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The supported catalyst was systematically optimized with respect to catalyst dosage and calcination temperature.

实验了催化剂的负载量和煅烧温度对催化剂活性的影响。

The results showed that new-type solid ferric potassium alum was a good catalyst for the synthesis of ethyl decanoate and the optimum conditions were as follows: molar ratio of acid to alcohol was 1∶2, the use level of catalyst was 0.6 g/0.05 mol capric acid, water-taking reagent benzene was...

结果表明,新型固体酸铁钾矾是合成癸酸乙酯的良好催化剂,在酸醇物质的量比为1∶2,催化剂用量为0.6g(0.05mol癸酸),带水剂苯为15mL,反应时间为2.5h的条件下,癸酸乙酯的酯化率可达98%。

The results showed that new-type solid ferric potassium alum was a good catalyst for the synthesis of ethyl decanoate and the optimum conditions were as follows: molar ratio of acid to alcohol was 1:2, the use level of catalyst was 0.6g/0.05 mol capric acid, water-taking reagent benzene was 15 mL, reaction time was 2.5 h and the yield of ethyl decanoate could reach 98%.

结果表明,新型固体酸铁钾矾是合成葵酸乙酯的良好催化剂,在酸醇物质的量比为1:2,催化剂用量为0.69(0.05 mol癸酸),带水剂苯为15mL,反应时间为2.5h的条件下,癸酸乙酯的酯化率可达98%。

With the increasing of content of catalyst, the residue of Salix, Caragana and Poplar all dropped, the residue was lowest when content of catalyst was 7%.

随着催化剂用量的增加,沙柳、柠条和杨木的残渣率都下降,在催化剂用量7%时都达到最低。

It has also been studied that the influence of the cementite formation in catalyst Pt-Fe/C,as it is heated. In the end,the adsorptive oxygen on catalyst surface has been evaluated.

本文对铂铁合金催化剂中形成渗碳体的情况亦做了初步研究,分析了渗碳体的形成对催化剂性质的影响。

Here we applied many types of cinchona alkaloid derivatives and otherβ-aminoalchohol compounds in IFB reactions and investigated the effects of solvent, temperature and catalyst amount on the enantioselectivities in order to find the proper catalyst and optimize reaction condition.

本文考察了多种金鸡纳生物碱衍生物及其它一些β-氨基醇类化合物在IFB反应中的应用,并研究了催化剂的结构、溶剂效应、温度、催化剂用量及反应底物类型对立体选择性的影响,以筛选适合的催化剂和优化反应条件。

4The obtained solid alkali catalyst was applied to biodiesel preparation with colza oil and used oil as materials respectively and the technics was optimized by sigle-factor and orthogoral experiments with esterification rate as the index. The optimal technique conditions using colza oil were: the amount of solid catalyst 12%, the mol ratio of methanol to oil 9:1, reaction temperature 65℃, reaction time 3h, under which the esterification rate reached to 94.48%.

4以菜籽油和煎炸废油为原料,利用固体碱催化剂催化制备生物柴油,以转化率为考察指标,采用单因素和正交试验对工艺进行优化,得到以菜籽油为原料时制备的最佳工艺参数为固体催化剂投入量2.5%,醇油摩尔比9∶1,反应温度65℃,反应时间3h,转化率达到93.9%;以煎炸废油为原料时最佳工艺参数为反应温度65℃,反应时间3h,固体催化剂投入量4%,醇油摩尔比6∶1,转化率达到91.2%。

The byproducts using a HZSM-5 supported multi-metal catalyst are polymer of MXDA condensation detected by MS, which is different from the byproducts using the carbon supported metal catalyst.

反应副产物用MS定性分析表明:分子筛负载的多金属加氢催化剂与活性炭负载的多金属催化剂不同。分子筛负载的多金属加氢催化剂产生的副反应主要为MXDA的分子间脱氨缩合反应。

With the ceaselessly improvement of catalyst properties, the production process of catalyst became more and more intricacy that requires even more strict process controlment on production process and even higher quality management on process.

聚丙烯高效催化剂是丙烯聚合工业的技术核心,催化剂产品质量直接影响着聚丙烯产品的质量及新产品的开发。

Ltd. The results show that in contrast to phosphoric acid catalyst, the production of cumene on zeolite catalyst exhibits low operating cost, high product yields, high product purity and little corrosion.

结果表明,采用沸石分子筛催化剂生产异丙苯,与固体磷酸催化剂相比,具有收率高、产品质量好、操作费用低、无腐蚀等优点。

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