用人工神经网络方法预测鼓泡塔气含率

A new correlation for the prediction of gas hod up in bubble columns was proposed based on an extensive experimental database set up from the literature published over last 30 years .The updated estimation method relying on artificial neural network,dimensional analysis and phenomenological approaches was used and the model prediction agreed with the experimental data with average relative error less than 10%.     

交联球形壳聚糖树脂制备方法研究

介绍了壳聚糖－乙酸溶液制备交联球形壳聚糖树脂的方法，考察了各种制备因素对产品性能的影响，得到了较为合适的反应条件。产品溶酸性能、吸附性能有较大提高，并且容易再生。     

磷块岩浮选机的放大方法研究(Ⅰ)——实验室扩试确定放大准则

在12立升充气搅拌式磷块岩浮选机和12立升自吸搅拌式磷块岩浮选机的传递特性研究以及验证两区综合模型的合理性基础上,提出了磷块岩浮选机放大的准则是传质条件相似(k_La)_1=(k_La)_2和悬浮条件相似(W/V_F)=(W/V_F)_2。     

充填浮选柱捕集区气含率的试验研究

通过冷模试验方法考察了充填浮选柱捕集区的气含率，经试验数据回归分析，气含率εｇ＝０．０９６Ｊｇ０．９１（Ｈｃ／Ｄ）－０．１８。并结合漂移通量的理论，确定充填浮选柱的捕集区为近似均匀鼓泡流。     

酯交换法合成碳酸二苯酯研究进展

对碳酸二苯酯合成用催化剂、合成工艺、反应装置等进行了综述。认为国内应加强酯交换法合成碳酸二苯酯的基础研究 ,尽快实现其产业化     

秸秆蒸汽汽爆、固态发酵处理结合快速热解制液体燃料

为了改善生物质热解油的品质,引入了蒸汽汽爆、固态发酵对生物质进行了分级处理脱除其中半纤维素和纤维素,降低了生物质的羧基和羟基含量.研究了生化处理改变生物质组分对其快速热解及其热解产品的影响.结果表明,汽爆、发酵处理使得焦产率增加,油产率略有增加,热解气产率降低;除汽爆处理增加了CO2外,汽爆、发酵处理对热解气形成的规律影响较小;汽爆、发酵处理脱除半纤维素、纤维素后,醋酸降低了36%～49%,羟基丙酮减少了25.0%～38.5%,而酚类产物明显增加.油品的热值也由原麦秸的16～17MJ/kg增加到22～24MJ/kg.     

中空纤维超滤膜去除乳酸钙中蛋白质的研究

发酵法联合生产乳酸-乳酸钙工艺中,分离出的乳酸钙产品含有蛋白质、还原糖、重金属等杂质,影响产品的品质。本实验研究了中空纤维膜对乳酸钙中蛋白质的去除,并分析了压差、温度、浓度及pH值等因素的影响。得到了较好的工艺操作条件为Δp=0.05MPa,Δ=30g/L,30°C,pH=4。进一步提出用多步超滤能提高蛋白质的去除率15%～27%。     

云南中低品位胶磷矿加工利用技术方案研究

针对云南沉积型磷矿储量大、品位较低、矿石类型复杂的特点,提出了胶磷矿加工利用新的工艺技术路线.在数字矿床与生产配矿技术研究的基础上确定出最优入选矿石品位,通过详细解析磷矿石的工艺矿物学特征制定出最佳选矿工艺和高效浮选药剂,为合理地利用中低品位胶磷矿提供重要的技术支撑.     

Flow of gas-liquid-solid system and its application in packed flotation column

A packed flotation column, which is packed with multiple board ripple packings, was described. Based on comprehensive steady state models, chemical reactor developed previously in chemical engineering subjects, have been extended to packed flotation column for mineral separation. The experimental results verify that tarts in series model is better than axially-dispersed plug flow model to describe flow pattern in the collection zone of column by RTD (residence time distribution), and the error of experimental data and calculated data of both models are 0. 07 % - 0. 1% and 0. 18 % - 0.45 % respectively. And, RTD of gas phase was also considered, results also show that gas in the whole column appears plug flow. The cleaning process through adding wash water in froth zone of column was described, and the effect of superficial air vdodty and superficial wash water vdocity on the cleaning action of froth zone were discussed. Flotation experiment for single column was conducted for phosphate ores. The recovery for P2Os was 85.8%, and the grade was 26.8%.     

振动流化床中氢气还原分解磷石膏

在振动流化床中对氢气还原分解磷石膏反应进行了研究,考察了氢气体积分数、反应温度、气体流量、床层高径比及反应时间对磷石膏分解反应的影响.结果表明:随着氢气浓度升高,分解率有增大趋势,但脱硫率先增加后减少;反应温度越高以及物料高径比越小,分解率与脱硫率越高;过高或过低的气体流量都不利于磷石膏的分解,当气体流量为242 mL/min时,分解率与脱硫率最高;并且反应时间越长,磷石膏分解越充分,但应设定范围.当还原分解温度1 050℃,氢气体积分数为5%,物料高径比为1.2,气体流量为242 mL/min(u=20 umf),反应时间为60 min,磷石膏的分解率与脱硫率分别能达到98.78%和84.24%,能满足磷石膏制酸联产水泥的要求,可用于指导磷石膏还原分解制酸联产水泥的新工艺研究.