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以异佛尔酮为原料,经氰化、亚胺化和氢化三步反应合成了异佛尔酮二胺,并对反应工艺条件进行了优化。中间产物异佛尔酮腈合成的优化实验条件:NH4Cl为酸化试剂、DMF为反应介质、0.0669 mol异佛尔酮和0.048 mol Na CN与5 m L浓度为6 mol·L-1的NH4Cl水溶液在70℃下反应4 h,得异佛尔酮腈,收率为94.9%。中间产物异佛尔酮亚胺合成的优化实验条件为:以Ca O为催化剂、氨压0.2 MPa、70℃反应4 h,异佛尔酮腈转化率为97.4%,异佛尔酮亚胺收率为87.6%。异佛尔酮二胺合成的优化实验条件为:温度120℃、氢压6 MPa、氨压0.2 MPa、催化剂为2.0 g Raney Co,反应8 h后,异佛尔酮亚胺的转化率为100%,异佛尔酮二胺的收率为95.6%。另外,对中间产物和终产物分别进行了IR、MS、1H-NMR等分析,确认其结构无误。 相似文献
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乙酸甲酯催化精馏水解工艺研究 总被引:10,自引:0,他引:10
采用阳离子交换树脂为催化剂 ,研究了乙酸甲酯催化精馏水解工艺。反应区充填离子交换树脂催化剂捆束包 ,提馏段充填Mo Ti金属板波纹丝网填料。在小试、中试 (塔径为 2 0 0mm)和工业化 (塔径为1 0 0 0mm)实验中 ,系统地研究了水酯摩尔比、回流进料比和空速对酯分解率和分解液中酸水质量比的影响 ,获得不改变现有聚乙烯醇生产中乙酸甲酯分解回收工艺流程的最佳分解率为 50 %— 60 % ,由此导致比原工艺节能约 30 %和原有设备利用率成倍提高 相似文献
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采用离子交换法和浸渍法向NaX分子筛引入Cs进行改性,分别记做CsX-IE和CsX-IMP。采用SEM、XRD、FT-IR、BET、TG和CO2-TPD等分析手段对催化剂进行表征,并在固定床微反应器装置上,对改性后的分子筛催化丙酮缩合制备异佛尔酮反应进行了催化性能评价。研究表明:2种制备方法得到的改性后分子筛催化剂均具有完整的晶体结构、较大的比表面积、适当的碱性位和良好的热稳定性,催化活性比较高。同时得到适宜的工艺条件:反应温度350℃,液时空速2.0 h-1,在此工艺条件下,丙酮的转化率为26.05%,异佛尔酮的选择性为52.27%。 相似文献
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采用等体积浸渍法制备出蛋壳型Pd/Al2O3催化剂,采用连续加氢固定床微反装置研究了异佛尔酮(IP)的选择性加氢反应,考察了载体焙烧温度、蛋壳层厚度、Pd负载量及粒子大小、溶剂等反应条件对Pd/Al2O3催化剂上IP选择性加氢的影响.结果表明,蛋壳型Pd/Al2O3是IP选择性加氢制备3,3,5-三甲基环己酮(TMCH)的优异催化剂,反应条件缓和,IP转化率及TMCH选择性均可达到99.5%以上,具有良好的工业应用前景. 相似文献
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Three Li3PO4 catalysts with hollow structure were prepared: N-Li3PO4 (Na3PO4 added to Li3PO4), L-Li3PO4 (LiOH added to Na3PO4), and S-Li3PO4 (LiOH and Na3PO4 added simultaneously). As a catalyst for propylene oxide isomerization, L-Li3PO4 exhibits the highest conversion and selectivity among the three samples. And the change of Li during the isomerization reaction was discussed. There are two Li ions in the crystal lattice (Li1s1 and Li1s2) based on the X-ray photoelectron spectroscopy (XPS) spectra. After catalytic reaction, the ratio of the surface atomic Li1s1/Li1s2 concentration changes from 1:1 to 1.32:1, indicating the motion and shift of Li ions. 相似文献
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A kinetic study on isophorone synthesis via self‐condensation of supercritical acetone catalyzed by aqueous KOH in a tubular flow reactor was conducted. The intention was to improve the isophorone selectivity, with the main approach to reduce the by‐products higher‐boiling than isophorone. A higher isophorone selectivity was obtained with increased reaction temperature. The structures of main products were determined by gas chromatography‐mass spectrometry and nuclear magnetic resonance analysis. The key reaction pathways and a corresponding kinetic model were proposed. The fitted apparent activation energies indicated the reason of isophorone selectivity improvement in that high temperature favors reversion of reversible by‐products. 相似文献