HYDRODYNAMIC STUDIES IN FISCHER-TROPSCH DERIVED WAXES IN A BUBBLE COLUMN

Gas hold-up and Sauter mean bubble diameter measurements were made in a 0.051 m diameter by 3 m long glass bubble column in the system, nitrogen-molten wax, with three different waxes (paraffin wax FT-300, Sasol's Arge wax and Mobil's reactor wax). Paraffin wax has a tendency to foam and gas hold-up is a strong function of gas distributor type, temperature and start-up procedure, whereas the reactor waxes do not foam and are much less affected by these variables, In experiments at 265°C with a 1.85 mm single hole orifice plate distributor the gas hold-ups were nearly the same for all three waxes. However, significant differences in Sauter mean bubble diameters were obtained in experiments with different waxes; FT-300 wax produced the smallest Sauter mean bubble diameters whereas Mobil's reactor wax produced the largest bubbles. Addition of 1-octadecanol and octadecanoic acid (up to 10wt%) to the FT-300 paraffin wax caused an increase in gas hold-up and a delay in the foam break-up in runs at 265°C with the 1.85 mm orifice plate distributor.     

气升式内环流反应器中油滴的分散特性

本文研究了气升式内环流反应器中油滴的分散特性。以对数正态分布密度函数为油滴尺寸的分散模型,导出了油滴的Sauter平均直径解析式。对模型作了实验验证,关联了模型参数。提出了油滴的尺寸分布密度函数和Sauter平均直径的半经验式。结果表明计算值与实验值吻合良好。     

气固错流移动颗粒床过滤器压降特性研究

研究了错流移动颗粒床过滤器操作压降与过滤介质特性、表现过滤气速、颗粒层移动速度和床层粉尘沉积量之间的关系。结果表明，无粉尘沉积时，床层压降可以用Ergun方程计算。颗粒层移动速度的变化并不会造成床层压降的显著变化。除尘过程中，床层内粉尘沉积量随气体中粉尘浓度的增大、颗粒层移动速度的减小而增加，同时将导致床层压降的显著增大。错流移动床除尘操作压降可以用带修正项的Ergun方程计算，其修正项为比沉积率和颗粒层空欧率的函数。在实验数据范围内，该方程的计算结果与实验数据最大偏差小于15％。     

水质条件对厌氧氨氧化颗粒污泥EPS含量的影响

为研究水质条件对厌氧氨氧化颗粒污泥EPS含量的影响,采用16个SBR反应器研究同周期内基质利用阶段与基质匮乏阶段EPS含量的变化以及总氮质量浓度、IC/TN、COD/TN对于厌氧氨氧化颗粒污泥EPS含量的影响.结果表明,同周期内,基质利用阶段的EPS含量不断升高,基质匮乏阶段EPS含量不断降低;总氮质量浓度为35~280 mg/L时,提高总氮质量浓度可以提高EPS的含量,总氮质量浓度280 mg/L时EPS含量有所减少;IC/TN为0.01~0.2时,EPS及其各组分含量随无机碳质量浓度的升高而增加,IC/TN0.2时,无机碳质量浓度对于EPS及其各组分含量无明显影响;COD/TN0.5时,有机物对于EPS含量具有促进作用,COD/TN0.5时,有机物的提高对于EPS含量有抑制作用.在厌氧氨氧化颗粒污泥工艺的实际运行过程中,应避免过长的基质利用阶段与基质匮乏阶段,总氮质量浓度应保持在150~210 mg/L,无机碳质量浓度应保持在IC/TN为0.1~0.2,有机物质量浓度应保持在COD/TN0.5.     

使用驾驶人瞳孔直径的固定物冲突识别方法

以寻找可反映驾驶人心理负荷的交通冲突识别指标及基于该指标的交通冲突识别方法为目的,通过比较分析明确了冲突刺激与瞳孔直径的相关关系,针对原始GSA(gravitational search algorithm)识别方法仅可搜索最优解的缺陷并面向交通冲突识别要求提出了基于瞳孔直径的GSA-T交通冲突快速识别方法.撞固定物冲突验证结果显示GSA-T方法的对比次数和识别时间均比枚举方法少,证明GSA-T方法具有较低时间复杂度和空间复杂度的优势,可满足交通冲突识别和道路安全评价的要求.     

软土地区旧桩拔除技术和新建桩基础调整方案及施工措施

结合天津南开区某地块定向经济适用房项目,介绍其在基础施工中遇到旧预制方桩时,采用全套管高压喷气、射水振动沉管施工工艺清孔拔桩,并对该工艺进行分析得出:该拔桩施工工艺适用于软土地区旧桩拔除项目;并针对旧桩孔无法回填压实、部分新建桩基础与拔除旧桩孔距离较近等原因导致钻孔倾斜、串孔等问题,提出远离旧桩位置或调整至旧桩桩心位置等方法调整桩位,并采用加大桩径、增设承台等调整方案承担因调整桩位而产生的上部偏心荷载;采用拌和白灰、分层压实、回填静置等措施提高回填土的密实度,采用保证垂直度和调节泥浆配合比等措施,以改善不良施工条件,得出适当增加混凝土充盈系数保证成桩质量等施工经验,为后续类似工程提供借鉴。     

散粒体的自组织临界性分析

基于二维模拟实验,研究竖向荷载下散粒体中的自组织临界性,揭示细观拱效应与宏观大崩塌的变化规律,以及拱效应与材料性质的关系.散粒体中每个小自组织的临界发展过程包括自组织搭拱、拱随遇平衡和拱崩塌的动力学演化.散粒体大坍塌是众多小自组织临界发生后的力学性质由量变到质变的过程.用随机理论细观探讨一个预期失败模式的理论模型,为研究散体材料结构自组织临界性系统的可预测性及灾害预测预报提供了科学依据.     

基于归一负荷矩的配电网台区低电压治理研究

对不同线径电力架空线负荷矩的研究表明:当单位长度线路上具有相同电压降时,线路负荷矩随着导线型号的变化而变化。深入分析线路负荷矩与导线截面之间的内在联系,突破了传统方法只能进行同型导线计算的瓶颈,对不同线径架空线进行归一化处理,确定台区实施线径更换的最优段域。该方法已应用于线路低电压治理分析中,实际工程监测数据表明该方法具有较强的可行性、经济性和应用价值。     

变直径空心件楔横轧收口模拟研究

采用楔横轧技术,对变直径空心件收口成形工艺进行研究。根据工件尺寸,使用UG建立不同方案下的模具,将模具设计和数值模拟相结合,模拟工件的成形过程。对比模拟结果,得出最佳的成形方案,并改进成形工艺参数,最终确定了变直径空心件楔横轧工艺的成形方案。     

Influence of bubble diameter and solids concentration on bubble stability: Development of a novel analytical approach

The properties and thickness of the bubbles in the froth control the flotation process. There is no work showing how to measure bubble film composition and thickness by a straightforward manner. In this work, a novel approach, a custom-designed bubble cell associated with layer interferometry（in the UV-vis region） and FT-IR spectroscopy was used to investigate the effect of solid particle type（hydrophilic vs hydrophobic）, concentration and bubble diameter on stability of a bubble blown in air. Stability was quantified by measuring bubble lifetime and hydrated film thickness. Kerosene with silicone oil as a foaming agent was used to evaluate the impact of bubble diameter（test series I）. Frother solutions（MIBC, Dowfroth 250, Hexanol and F-150） were used for the solid type concentration experiments（test series II）. In the first series of experiments, it was determined that as the diameter of a bubble increased from 10 to 25 mm, so did the hydrated film thickness from 350 to 1000 nm. In the second series, as the silica concentration increased（0 to 10%）, an increase in bubble lifetime and hydrated film thickness was resulted（130%-250%）. An impact of solid hydrophobicity was found but to a lesser degree than expected. It is possible that the small particle size（〈0.1 m） of silica was responsible for this behavior. The findings are used to interpret the effect of solids in flotation froth.