含硫化物废水在升流式填料塔中的处理及数学模拟

在升流式填料塔中,通过接种排硫硫杆菌形成稳定生物膜.在pH值和温度分别控制在 7. 0±0. 1和 30±2℃条件下,进水质量浓度分别为 85. 76, 177. 83, 269. 55和 394. 26mg/L时,改变硫化物容积负荷 (VLR)和溶解氧水平进行正交试验.研究和分析硫化物容积负荷与溶解氧共同作用下硫化物的去除规律、硫酸盐的生成规律以及单质硫的生成率,并对建立的模拟方程进行了验证.结果表明,在升流式生物填料塔内废水中的硫化物去除率能达到9500以上;应用模拟方程,对于不同的进水浓度,都能找到一个最佳的运行工况.在硫化物去除率和单质硫的生成率达到最佳时,保持反应器的最大容积负荷和最小的溶解氧.     

高温高压振动丝黏度仪的研制

在振动丝技术的基础上,设计和制造出一种黏度仪,其工作原理是将截面为圆形的振动丝浸在待测液体中,然后让振动丝进行垂直于中心轴线的横向振动,从而测定流体的黏度和密度,写出了相应的工作方程,并对振动丝黏度仪的设计和操作过程进行了描述.振动丝黏度仪主要包括振动丝传感器、温度控制系统、压力控制系统和信号调节系统.确定了仪器的操作参数,测定了正己烷在298.15~403.15K、0.10MPa和5.1MPa两个压力条件下的黏度和密度.比较实验数据和文献数据可知,本仪器测量密度时测量误差小于±0.50/0,测量黏度时的测量精度为±0.50/0,测量误差在±2.00/0以内.目前该仪器已经用于高温高压液体黏度和密度的测定.     

晋城矿区综采放顶煤工作面顶煤冒放性分析

根据晋城煤业集团综采放顶煤开采实际情况,从影响顶煤冒放性的煤体裂隙、开采工艺和支架与围岩关系3个方面进行分析,对综放工作面的布置、采放比、放煤步距、支架架型与工作阻力提出了建议.     

NaCl状态方程的分子动力学模拟

利用在分子动力学中引入壳层模型方法，模拟了高温高压下NaCl的状态方程．在压强上升到300kbar的广泛温度范围内，分子动力学模拟的状态方程和实验值吻合的很好，同时也进一步研究了温度300K压强上升到300kbar时NaCl的体积压缩率．     

冲击破煤过程中能量耗散的理论分析

介绍了能量在冲击式破煤过程中的产生、传递和耗散过程以及能量最终的分布范围;运用应力波的方法分析了应力波在煤体中传播过程,并得出能量在衰减过程中衰减率的计算方法;还分析了剥落厚度的计算方法,并得出正弦应力波在煤体中传播时的冲劈厚度和最大煤块尺寸的关系;根据冲击规律和能量的传递特征对能量的传递过程进行了分析,并求出冲击消耗能量和最小散逸能之间的关系,指出了要使煤块破碎必须满足冲击消耗能量要大于最小散逸能。     

深过冷Cu-20Wt%Pb亚偏晶合金的凝固行为

采用熔融玻璃净化和循环过热相结合的方法，使Cu-20wt％Pb亚偏晶合金获得了208K的深过冷，在宽过冷范围内研究了Cu-Pb亚偏晶合金的组织演化规律。结果表明，过冷合金熔体初生相为α(Cu)，在0～146K的过冷度范围内，均有两次再辉现象；在183～208K的过冷范围内，只出现一次再辉。当△T≤98K时，合金凝固组织为粗大枝晶α 枝晶间Pb相；当116K△≤T≤146K时，凝固组织已无明显的枝晶形貌，组织由细密α基体 细小的Pb颗粒组成；当△T≥183K时，凝固组织与中等过冷度下的组织相似，只是Pb相更细小，分布更均匀。当△T≥133K时试样出现裂纹。     

煤与生物质共超临界水催化气化制氢的实验研究

在压力为20～25MPa、停留时间为15～30s、：NaOH添加量(质量分数)为0．1％、反应器外壁温度为650℃的条件下，对煤与生物质的模型化合物羧甲基纤维素钠(CMC)在超临界水环境中的催化气化制氢性能进行了研究，探讨了物料浓度、压力以及停留时间对煤与CMC共气化制氢的影响．实验结果表明：煤与CMC二共超临界水催化气化制氢的主要气体产物是H2、CO2和CH4，H2的体积分数可高达60％以上；增加物料浓度、升高压力有利于提高产氢率，但延长停留时间不利于氢气的制取．     

水合活化固硫装置脱硫效率试验研究

通过建立水合活化固硫试验装置，研究装置的工艺特性对装置脱硫率的影响规律．试验结果表明，各因子对脱硫率的影响程度由大到小依次是：水钙摩尔比、钙硫摩尔比、二氧化硫量、烟气入口温度和停留时间；在其他因子保持不变的前提下，装置的脱硫率分别随各单项因子的增加而有不同程度的提高．试验研究的结果验证了本文中探讨的水合活化固硫机理——反应发生在气、液、固三相之间，雾化水滴和吸收剂颗粒碰撞并在其表面形成液膜是固硫反应的前提．     

The fate of injectant coal in blast furnaces: The origin of extractable materials of high molecular mass in blast furnace carryover dusts

The aim of the work was to investigate the fate of injectant coal in blast furnaces and the origin of extractable materials in blast furnace carryover dusts. Two sets of samples including injectant coal and the corresponding carryover dusts from a full sized blast furnace and a pilot scale rig have been examined. The samples were extracted using 1-methyl-2-pyrrolidinone (NMP) solvent and the extracts studied by size exclusion chromatography (SEC). The blast furnace carryover dust extracts contained high molecular weight carbonaceous material, of apparent mass corresponding to 10⁷?10⁸ u, by polystyrene calibration. In contrast, the feed coke and char prepared in a wire mesh reactor under high temperature conditions did not give any extractable material. Meanwhile, controlled combustion experiments in a high-pressure wire mesh reactor suggest that the extent of combustion of injectant coal in the blast furnace tuyeres and raceways is limited by time of exposure and very low oxygen concentration. It is thus likely that the extractable, soot-like material in the blast furnace dust originated in tars is released by the injectant coal. Our results suggest that the unburned tars were thermally altered during the upward path within the furnace, giving rise to the formation of heavy molecular weight (soot-like) materials.     

Influence of overpressure on coalbed methane reservoir in south Qinshui basin

In theory, from the high temperature and pressure during the coal generating gas to the present low temperature and pressure of coalbed methane reservoir, the accumulation of coalbed methane was from oversaturated to undersaturated. The gas content of the coalbed methane reservoir in the south Qinshui basin was 12-35.7 m3/t. According to the isotherm and measured gas content of No. 3 coal, the adsorbed gas content in some wells was highly saturated and oversaturated, which was hard to theoretically understand. In addition, there were no thermogenic and biogenic gases at the late stage in the south Qinshui basin. This article proposed that the overpressure was the main reason for the present high saturation of the coalbed methane reservoir. In early Cretaceous, the coalbed methane reservoir was characterized by overpressure and high saturation caused by gas generation from coal measure source rocks. In late Cretaceous, the coalbed methane reservoir was rapidly uplifted, and with the temperature and pressure decreasing, the pressure condition of adsorbed gas changed from overpressure to normal-under pressure, which resulted in the high saturation and gas content in the present coalbed methane reservoir.