U型工作面上隅角埋管瓦斯抽采数值模拟研究

传统的U型通风工作面上隅角瓦斯积聚现象经常出现，严重制约着矿井正常生产能力的有效发挥，对矿井安全生产造成重大威胁。基于前人对采空区非均质多孔介质气体运移理论的研究，采用Fluent软件数值模拟研究了U型和上隅角埋管条件下U型通风系统的静压力场和瓦斯浓度场。研究结果表明：在相同的模型参数条件下，U型通风容易造成上隅角瓦斯积聚，上隅角瓦斯超限问题十分严重；采空区5m处埋管，治理上隅角瓦斯积聚的效果欠佳，达不到安全开采的条件；15m处埋管可以较好的解决上隅角瓦斯超限问题，工作面没有出现瓦斯积聚现象，工作面和回风巷的瓦斯浓度始终处于1％以下；25m处埋管的效果与15m基本相同，没有表现出更好的瓦斯治理效果。综合数值模拟的结果，确定了上隅角埋管抽放采空区瓦斯的理想抽放位置为距离地板垂高1．2m、沿走向深入采空区15m处。     

采场通风方式与瓦斯运移规律研究

采场是煤矿生产的核心地带,而采场通风系统是确保采场作业安全,创造良好生产环境的重要环节。本文以采场风流流动及瓦斯运移理论为基础,通过现场试验、模型模拟试验及计算机模拟研究等方法,着重研究了中国常用的和有发展前途的走向长壁后退式U型通风方式、U+L型通曲方式、后退式Y型通风方式条件下采场风流流动及瓦斯运移规律。     

O&M SPENDING LEVELS IN THIRD WORLD IRRIGATION SYSTEMS: EXPLORING ECONOMIC ALTERNATIVES1

ABSTRACT: Third World irrigation and drainage systems have experienced major declines recently in both capability and performance. This is due initially to working them well beyond their design capaci-capacities; scouring, sedimentation, and overtopping result. Chronic O&M underfunding then adds heavily to this worsening malaise. International donors have assisted irrigation departments with rehabilitation projects and programs to improve O&M effectiveness on a grand (billions of dollars) scale. Despite their historical propensity to examine, almost fastidiously, program economic justifications (B/C, IRR, etc), the donors apparently have glossed over two basic analytic elements for (a) more spending on O&M as distinct from an equivalent spending on other means to provide farmers with an m³ of water; and (b) different levels of O&M spending on canals and drains. Surely those different levels provide differing benefits, in total, and at the margin. Which level is most economic? This paper identifies these latter analytical issues, posits methodologies key to an O&M spending level analysis, and discusses the information base. Particular attention is paid to identifying relevant costs and benefits, and to suggesting supplementary criteria for O&M spending level selection. The paper is an exercise in delineation of an imminently practical area of irrigation engineering economics.     

矿井主通风机叶轮磨损失效的评价

矿井主通风机叶轮严重磨损威胁着矿井安全生产 ,研究主通风机叶轮磨损和正确地评价叶轮的磨损失效 ,对煤矿安全生产具有重大的现实意义。应用气—固两相流动理论分析了主通风机叶轮的磨损部位 ,结论与现场叶轮的实际磨损相吻合。提出了叶轮磨损过程的 3个阶段。利用材料磨损理论分析了主通风机叶轮磨损机理 ,得出了叶轮磨损是以气体动力学磨料的冲蚀磨损为主 ,低应力擦伤型磨料磨损、腐蚀磨损为辅的结论。依据国家标准 ,结合矿井主通风机工作特点 ,从安全角度提出了矿井主通风机叶轮磨损永久失效的判据 ,并给出了判定标准。     

化学事故救援方舱舱室环境安全性模拟研究

运用计算流体动力学(CFD)方法,对具有超压防护功能的某化学事故应急救援手术方舱室内气体污染物运动扩散的规律以及对人员安全的影响进行了数值模拟,其研究结果表明:当大气环境中氢氰酸(HCN)浓度为5mg/L时,前10s从常规进风口进入舱室的HCN在滤毒通风装置开启后,随气流运动逐渐向整个舱室扩散,经净化空气的混合稀释作用,绝大部分通过舱体缝隙排出舱室,30min内舱室HCN浓度的总量下降了95.1%,说明超压防护很好地保证了舱室环境的安全性。     

矿井采掘工作面通风效果的综合评价

运用模糊综合评价法对矿井采掘工作面进行了通风效果的评价,先确定了影响工作面通风效果的指标,并逐一构造了其隶属函数,然后采用层次分析法定出评价指标的相对权重,最后对计算模糊评判的算法进行了分析,以此来确定采掘工作面通风效果的评价等级。以东滩煤矿部分采掘工作面的环境状况为例进行了评价,据实际考察评价结果反映,通过该评价方法得到的结果与现场完全一致。     

船舶载运煤炭甲烷释放特性研究

为了研究船舶载运煤炭甲烷释放规律,基于Fick扩散定律建立了货舱甲烷体积分数计算模型,分析了不同扩散系数条件下甲烷释放量与时间的关系,确定了空隙系数的取值范围,通过对某船舶煤炭运输过程中甲烷体积分数随船实测对模型进行了验证.结果表明,货舱甲烷体积分数随运输时间增加而增加,扩散系数为1.0×10-8 cm2/s时,甲烷释放量达到极大值;煤炭的空隙系数基本在0.53～ 0.57 m3/t之间.当煤炭极限甲烷解吸量为1.6 ～ 3.83 m3/t时,货舱甲烷最高体积分数在0.53％ ～ 1.22％,5个货舱中4个货舱的甲烷释放量与理论计算相吻合,1个货舱的最大甲烷释放量高出理论计算量6％,船运煤炭过程中的甲烷释放计算模型与实测结果较为吻合.对于甲烷体积分数超限的货舱,及时通风可使甲烷体积分数迅速降低,有效地解决船运煤炭过程中甲烷体积分数超限的问题.     

特长公路隧道火灾烟气沉降特性对人员疏散影响的研究*

为研究特长公路隧道火灾烟气沉降对人员疏散安全的影响,通过数值模拟方法,对0,1.0,1.5 m/s和临界风速值4种不同纵向通风风速下隧道火灾烟气沉降特征进行研究,并分析不同风速下烟气沉降对人员疏散的影响。研究结果表明:在无纵向风时,烟气沉降现象较为明显,烟气下沉造成的不均匀烟气温度、能见度分布,提前终止人员疏散的进行;随着纵向风速的增加,沉降现象仍存在,但沉降点后移,对人员疏散的影响减小;在1.5 m/s的纵向通风条件下,火源下游500 m范围内烟气基本不发生沉降且能维持分层,此时几乎不影响火灾下游人员疏散。在实际应用中,火灾初期可先以1.5 m/s的分层风速值进行通风,待下游人员疏散后,再施加临界风速加快烟气排出。研究结果可为特长公路隧道火灾防治和疏散救援提供参考。     

Aerobic treatment of palm oil mill effluent

In this study treatment of palm oil mill effluent (POME) was investigated using aerobic oxidation based on an activated sludge process. The effects of sludge volume index, scum index and mixed liquor suspended solids during the acclimatizing phase and biomass build-up phase were investigated in order to ascertain the reactor stability. The efficiency of the activated sludge process was evaluated by treating anaerobically digested and diluted raw POME obtained from Golden Hope Plantations, Malaysia. The treatment of POME was carried out at a fixed biomass concentration of 3900+/-200mg/L, whereas the corresponding sludge volume index was found to be around 105+/-5mL/g. The initial studies on the efficiency of the activated sludge reactor were carried out using diluted raw POME for varying the hydraulic retention time, viz: 18, 24, 30 and 36h and influent COD concentration, viz: 1000, 2000, 3000, 4000 and 5000mg/L, respectively. The results showed that at the end of 36h of hydraulic retention time for the above said influent COD, the COD removal efficiencies were found to be 83%, 72%, 64%, 54% and 42% whereas at 24h hydraulic retention time they were 57%, 45%, 38%, 30% and 27%, respectively. The effectiveness of aerobic oxidation was also compared between anaerobically digested and diluted raw POME having corresponding CODs of 3908 and 3925mg/L, for varying hydraulic retention time, viz: 18, 24, 30, 36, 42, 48, 54 and 60h. The dissolved oxygen concentration and pH in the activated sludge reactor were found to be 1.8-2.2mg/L and 7-8.5, respectively. The scum index was found to rise from 0.5% to 1.9% during the acclimatizing phase and biomass build-up phase.