Tianjin Key Laboratory of Applied Catalysis Science and Technology, School of Chemical Engineering and Technology Institution, Tianjin University, Tianjin 300072, PR China.
ChemSusChem. 2010 Oct 25;3(10):1192-9. doi: 10.1002/cssc.201000109.
Ethanol was directly synthesized from dimethyl ether (DME) and syngas with the combined H-Mordenite and Cu/ZnO catalysts that were separately loaded in a dual-catalyst bed reactor. Methyl acetate (MA) was formed by DME carbonylation over the H-Mordenite catalyst. Thereafter, ethanol and methanol were produced by MA hydrogenation over the Cu/ZnO catalyst. With the reactant gas containing 1.0% DME, the optimized temperature for the reaction was at 493 K to reach 100% conversion. In the products, the yield of methanol and ethanol could reach 46.3% and 42.2%, respectively, with a small amount of MA, ethyl acetate, and CO(2). This process is environmentally friendly as the main byproduct methanol can be recycled to DME by a dehydration reaction. In contrast, for the physically mixed catalysts, the low conversion of DME and high selectivity of methanol were observed.
乙醇可直接由二甲醚(DME)和合成气在双催化剂床反应器中负载的 H-丝光沸石和 Cu/ZnO 催化剂共同合成。H-丝光沸石催化剂上 DME 羰基化生成乙酸甲酯(MA)。然后,MA 在 Cu/ZnO 催化剂上加氢生成乙醇和甲醇。在含有 1.0% DME 的反应物气体中,反应的最佳温度在 493 K 以达到 100%转化率。在产物中,甲醇和乙醇的收率分别可达 46.3%和 42.2%,同时生成少量的 MA、乙酸乙酯和 CO(2)。由于主要副产物甲醇可以通过脱水反应循环回 DME,因此该工艺具有环保性。相比之下,对于物理混合的催化剂,观察到 DME 转化率低和甲醇选择性高的现象。