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Promoted zinc chromite catalyst for higher alcohol synthesis in a slurry reactor.

机译:用于淤浆反应器中高级醇合成的促进型亚铬酸锌催化剂。

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The motivation for this research was the desire to synthesize higher (C2–C4) alcohols in a slurry reactor from a mixture of carbon monoxide (CO) and hydrogen (H2), so called “synthesis gas”.; Unpromoted “zinc chromite” catalyst and the same catalyst promoted with 6 wt% cesium (Cs) were evaluated in a continuous slurry reactor with decahydronaphthalene (DHN) and tetrahydroquinoline (THQ) as slurry liquids. The conditions were: Temperature—375°C and 400°C; Pressure—13.6 MPa (2000 psig); Gas Hourly Space Velocity (GHSV)—5000 standard liters/kg(cat)-hr; and H2/CO feed ratio—0.5,1.0 and 2.0 mole/mole. The experiments lasted for 8–12 days of continuous operation. In, DHN, upon adding Cs, promoted catalyst obtained greater higher alcohol (HA) selectivity. However, this catalyst showed more sensitive to the change of operating conditions than the unpromoted one. Liquid medium affected catalyst activity and selectivity by the competitive adsorption and interaction(s) between liquid and adsorbed species on the catalyst surface. The selectivity of HA and DME, and CO conversion observed in THQ appeared to be lower compared with DHN. Methane selectivity was higher when using THQ as slurry liquid.; In contrast to DHN, THQ was extensively alkyalted to methyl THQs during the experiment. The alkylation rate was faster with unpromoted catalyst than with the Cs-promoted catalyst. A variety of analyses were carried out to identify the major components of the “spent” THQ. Silica gel liquid chromatography and HPLC (high performance liquid chromatography) were used to fractionate the “spent” THQ, while GC/MS (gas chromatography/mass spectroscopy), FTIR (Fourier transform infrared) spectroscopy and NMR (nuclear magnetic resonance) were applied to identify the major compounds. Methyl-, dimethyl-, and trimethyl-THQ comprised more than 80% of the “spent” liquid. The balance was various methylated indoles. A methyl group always was attached to the N atom in the ring structure. To explain the liquid medium effect on apparent catalyst activity and selectivity, mechanisms have been proposed.
机译:这项研究的动机是希望在淤浆反应器中由一氧化碳(CO)和氢(H)的混合物合成高级(C 2 –C 4 )醇 2 ),即所谓的“合成气”。在十氢萘(DHN)和四氢喹啉(THQ)作为浆液的连续浆液反应器中,评估了未助催化剂的“亚铬酸锌”催化剂和用6 wt%铯(Cs)助催化剂相同的催化剂。条件为:温度-375°C和400°C;压力-13.6 MPa(2000 psig);气时空速(GHSV)-5000标准升/ kg(cat)-hr; H 2 / CO的进料比为0.5、1.0和2.0摩尔/摩尔。实验持续了8-12天的连续操作。在DHN中,添加Cs后,促进的催化剂获得更高的更高的醇(HA)选择性。但是,这种催化剂对操作条件的变化比未助催化剂更敏感。液体介质通过催化剂表面上液体和被吸附物质之间的竞争性吸附和相互作用而影响催化剂的活性和选择性。与DHN相比,THQ中观察到的HA和DME的选择性以及CO转化率较低。当使用THQ作为浆液时,甲烷的选择性更高。与DHN相比,THQ在实验过程中广泛烷基化为甲基THQ。未促进的催化剂的烷基化速率比Cs促进的催化剂快。进行了各种分析,以确定“用过的” THQ的主要组成部分。使用硅胶液相色谱法和HPLC(高效液相色谱法)对“用过的” THQ进行分馏,同时应用GC / MS(气相色谱/质谱),FTIR(傅立叶变换红外)光谱和NMR(核磁共振)识别主要化合物。甲基,二甲基和三甲基THQ占“用过的”液体的80%以上。剩余的是各种甲基化的吲哚。甲基总是连接在环结构的N原子上。为了解释液体介质对表观催化剂活性和选择性的影响,提出了机理。

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