharacteristic parameters to investigate the changes in coal during oxidation. The results establish that the microcharacteristics of coal molecules determine the degree of spontaneous combustion based on intrinsic properties and that changes in the macrocharacteristics of the spontaneous combustion of coal reflect the microstructural changes. The contents of the hydroxyl groups, carbonyl groups, alkyl ether and aryl ether in the coal molecules gradually decrease with the metamorphic increase. Oxygen-containing functional groups have higher reactivities and easily react with oxygen, causing the macroparameters, such as the oxygen consumption rate, the gas generation rate and the heat energy release rate, to consistently decrease with the increase of the metamorphic degree. Small-particle-size coal molecules have more active aliphatic hydrocarbons, oxygen-containing functional groups and a larger specific surface area, increasing the chances of adsorbing the oxygen of active groups and promoting the reaction between coal and oxygen. The experimental results indicate that coal samples with higher metamorphic degrees or larger sizes exhibit lower tendencies toward spontaneous combustion. Evaluation of the spontaneous combustion of coal based on a temperature-programmed oil bath experimental system is of great practical importance for preventing the spontaneous combustion of coal during storage, processing and utilization and can serve as a convenient reference for production safety in mining applications.     

立体抽采条件下高瓦斯采空区煤自燃危险性预测

为准确预测高瓦斯采空区煤自燃的状况,通过分析发现高抽巷是监测采空区遗煤自然发火的最有效地点。推算出采空区气体在高抽巷中所占的体积分数,进而确定采空区遗煤不同的燃烧阶段所对应的CO体积分数和CO指数。结果表明:当高抽巷中的CO体积分数Chdr CO<30×10-6或CO指数ICO<0.5%时,采空区的遗煤处于低温氧化阶段;当高抽巷中的CO体积分数Chdr CO≥30×10-6或CO指数ICO≥0.5%时,采空区遗煤进入自然发火危险阶段,此时必须采取措施控制采空区自燃氧化的进一步发展。对80501工作面的采空区煤自燃成功地进行预测预报,实现了安全生产。     

基于因子交互作用矩阵的采空区危险度评价研究

基于因子交互作用影响矩阵及采空区危险度影响因子分析,选取12个采空区危险度主要影响因子,建立采空区危 险度多因子交互作用矩阵模型。通过专家打分法,确定各影响因子相互作用权值,得到影响矩阵对单一因子的影响值及 单一因子对矩阵系统的影响值,从而得出采空区危险度因子影响权重表。分析影响权重表,得到对采空区影响最大的因 子为矿柱尺寸及分布和岩体断裂及破损带。采用差值法,对采空区危险度进行等级划分,最后得到采空区危险度分级图 。经过实例验证,影响矩阵法分析评价结果与实际吻合,表明采用影响矩阵法评价采空区危险度是可行的,具有实际应用 意义,可在实际矿山工程中应用推广。     

单轴应力对煤自燃特性参数和导热系数的影响研究

为探究单轴应力作用下煤氧化和传热特性,利用自制荷载加压煤自燃特性参数测定装置对炉体内长焰煤煤样进行程序升温。结合程序升温过程中煤临界温度Tc和Tg,对其进行阶段划分:阶段1为30℃~Tc;阶段2为Tc~Tg。计算了不同单轴应力下2个阶段煤表观活化能和平均耗氧速率。根据能量守恒得出程序升温过程煤导热系数随温度的变化,进一步分析煤导热系数与单轴应力的关系。结果表明:阶段1单轴应力为4 MPa时为临界轴压,煤表观活化能最大,平均耗氧速率最小;阶段2煤表观活化能和平均耗氧速率随单轴应力增大均呈抛物线变化,单轴应力为2.7 MPa时为临界轴压,煤表观活化能最大,平均耗氧速率最小;阶段1和2煤导热系数随温度升高均先减小后增大,并且煤导热系数随单轴应力增大呈三次函数变化。     

考虑煤体粒度的落煤瓦斯涌出预测模型研究*

为了探究不同煤体粒度对于工作面瓦斯涌出的影响规律,以王家岭煤矿为研究对象,通过现场测试分析采落煤与放落煤的粒度分布,采用数值模拟计算不同粒度煤体的瓦斯涌出特征;并推导采落煤和放落煤的瓦斯涌出预测模型,对模型进行现场应用。研究结果表明:王家岭煤矿采落煤粒度分布范围更广,存在较高比例的微小粒度和大粒度煤体;煤体粒度越小,则瓦斯涌出速度越快。采落煤和放落煤的综合涌出强度均可以用指数函数来描述,模型计算结果与现场实际数据误差在合理范围内。     

Changes in the reaction regime during low-temperature oxidation of coal in confined spaces

A study of the initial stage of the low-temperature oxidation of coal is important, not only for the prevention for fires in coal industry, but also in reducing emissions of hazardous gases. A batch reactor was introduced and a series of simulated experiments of coal oxidation was carried out in this paper. The time-dependent rates of CO emission and oxygen consumption during oxidation experiments of coal samples with different particle size ranges were obtained simultaneously from the measurements of CO and O₂ concentration in the reactor. The experimental results show that the rate of CO emission presents three stages in the duration of coal oxidation. Based on the rates of oxygen consumption, the reaction order and reaction rate were obtained from the reaction rate equation. These results indicate that the reaction regime switches during coal oxidation in confined spaces. The initial decrease of reaction rate is due to the decrease of the active sites in coal. While the decrease of reaction rate in the following period of coal oxidation is attributed to the reaction-inhibition mechanism of oxidation products. And it is mainly represented by the chemisorption sequence of coal oxidation. The oxidative activity of coal can be restored when the oxidation products are evacuated. A mechanism of low-temperature oxidation of coal in confined spaces was also suggested.     

易自燃厚煤层工作面自然发火CO预测及防治

为了有效预防遗煤自燃,深入研究自然发火初期的CO预测技术。基于回风隅角CO源的理论模型,以Gambit建立相似二维采场模型,数值模拟了采空区自燃“三带”范围,并采用现场束管监测手段对结果进行了验证。利用程序升温实验获得了不同温度段回风隅角CO的极限指标,并与现场实测值对比分析,进而预判采空区遗煤发火程度,为制定有针对性的防治措施提供理论指导。研究结果表明:CO作为低温氧化阶段预测指标对预防遗煤自燃具有重要作用。     

采空区遗煤自燃升温过程的数值模型及其应用

基于漏风渗流方程、氧浓度渗流-扩散-消耗方程和传热方程,建立了采空区自然发火非定常数值模型,并用迎风格式的有限元方法联立求解.结合实例,从理论上描绘了采空区漏风渗流、氧浓度分布和温度分布,以及它们随时间的加速变化过程,同时给出自燃的附产物CO的分布情况,重点给出了遗煤的自燃耗氧与升温的量化关系.结果表明,通常情况下采空区高温区偏在入风一侧,边界漏风对高温区有一定影响.与传统的采空区冷却带、自燃带和窒息带的三带划分相比,该模型能对自然发火问题给出更准确的解.模拟的自燃升温是加速的过程,同基于实验分析和实际观测得到的规律基本一致.     

采空区开区注氮灭火温度场冷却过程的数值模拟

为研究开区注氮条件下,采空区遗煤自燃被抑制和熄灭作用复杂力学过程(原理),由非均质多孔介质中的渗流连续性方程、气体弥散方程和综合传热方程的联立,建立了注氮采空区煤自燃的非定常数值模型。结合实例,用迎风格式有限元方法求解。计算在不同情况下采空区自燃高温点熄灭过程,以图形方式给出了采空区的漏风流态、氮气流态,描绘灭火降温过程中,采空区氧、CO和温度分布的动态变化过程。提出了对自燃早期火灾施行开区注氮灭火的方法和适用的判定准则。理论计算得到开区注氮灭火分为两个阶段过程,即原火源熄灭和新自燃氧化区形成并自燃。指出实施开区注氮灭火应准确把握注氮时机和防止新自燃氧化区形成的工作面开采推进时机;并配合降低漏风措施条件下进行注氮。