黄金冶炼厂污染源治理技术

本文阐述了采用加温加压无氰解吸、金电解精炼，活性炭酸洗、火法再生产工艺，所产生污染物的治理技术。     

B113－2型低汽／气比CO高温变换催化剂的研制

介绍了Ｂ１１３－２Ｍ低汽／气比ＣＯ高温变换催化剂的研制方法及其特点．实验室测试表明，Ｂ１１３－２型催化剂具有堆密度低、运行强度高、选择性好、抗沸水性能优、本体含硫低及低温活性好等优点．     

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%.     

异丁醛合成2,4,6-三异丙基-1,3,5-三噁烷的研究

本文以异丁醛为原料在杂多酸催化剂的作用下，环化合成了无毒升华剂2，4，6－三异丙基－1，3，5－三恶烷，考查了各种反应条件的影响，确定以磷钨酸为催化剂时的最佳反应条件：反应温度25℃，催化剂用量1．5％，反应时间2．5h，产物的收率达84％以上。     

非叠氮化物气体发生剂的设计与研究

通过正交实验研究了新型非叠氮化物可燃剂PAK与混合氧化剂的燃烧性能 ,找到了适用于汽车安全气囊用的气体发生剂PAK - 2的组成。 60L压力舱实验结果表明 ,PAK - 2气体发生剂达到了国际同类产品的技术要求     

2-氨基-4-溴-5-氯苯甲酸的合成

以硝基苯为原料，经溴化、还原、缩合、环合、氯化和氧化等６步反应合成了２－氨基－４－溴－５－氯苯甲酸，总收率为１１．７％。     

下喷式环流反应器环隙气含率影响因素

下喷式环流反应器是一种用于强化气-液两相反应过程的新型装置，虽然已在工业上有了较广泛的应用，但对其理论研究远未成熟，其工业装置的设计仍依赖于实验和经验。本文借助实验室自制实验装置，对下喷式环流反应器环隙气含率的影响规律进行了研究。首先，对喷射器的吸气量进行了测量，获得了不同条件下喷射器最大吸气量的性能曲线；在此基础上，分别研究了气相流量、液相流量以及喷射器安装位置对环隙气含率的影响规律。结果表明：气相流量和液相流量对气含率具有重要的影响，随着气相流量和液相流量的增大，气含率快速提高，而喷嘴位置对气含率的影响相对较小；考虑到增加气相流量和液相流量所需要的能耗和设备代价，通过增加液相流量来达到提高气含率的目的是优选方案。     

7-氨基-6-氰基-5-(3-硝基苯基)吡喃并嘧啶-2,4-二酮的合成

报道了常温、超声辐射、水中、无催化剂条件下，以3-硝基苯甲醛、丙二腈和巴比妥酸为原料合成标题化合物的方法。考察了超声技术、反应时间及反应温度对反应的影响。最佳反应条件为：室温、超声辐射2h，收率为86．2％。     

6-硝基-1,2-重氮氧基-4-萘磺酸及其杂质的高效液相色谱分析

本文以反相高效液相色谱对6-硝基-1，2-重氮氧基-4-茶磺酸及有机杂质进行了分析，选择了流动相、离子对、检测波长，研究了不同牌号ODS C18色谱柱的重现性，得到了6-硝基-1，2-重氮氧基-4-萘磺酸及杂质(1，2-重氮氧基-4-萘磺酸、8-硝基-1，2-重氮氧基-4-萘磺酸)的相关系数分别为：0.99956、0.99991、0.99317；标准偏差和变异系数分别为：0.214250％、0．016890％、0．564557％、0.012695%、0.488467％、0.014560％得到了准确度数据，确定了最小检出量。     

STUDY ON PERMEATION OF ACETONE/NITROGEN MIXED GAS THROUGH AL2O3 MICROPOROUS MEMBRANES: MOLECULAR DYNAMICS

In this work, by applying Materials Studio 2.2 software package, molecular dynamics (MD) was performed to investigate the dynamic processes of 1:4 acetone/nitrogen mixed gas permeating through different Al₂O₃ microporous membranes. Three systems were modeled by considering different box lengths, microporous sizes, and textures of Al₂O₃ membranes to compare different permeation behaviors. In each system, initial mixed gas contained 20 acetone molecules and 80 nitrogen molecules, and its density was set to 0.1 g/cm³. Analysis on the concentration profiles of nitrogen molecules (N2) and acetone molecules (Ace) in each system at different sampling times was implemented to discuss the permeation behaviors of smaller N2 and larger Ace. The results showed that adsorption and diffusion occurred synchronously but adsorption was dominant for acetone molecules and that the adsorption on the floor surface of the feed gas region more easily reached equilibrium (local equilibrium) than the diffusion and the adsorption on the ceiling of the initially vacuum region. Furthermore, for nitrogen, adsorption followed diffusion. Higher temperature is in favor of the enrichment of acetone on the floor surface of the feed gas region but against the adsorption of nitrogen. The adsorptive layer was found to be a double-layer with COMPASS force field and to be a monolayer with PCFF force field.