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hydrogenation相关的网络例句

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与 hydrogenation 相关的网络例句 [注:此内容来源于网络,仅供参考]

The Circulation-hydrogenation Compressor Model BLC-305/A is an important equipment with Hydrogenation devices, which is imported by Lanzhou Petrochemical Company Refinery. Due to high-speed rolling periodically, the spare parts of this compressor, to a varying extent, show a lot of signs of wear and tear. Especially, the axle sleeve of the rotor axle of the compressor is so worn to the greatest degree that its work efficiency decreases by a big margin. Machinery Factory of Lanzhou Petroleum Processing and Chemical Complex has undertaken this task to repair the rotor.

BCL—305/A型循环加氢压缩机是兰州石化炼油厂从国外引进的一台用于加氢装置的重要设备,该设备经长周期的高速运转,零部件均有不同程度的磨损,特别是压缩机转子轴上的轴套磨损程度最大,使整机效率大幅度下降,兰炼机械厂承担了这项转子修复任务。

The degree of hydrogenation of methyl benzoate might be controled by adding the promoters and changing the nano-size of ZnO. For hydrogenation of methyl benzoate to benzaldehyde, the active-structure of a catalyst should be modified to decrease the absorption of benzaldehyde on the surface of it, because benzaldehyde absorbed is hydrogenated easily. Using 30-40%ZnO/γ-Al〓O〓 or Li-30%ZnO/γ-Al〓O〓, a higher selectivity to benzaldehyde is obtained. Hydrogenolysis of methyl benzoate to toluene or benzene is carried out effectively using a catalyst modified. For instance, 45.3% selectivity to benzene and 100% conversion of methyl benzoate at 420℃ was obtained over 10%ZnO/MCM-41 with the nano-size particles of ZnO (2.4nm).

也可以通过助催化剂的添加和活性组分的纳米化,并根据苯甲酸甲酯多步加氢反应的特点实行加氢深度的调控:苯甲酸甲酯选择性加氢制苯甲醛中,由于苯甲醛容易进一步加氢,需要对活性结构进行调变,以减弱苯甲醛的吸附,使用30-40%ZnO/γ-Al〓O〓催化剂或Li调变的Li-30%ZnO/γ-Al〓O〓催化剂,可获得较高的苯甲酸甲酯加氢制苯甲醛的活性;采用同样的方式,苯甲酸甲酯选择性氢解为甲苯或苯也获得了较好的结果,如使用ZnO纳米化的10%ZnO/MCM-41催化剂,在420℃,可获得45.3%的苯选择性,苯甲酸甲酯完全转化。

At first, the rought C〓F〓 mixed gases are obtained by pyrolysis process of R22. A experimental pyrolysis device is designed and made by ourself. The optimum operating conditions are offered in the paper. Secondly, the much efforts is on the synthesis of R134. After through the discussion of basic thermodynamics and kinetics, selecting and preparating catalyst, it is possible that the synthesis of R134 by pyrolyzed gases hydrogenation. Base on the character of catalytic process, the kinetics equation about C〓F〓 catalytic hydrogenation is established. The rate constant of the reaction is obtained through experiment data regression. In order to achieve higher yield of R134, some optimum technological conditions is determined.

论文首先对R22裂解制成四氟乙烯混合原料气的裂解过程进行了讨论,自行设计和制作裂解反应装置,并确定裂解反应的最佳操作条件;然后,重点对R134的合成进行基础研究,分别从热力学和动力学的角度探讨以含四氟乙烯的R22裂解混合气为原料合成R134这一全新工艺的可能性,选择和制备加氢催化剂,根据催化过程特点建立四氟乙烯催化加氢反应的总包动力学方程,并在此基础上自行设计和制作中试合成装置,获得了以裂解混合气为原料合成R134的最佳工艺条件,为R134的工业化生产提供了必要的理论依据和实验基础。

A novel Ziegler-Natta type catalyst for the hydrogenation reaction of isooctene to isooctane was developed by investigated the effect of the solvent and the ratio of aluminium/nickel on the conversion,and the influence of process conditions on the hydrogenation reaction by Ziegler-Natta type catalyst was also studied.

探讨了在Ziegler-Natta型均相催化剂上进行异辛烯加氢反应时,催化剂中的溶剂和铝/镍质量比对反应转化率的影响,得到了优化的Ziegler-Natta型均相催化剂,并考察了工艺条件对异辛烯加氢反应的影响。

A novel Pd/C catalyst with high activity,high selectivity and good stability developed by our group was used for the hydrogenation of N-(3-nitro-4-methoxyphenyl)acetamide into N-(3-amino-4-methoxyphenyl)acetamide in methanol and water,respectively.

笔者开发了一种高效的Pd/C催化剂,分别选用甲醇和水作为反应溶剂,实现了高活性、高选择性和高稳定性地催化加氢制备N-(3-氨基-4-甲氧基苯基)乙酰胺。

Influence of active components in the catalyst and acetonitrile hydrogenation condition on behaviors of the catalyst and stability of the catalyst were investigated.

研究了催化剂活性组分和乙腈催化加氢工艺条件对催化剂性能的影响,并考察了该催化剂的稳定性。

A gas chromatographic analysis method was established in the study of the conversion of acrolein to 1,3-propanediol by hydration and hydrogenation.

建立丙烯醛水合加氢制1,3-丙二醇的气相色谱定性定量分析方法。

The possibilities of chemical reprocessing (hydrogenation, hydrolysis, alcoholysis, glycolysis, and pyrolysis) are still in the development phase, so that they cannot yet be economically applied on a large scale.

化学加工(加氢、水解、糊、糖酵解,热解)的可能性仍然在开发阶段,所以在经济上它们仍然不能被大规模的应用。

During the reaction of alkylation, general contained 0.2%~2.0% butadiene will produce viscous heavy composite materials, which will raise final boiling point of alkylate and decrease octane, what is more, it will react with acid to produce corresponding ester, which will increase the consumption of acid, Therefore, we must remove butadiene by selective hydrogenation, at the same time, it will convert some of 1- butane to 2- butane by isomerization and raise octane of alkylate.

一般含有0.2%~2.0%的丁二烯,其在烷基化反应中,可生成一种分子量很高的粘稠重质迭合物,使烷基化油的干点升高,辛烷值降低,并且它还和酸反应生成相应的酯而加大酸耗量。因此必须经过选择性加氢除掉丁二烯,同时,将部分1-丁烯异构化为2-丁烯,以提高烷基化油的辛烷值。

After hydrogenation of the double bond and the addition of alkyne to a carbonyl we introduced the N-hydroxy group by SN2 reaction.

不对称氢化和炔负离子对羰基的立体选择性加成构建了两个新的手性中心,之后用羟胺衍生物对羟基的SN2取代反应引入了羟胺片断。

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