首页> 外文学位 >EFFECT OF CESIUM ON ALCOHOL SYNTHESIS, WATER-GAS SHIFT REACTION, AND ESTER HYDROGENOLYSIS OVER COPPER - ZINC OXIDE CATALYSTS.
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EFFECT OF CESIUM ON ALCOHOL SYNTHESIS, WATER-GAS SHIFT REACTION, AND ESTER HYDROGENOLYSIS OVER COPPER - ZINC OXIDE CATALYSTS.

机译:铯对铜锌氧化物催化剂上醇合成,水煤气变换反应和酯加氢分解的影响。

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This study comprises three subjects: (1) The effects of cesium doping and water concentration in the synthesis gas on methanol synthesis rate and the water-gas shift (WGS) reaction; (2) The hydrogenolysis of alkyl esters; and (3) The effect of cesium on higher alcohol synthesis, as well as the investigation of the chain growth reaction in higher alcohol synthesis over the Cu/ZnO catalysts.; A two-parameter kinetic model quantitatively demonstrated that the maximum rate of methanol synthesis is determined by the balance between the promotional effect of cesium and the retarding effect stemming from the blockage of hydrogen activing sites. Another six-parameter kinetic model, in which the methanol and WGS reactions were considered simultaneously, can account for methanol activity in the water dependence study. At higher water concentrations, the cesium-doped catalysts were more active than the undoped catalyst for methanol synthesis, which was quantitatively shown to be due to the promotion of the WGS reaction by the cesium doping.; The inhibition effect that occurred at high water concentrations in methyl acetate hydrogenolysis is due to the blockage of hydrogen activating sites. In addition, the kinetics of hydrogenolysis of n-propyl acetate resulted in a -0.49 order with respect to n-propyl acetate and a +1.83 order to hydrogen, which are in fair agreement with those derived in terms of Langmuir-Hinshelwood type kinetics. The aldehydic species involved in the hydrogenolysis of esters was evidenced by a isopropylamine trapping experiment.; By injecting the potential precursors of the intermediates into the synthesis gas, it was found that in the higher alcohol synthesis (i) the most pronounced effect of the cesium doping was to promote the reaction step from C(,2) to C(,3); (ii) the limiting step was the conversion of C(,1) alcohol to C(,2) alcohol; (iii) the growth reaction was terminated after forming branched alcohols such as 2-methyl-1-propanol; (iv) the products resulting from (beta) carbon addition ((beta)(,C)), but not the products formed from CO insertion (i(,CO)) and (alpha) oxygen addition ((alpha)(,O)), were significantly promoted by cesium doping; (v) methyl esters and alcohols were formed from the same precursors; and (vi) the formation of methyl esters was constrained by equilibrium at high temperatures. Further, a modified aldol-type condensation mechanism, where adsorbed 1,3 diols are involved as the intermediates, was proposed to account for the cesium effect. The chain growth scheme in higher alcohol synthesis was constructed in terms of C(,1) ((beta)(,C), i(,CO), and (alpha)(,O)), C(,2), and C(,3) additions.
机译:这项研究包括三个主题:(1)铯中的铯掺杂和水浓度对甲醇合成速率和水煤气变换(WGS)反应的影响; (2)烷基酯的氢解; (3)铯对高级醇合成的影响,以及在Cu / ZnO催化剂上高级醇合成中链增长反应的研究。两参数动力学模型定量表明,甲醇合成的最大速率取决于铯的促进作用与氢活化位点的阻断所产生的阻滞作用之间的平衡。同时考虑甲醇和WGS反应的另一个六参数动力学模型可以解释水依赖性研究中的甲醇活性。在较高的水浓度下,铯掺杂的催化剂比未掺杂的催化剂对甲醇合成的活性更高,这定量地证明是由于铯掺杂促进了WGS反应。在乙酸甲酯氢解中高水浓度下发生的抑制作用是由于氢活化位点的阻塞。另外,乙酸正丙酯的氢解动力学导致相对于乙酸正丙酯为-0.49阶,氢为+1.83阶,这与根据Langmuir-Hinshelwood型动力学得出的那些完全一致。酯的氢解反应所涉及的醛类物质是通过异丙胺捕获实验证明的。通过将中间体的潜在前体注入合成气中,发现在高级醇合成(i)中,铯掺杂的最明显作用是促进反应步骤从C(,2)到C(,3 ); (ii)限制步骤是将C(,1)醇转化为C(,2)醇; (iii)在形成支链醇如2-甲基-1-丙醇后终止生长反应; (iv)由β碳加成(β(,C))产生的产物,但不是由CO插入(i(,CO))和α氧加成(α(,O)形成的产物))被铯掺杂显着促进; (v)甲酯和醇是由相同的前体形成的; (vi)在高温下平衡限制了甲酯的形成。此外,提出了一种改性的醛醇缩合机理,其中涉及吸附的1,3二醇作为中间体,以解决铯的影响。根据C(,1)(β(,C),i(,CO)和α((O)),C(,2)和C(,1)构建高级醇合成中的链增长方案C(,3)加法。

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