首页> 外文期刊>Journal of natural gas science and engineering >Simultaneous production of methanol, DME and hydrogen in a thermally double coupled reactor with different endothermic reactions: Application of cyclohexane, methylcyclohexane and decalin dehydrogenation reactions
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Simultaneous production of methanol, DME and hydrogen in a thermally double coupled reactor with different endothermic reactions: Application of cyclohexane, methylcyclohexane and decalin dehydrogenation reactions

机译:在具有不同吸热反应的热双偶合反应器中同时生产甲醇,DME和氢气:环己烷,甲基环己烷和十氢化萘脱氢反应的应用

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Three different units of a multi-tubular reactor with 2962 three concentric tubes have been investigated as a thermally double coupled reactor (TDCR) in co-current mode. Exothermic reactions are same for all three units and are occurred in the inner (methanol synthesis) and outer tubes (direct DME synthesis from syngas) while endothermic reaction is different for each unit. Three endothermic dehydrogenation reactions of cyclohexane (CH), methylcyclohexane (MCH) and decalin (DC) have been considered for middle tube side of each unit. A steady-state heterogeneous catalytic reaction model is applied to evaluate the performance of TDCR for simultaneous production of methanol, hydrogen and dimethy-lether (DME) in one reactor. The simulation results of each unit are compared with others that operated at the same feed conditions. Results show that conversion of CH, MCH and DC reaches to 67%, 56% and 77% at the output of each unit respectively. Output methanol yield with application of CH and MCH dehydrogenation as endothermic reactions are same equal to 0.37. Also, methanol yield for DC unit is 0.33. In addition, conversion of monoxide at the output of DME synthesis side reaches to 64%, 65% and 62% for CH, MCH and DC units, respectively.
机译:具有并流模式的热双偶合反应堆(TDCR)已研究了具有2962个三个同心管的多管反应器的三个不同单元。这三个单元的放热反应相同,发生在内部(甲醇合成)和外部管(由合成气直接合成DME)中,而每个单元的吸热反应不同。对于每个单元的中管侧,已经考虑了环己烷(CH),甲基环己烷(MCH)和十氢化萘(DC)的三个吸热脱氢反应。应用稳态多相催化反应模型评估TDCR在一个反应​​器中同时生产甲醇,氢和二甲基醚(DME)的性能。将每个单元的仿真结果与在相同进料条件下运行的其他单元的仿真结果进行比较。结果表明,CH,MCH和DC的转化率在每个单元的输出处分别达到67%,56%和77%。在吸热反应中应用CH和MCH脱氢后的甲醇输出量等于0.37。另外,DC单元的甲醇产率为0.33。另外,对于CH,MCH和DC单元,在DME合成侧的输出处的一氧化碳转化率分别达到64%,65%和62%。

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