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Synthesis of cyclopentadiene trimer (tricyclopentadiene) over various zeolites: A feasibility study for scale-up reactions and comparative economic analysis between two-step and one-pot processes using an engineering estimation

机译:在多种沸石上合成环戊二烯三聚体(三环戊二烯):规模化反应的可行性研究以及使用工程估算的两步法和一锅法之间的比较经济分析

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摘要

Several researchers have continuously studied the development of HEDFs using tricyclopentadiene (TCPD) as a raw material. However, the production of high-energy-density fuels (HEDFs) using the TCPD raw material has been performed mainly in a laboratory-scale process, and there is no clear standard to judge the value of commercialization. Therefore, in this study, the scale-up effects were investigated for four reaction cases (1. cycloaddition of endo-dicyclopentadiene (DCPD) over Al-MCM-41; 2. isomerization of endo-tetra-hydrotricyclopentadiene (THTCPD) over HY(30); 3. one-pot DCPD oligomerization and TCPD isomerization over MMZ-H beta(300); 4. one-pot DCPD oligomerization and TCPD isomerization over H beta(25)) for manufacturing highly valuable TCPD. These four cases were analyzed and compared with the results of corresponding laboratory-scale tests for checking the reproducibility of each reaction to some degree. Additionally, the measurement and analysis of the important major physical properties of the final products from each reaction case were carried out according to ASTM (American Society for Testing and Materials) methods such as specific gravity, heat of combustion, viscosity and freezing point. Finally, the comparative economic analysis was performed between two-step process of the separate oligomerization/isomerization and one-pot oligomerization/ isomerization considering the regeneration of catalysts through the estimation of the unit manufacturing cost for each pilot scale production using an engineering estimate method based on the reaction conditions for the scale-up test results. As a result, the two-step process has a strong point in the relatively higher TCPD yield despite the disadvantage of the relatively longer process step.
机译:一些研究人员一直在研究以三环戊二烯(TCPD)为原料的HEDF的开发。但是,使用TCPD原料生产高能量密度燃料(HEDF)主要是在实验室规模的过程中进行的,尚无明确的标准来判断商业化的价值。因此,在本研究中,研究了四个反应案例的放大效应(1. Al-MCM-41上内环二环戊二烯(DCPD)的环加成; 2。HY上内环四氢三环戊二烯(THTCPD)的异构化( 30); 3。在MMZ-H beta(300)上进行一锅法DCPD异构化和TCPD异构化; 4。在H beta(25)上进行一锅法DCPD寡聚化和TCPD异构化),以生产高价值的TCPD。分析了这四种情况,并与相应的实验室规模测试的结果进行了比较,以在某种程度上检查每个反应的可重复性。另外,根据ASTM(美国测试和材料学会)的方法,如比重,燃烧热,粘度和凝固点,对每种反应情况下最终产物的重要主要物理性能进行测量和分析。最后,在考虑到催化剂再生的两步分离低聚/异构化和一锅低聚/异构化过程之间进行比较经济分析,方法是使用工程估算方法,通过估算每个中试规模生产的单位制造成本在反应条件下获得放大测试结果。结果,尽管存在相对较长的处理步骤的缺点,但是两步处理的优点在于相对较高的TCPD产量。

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