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Cobalt promoted Mo/beta zeolite for selective hydrocracking of tetralin and pyrolysis fuel oil into monocyclic aromatic hydrocarbons

机译:钴促进的Mo /β沸石用于将四氢萘和热解燃料油选择性加氢裂化为单环芳烃

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The Mo/beta (beta zeolite) catalyst was prepared by wet-impregnation and modified with cobalt promoter. The catalytic activity of monometallic Mo/beta catalyst in selective hydrocracking of tetralin into monocyclic aromatic hydrocarbons (MAH) such as benzene, toluene and xylene (BTX) was investigated in fixed bed reactor and compared its activity with bimetallic CoMo/beta catalyst. The catalytic results indicates that, incorporation of promoter (Co) not only improved their catalytic activity in hydrocracking reactions but also showed long term stability as compared with Mo/beta. Effect of different SiO2/Al2O3 ratio (25, 75,150) in beta zeolite was investigated on catalytic activity of CoMo/beta. CoMo/beta with SiO2/Al2O3 of 25, gave highest 62.6% of desired MAH yield at 99.5% conversion of tetralin for more than 140 h of reaction time. Likely, CoMo/beta catalyst was also found to be effective for the conversion of pyrolysis fuel oil (PFO) into MAH. Crude PFO was distilled out at 170 degrees C and total amount of 55 wt.% PFO was received after distillation. In the PFO hydrocracking, it produced 43.3% of MAH product yield at 70% conversion of PFO, which is significantly higher than the conversion (48%) and MAH yield (34.2%) obtained from monometallic Mo/beta catalysts. CoMo/beta catalyst was found to be more stable as well as active for longer reaction time (140 h). (C) 2015 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
机译:通过湿法浸渍制备Mo /β(β沸石)催化剂,并用钴助催化剂改性。在固定床反应器中研究了单金属Mo /β催化剂在四氢化萘选择性加氢裂化成苯,甲苯和二甲苯(BTX)等单环芳烃(MAH)中的催化活性,并将其与双金属CoMo /β催化剂进行了比较。催化结果表明,掺入促进剂(Co)不仅提高了其在加氢裂化反应中的催化活性,而且与Mo /β相比显示出长期稳定性。研究了不同的SiO2 / Al2O3比(25、75,150)在β沸石中对CoMo /β催化活性的影响。 SiO2 / Al2O3为25的CoMo / beta在超过140小时的反应时间内,在四氢化萘的转化率为99.5%时,可得到最高的MAH收率的62.6%。可能还发现,CoMo /β催化剂对于将热解燃料油(PFO)转化为MAH也有效。在170℃下蒸馏出粗制的PFO,蒸馏后得到的PFO总量为55重量%。在PFO加氢裂化中,当PFO转化率为70%时,MAH产物的产率为43.3%,明显高于从单金属Mo /β催化剂获得的转化率(48%)和MAH产率(34.2%)。发现CoMo /β催化剂在更长的反应时间(140小时)内更稳定且具有活性。 (C)2015韩国工业和工程化学学会。由Elsevier B.V.发布。保留所有权利。

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