煤层瓦斯含量测定定点取样方法研究进展

基于文献调研及前期研究,分析了目前煤矿井下煤层瓦斯含量直接测定时所采用定点取样方法及其弊端,阐述了学者们提出的改进型定点取样方法,并对煤层瓦斯含量测定定点取样方法的研究进行了展望,指出:①取样过程瓦斯损失量小、取样时升温低、机械复杂度低是基于煤芯管法定点取样方法的发展方向;②开展煤储层条件下的瓦斯运移规律研究,建立并完善各种基于煤芯管法的定点取样方法的瓦斯损失量模型;③适用于松软煤层的定点取样方法的研发亟待开展;④基于负压气力输送理论的定点取样方法是定点取样方法研究的趋势,动态颗粒煤变负压瓦斯解吸规律是建立对应瓦斯损失量模型的基础研究。     

张集矿综采工作面瓦斯治理措施及效果分析

张集矿属于煤与瓦斯突出矿井,针对目前所开采的17266工作面地质构造条件复杂、瓦斯涌出量大、处于突出危险区等瓦斯治理难题,采取"风排瓦斯、高抽巷穿层钻孔抽采、运输巷、回风巷顺层钻孔抽采和上隅角埋管抽采"等瓦斯综合治理措施,用分源预测法得出工作面绝对瓦斯涌出量为30.3 m3/min。结果表明,工作面的主要瓦斯涌出来源为本煤层瓦斯涌出。工作面风排瓦斯量11.0 m3/min,工作面瓦斯抽采率达63.0%以上。     

含固率和接种比对叶菜类蔬菜垃圾厌氧消化的影响

通过叶菜类蔬菜垃圾中温批式厌氧消化实验,比较了含固率(3%、5%、7%)和接种比(1.5、2.5、3.5)对产甲烷效果的联合影响.结果表明,在研究实验参数范围内,含固率越低、接种比越高,越有利于缩短产甲烷反应迟滞期,平均日产甲烷速率越快.经过52d的培养,在含固率为3%、接种比为3.5的工况中,平均日产甲烷速率最快,达到9.5mL/(gVS?d),日最大产甲烷速率最快,达到49.8mL/(gVS?d),最早进入快速产甲烷期.当接种比为3.5时,随着含固率的升高,产甲烷速率下降,迟滞期延长,但单位底物累计产甲烷量增大,含固率7%时单位底物累计净产甲烷量为481mL/gVS.而当接种比为1.5时,含固率为5%和7%的工况均无法启动甲烷化反应,含固率为3%的工况的产气迟滞期达15d.挥发性有机酸的累积抑制甲烷化反应的启动,迟滞期随着液相中有机酸浓度的增加而延长,当有机酸浓度低于1260mg/L,甲烷化反应没有明显的迟滞期.     

预处理方法对香蒲厌氧发酵联产H2-CH4效能的影响

通过厌氧发酵动力学分析、还原糖及其他代谢产物变化情况,结合香蒲微观结构解析,系统研究酸(HCl)、碱(NaOH)、酶(纤维素酶R-10)3种预处理对水生植物厌氧发酵联产H₂-CH₄的影响. 结果表明:香蒲分别经酸、碱、酶3种预处理后,厌氧发酵联产累积H₂、CH₄产量及含量均显著提高,c(HCl)、c(NaOH)均为1.0mol/L, w(纤维素酶R-10)(以底物计)为10mg/g时,预处理最佳. 其中1.0mol/L NaOH预处理香蒲效果最佳,φ(H₂)(H₂含量)达30.09%,累积产H₂量(以香蒲干质量计)达11.39mL/g;φ(CH₄)(CH₄含量)最高达67.48%,累积产CH₄量(以香蒲干质量计)达41.87mL/g;还原糖利用率达50.87%,sCOD(溶解性化学需氧量)利用率达66.17%. 纤维素酶预处理后香蒲产CH₄能力显著提高,产CH₄阶段φ(CH₄)最高为71.39%,累积产CH₄量达46.32mL/g,还原糖利用率达72.10%. 扫描电镜微观结构分析表明,碱预处理对香蒲纤维素结构破坏程度最大,可有效增加香蒲与微生物接触面积,有利于厌氧发酵联产H₂-CH₄工艺的快速启动和稳定运行.      

沸石滤池深度处理石化废水二级出水研究

采用小试规模沸石滤池,深度处理石化废水二级出水,通过考察滤池对CODCrNH4^-N和挥发酚的去除情况,分析了沸石去除污染物的规律和机理。结果表明：沸石滤池对CODCr,NH4^＋-N和挥发酚的平均去除率分别达到27．32％、94．67％和34．47％。在滤池运行初期,离子交换起主要作用。随着反应器的运行,离子交换因沸石饱和而减弱,而生物氧化逐渐起作用。由于沸石资源丰富、价格低廉和性能优越,所以沸石滤池作为三级深度处理技术具有广阔应用前景。     

内循环流化床烟气脱硫装置结构及流化性能

提出了开发一种新型内循环流化床烟气脱硫装置的设想,通过不同型式床顶、床底结构的试验,确定了实现这一构想的最佳流化床结构型式;研究了冷态条件下该装置内床料流化的状态及固含率轴向分布情况,初步考察了其流体力学性质.实验结果表明,气速在2.5～5m/s时,装置能实现大量固体颗粒的内循环,床料在床内的运动呈"环-核"结构,床内固体颗粒物浓度高于传统等径流化床,可将其用于烟气脱硫工艺.     

Restoration of hyper-eutrophic water with a modularized and air adjustable constructed submerged plant bed

A modularized and air adjustable constructed submerged plant bed (CSPB) which can be used to restore the eutrophic water is introduced in this paper. This plant bed helps hydrophyte grow under poor conditions such as frequently changed water depth, impaired water transparency, algae bloom and substantial duckweed in summer, which are not naturally suitable for growing hydrophyte. This pilot study in Waihuan River of Tianjin, China, revealed that reduction of Chemical Oxygen Demand (COD), Total Nitrogen (TN) and Total Phosphorus (TP) by the use of CSPB could be reached 30%–35%, 35%–40%, 30%–40% respectively in the growing season (from March to October) and 5%–10%, 5%–15%, 7%–20% respectively in the winter (from November to February) when the detention time was 6 d. The relationships between the concentration of COD, TN, TP and the detention time fit the first-order kinetic equation well and the coefficients of determination (R²) were all above 0.9. The attenuation coefficients k of the kinetic equation were a function of the water temperature. When the water temperature was quite low or quite high, k was not significantly changed with increasing or decreasing water temperature. While when the temperature was in a moderate range, an increase or decrease of water temperature would lead to a rapid increase or decrease in k.     

Control of chlorinated aromatic compounds from a municipal solid waste incinerator using limestone addition

In this study, limestone powder was directly added to synthetic MSW, which was fed into a small‐scale fluidized bed incinerator. The concentration of CBzs and CPs in the flue gas were measured before and after a secondary combustion air injection. Finally, the PCDDs and PCDFs concentrations were also measured in the flue gas after the secondary combustion zone. The CaCO₃ added to synthetic MSW not only controls HCl in the flue gas, but suppresses the formation of chlorinated aromatic compounds like CBzs, CPs, PCDDs, and PCDFs. The main mechanisms to control the formation of chlorinated aromatic compounds was more likely related to the suppression of catalytic capability of flyash than the HCl reduction in the flue gas. However, the NO concentration was increased by catalytic reaction of limestone in the fluidized bed.     

UASB+生物接触氧化工艺处理饮料废水

介绍采用升流式厌氧污泥床反应器(UASB反应器)+生物接触氧化工艺处理饮料废水的工艺设计和运行效果。运行结果表明:此工艺能有效处理饮料废水,COD、BOD5平均去除率分别达95.8%和98.1%,出水水质达DB 61/224—2006《陕西省渭河水系污染物排放标准》的一级排放标准。     

巨厚砾岩下冲击地压发生机理及加固技术研究

针对深部矿井巨厚砾岩下采场冲击地压的易发性和危险性,运用理论分析和室内相似材料模拟试验方法,对华丰煤矿巨厚砾岩下覆岩运动规律及采场冲击地压发生机理进行研究。研究发现:随着工作面的推进,离层自下而上发育,在巨厚砾岩层下部离层空间达到最大。煤层极限平衡区内集中静载荷能量E静和巨厚砾岩破断、垮落释放的集中动载荷能量E动是造成采场冲击地压的根本原因,并且E动诱发冲击地压的强度更高,危险性更大。当E静+E动-Ef min>0时,采场冲击地压启动。在此基础上,提出一种囊袋式离层加固技术,对离层区域进行横向挤压和纵向加固,有效控制巨厚砾岩断裂、垮落,防止冲击地压的发生,减少地表沉陷,实现了煤矿安全绿色开采。