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The higher temperature of polymerization, the higher conversion of methyl methacrylate.

超声波辐照下,MMA单体的转化率随聚合反应温度的提高而增大。

Under the experimental conditions, conversions of methane and carbon dioxide were from 30% to 65% and from 10% to 50%, respectively.

在实验条件下,甲烷和二氧化碳的转化率分别在30%~65%和10%~50%之间。

The conversion of methane is more than 92%, and the selectivity for CO and H〓 is 90% at 700℃.

在常压、700℃的条件下,甲烷的转化率大于92%,H〓和CO的选择性均在90%以上。

The influence of reaction time,temperature,pressure,and molar ratio of methanol to soybean oil were discussed.

讨论了不同的反应时间、温度、压力及摩尔比对大豆油转化率的影响。

In order to elevate the conversion of methyl acetate, the reactive extraction was adopted.

为进一步提高水解平衡转化率,实验结合反应萃取方法对平衡的改善进行了研究。

The purpose of this thesis is to apply the catalytic distillation technique to the hydrolysis of methyl acetate b...

本论文的目的是将催化精馏技术应用于醋酸甲酯水解反应过程,以期突破化学平衡的限制而获得较高的水解转化率

The purpose of this thesis is to apply the catalytic distillation technique to the hydrolysis of methyl acetate by breaking through the limitation of chemical equilibrium for getting high conversion of hydrolysis.

本论文的目的是将催化精馏技术应用于醋酸甲酯水解反应过程,以期突破化学平衡的限制而获得较高的水解转化率

The process has been simulated and optimized, and 99.5 wt% methyl acetate has been obtained in one column with 98% sulfuric acid as catalyst.

以98%浓硫酸作为催化剂,用醋酸和甲醇为原料,用一个塔成功制得纯度≥99.5%的醋酸甲酯,醋酸的转化率>99.9%。

The larger quantity of initiation, the higher conversion of methyl methacrylate.

引发剂用量增加, MMA 单体的转化率增大。

The experiment gains reaction parameters of methylal from formaldehyde and methanol,it also found a mathematical model for continuous production process.

通过实验取得了甲醛和甲醇合成甲缩醛的反应参数;建立了其连续生产工艺的数学模型,利用ASPEN PLUS软件对甲醛和甲醇缩合生成甲缩醛进行了模拟,结果表明反应精馏连续生产甲缩醛的工艺是可行的,转化率高达99%,并得到含甲缩醛99%的产物,同时确定了进料板和反应区。

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