乙醇-盐-水-5-Br-PADAP体系萃取分离测定钯

研究了在硫酸铵存在下 ,5 Br PADAP乙醇体系中Pd(Ⅱ )、Rh(Ⅲ )、Pt(Ⅳ )的萃取行为及乙醇溶液的分相条件 ,讨论了影响萃取率的各种因素 ,试验表明 ,室温下 ,一定 pH范围内 ,该体系中的Pd(Ⅱ )几乎可完全被乙醇相萃取 ,而Rh(Ⅲ )、Pt(Ⅳ )不被萃取或萃取率很低 ,从而可实现Pd(Ⅱ )、Rh(Ⅲ )、Pt(Ⅳ )混合离子的定量分离 ,同时建立了Pd(Ⅱ )的测定方法。乙醇相中Pd(Ⅱ ) 5 Br PADAP配合物表观摩尔吸光系数为 1.18× 10 5L·mol- 1·cm- 1,钯量在 0～ 9.6 0 μg/10ml范围内符合比耳定律 ,检出限为 0 .0 90 μg/10ml。用该法分离混合样和测定两种活性碳钯催化剂中钯 ,结果满意     

Theoretical and Experimental Study on the Adsorption and Desorption of Methane by Granular Activated Carbon at 25 ℃

A theoretical and experimental study was conducted to accurately determine the amount of adsorption and desorption of methane by various Granular Activated Carbon(GAC)under different physical conditions.To carry out the experiments,the volumetric method was used up to 500 psia at constant temperature of 25℃.In these experiments,adsorption as well as desorption capacities of four different GAC in the adsorption of methane,the major constituent of natural gas,at various equilibrium pressures and a constant temperature were studied.Also,various adsorption isotherm models were used to model the experimental data collected from the experiments.The accuracy of the results obtained from the adsorption isotherm models was compared and the values for the regressed parameters were reported.The results shows that the physical characteristics of activated carbons such as BET surface area,micropore volume,packing density,and pore size distribution play an important role in the amount of methane to be adsorbed and desorbed.     

Adsorption of Carbon Dioxide on Activated Carbon

The adsorption of CO2 on a raw activated carbon A and three modified activated carbon samples B, C, and D at temperatures ranging from 303 to 333 K and the thermodynamics of adsorption have been investigated using a vacuum adsorption apparatus in order to obtain more information about the effect of CO2 on removal of organic sulfur-containing compounds in industrial gases. The active ingredients impregnated in the carbon samples show significant influence on the adsorption for CO2 and its volumes adsorbed on modified carbon samples B, C, and D are all larger than that on the raw carbon sample A. On the other hand, the physical parameters such as surface area, pore volume, and micropore volume of carbon samples show no influence on the adsorbed amount of CO2. The Dubinin-Radushkevich (D-R) equation was the best model for fitting the adsorption data on carbon samples A and B, while the Preundlich equation was the best fit for the adsorption on carbon samples C and D. The isosteric heats of adsorption on carbon samples A, B, C, and D derived from the adsorption isotherms using the Clapeyron equation decreased slightly increasing surface loading. The heat of adsorption lay between 10.5 and 28.4 kJ/mol, with the carbon sample D having the highest value at all surface coverages that were studied. The observed entropy change associated with the adsorption for the carbon samples A, B, and C (above the surface coverage of 7 ml/g) was lower than the theoretical value for mobile adsorption. However, it was higher than the theoretical value for mobile adsorption but lower than the theoretical value for localized adsorption for carbon sample D.     

载体和担载酸对乙烯直接氧化合成乙酸反应的影响

 在固定床流动反应器上研究了Pd－酸／载体体系催化乙烯直接氧\r\n化合成乙酸的反应，并对载体相同但担载酸强度不同的催化剂的催化活\r\n性进行了比较．结果表明，担载酸的强度明显影响催化剂的活性，酸强\r\n度越大其催化活性越高．用NH3－TPD和异丙醇脱水探针反应表征了二氧\r\n化硅、活性碳和酸性白土三种载体担载的Pd－H4SiW12催化剂的酸性，\r\n并测试了三种催化剂的催化活性．结果表明，载体通过影响担载酸的强\r\n度而影响催化剂的活性，载体上的强酸中心越多，催化剂的活性越高．\r\n测定了二氧化硅、活性碳和酸性白土三种载体担载的Pd－H4SiW12催化\r\n剂上Pd的分散度，并与其催化活性相关联．结果表明，决定乙烯直接氧\r\n化生成乙酸反应活性的主要因素是催化剂的酸强度而不是Pd的分散度．     

活化条件对活性碳纳米管比表面积的影响

以KOH为活化剂, 研究了多壁碳纳米管在制备活性碳纳米管过程中四个重要影响因素: 活化剂用量、活化温度、活化时间和活化过程中保护气体的流速对所得活性碳纳米管BET比表面积的影响并解释了原因. 研究表明上述四个因素都会对活性碳纳米管的比表面积产生较大的影响, 其中活化剂用量的影响最大, 在研究范围内可引起比表面积增大约241 m²•g^-1. 在这四个影响因素中除活性碳纳米管的比表面积随活化温度的增加而不断增加外, 其他三个影响因素的变化都会使活性碳纳米管的比表面积出现最大值, 而且四个影响因素的改变, 都不改变活性碳纳米管的孔洞主要是中孔和大孔的特点.     

载体对负载型TiO2催化剂光催化性能的影响

 以活性碳（AC）和镁铝尖晶石（MA）为载体，采用真空吸附水解法制备了负载型光催化剂TiO2／AC和TiO2／MA，并采用TiO2溶胶负载法制备了活性碳负载催化剂TiO2（C）／AC．以氯仿为探针分子研究了其在催化剂上的吸附及光催化降解反应性能．结果表明，催化剂的制备方法、TiO2负载量与载体的吸附性能对光催化活性有明显的影响．通过优化制备条件，TiO2／AC催化剂的催化活性可提高到纳米TiO2的2．5倍．氯仿在AC上的饱和吸附量较高，但吸附强度较弱；在纳米TiO2上的吸附情况则正好相反．氯仿在AC和TiO2上吸附性质的差异有利于吸附在TiO2／AC上的氯仿分子从活性碳载体向TiO2光催化活性中心迁移．镁铝尖晶石载体对光催化反应没有明显的促进作用，与其基本上不吸附氯仿分子有关．与TiO2胶体负载法相比，真空吸附水解法是一种较好的负载型TiO2光催化剂制备方法．     

氯苯处理下小麦幼根生理学指标的变化及活性炭对氯苯毒性缓解作用的研究

以小麦幼根为材料,研究了不同浓度氯苯(1％,2％,3％,4％,5％)对小麦幼根生理学指标的影响及活性炭对小麦幼根的保护作用.结果显示,氯苯造成了小麦幼根生物量(根长、鲜重和干重)的下降,同时升高了小麦幼根细胞死亡水平、可溶性蛋白含量、丙二醛含量、活性氧含量以及抗氧化酶活性.表明氯苯对小麦幼根造成生长抑制,增加了氧化压力...     

管道直饮水生产工艺及效益浅析

介绍了管道直饮水工艺的基本原理及特征，详述了东营市安居小区分质供水工艺的流程及设计参数，并展望了其工艺的发展前景。     

光质对怀山药微型块茎诱导形成的影响

在不加活性碳的情况下,无论是固体培养或是液体培养在各光质下均不利于微型块茎的诱导.而在加入活性碳的固体培养基上,各光质均有利于微型块茎的诱导;尤以红光和白光下最好,诱导率达到100%,微型块茎的体积和可溶性糖含量也达到了最大.     

Ti(SO4)2/C催化合成邻苯二甲酸二异戊酯(DIAP)

研究了Ti(SO4 ) 2 /C在邻苯二甲酸酐和异戊醇酯化中的催化性能 ,结果表明 ,Ti(SO4 ) 2 /C在该反应中具有较高的催化活性 ,并得到了合成邻苯二甲酸二异戊酯的新工艺条件是 :催化剂用量 (邻苯二甲酸酐质量分数 )为 5 % ;异戊醇 0 5mol,邻苯二甲酸酐 0 2mol,反应温度 185℃ ,反应时间 180min ,在此条件下收率可达 95 %。