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Effect of Steam Deactivation Severity of ZSM-5 Additives on LPG Olefins Production in the FCC Process

机译:ZSM-5添加剂的蒸汽失活强度对FCC工艺中LPG烯烃生产的影响

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ZSM-5-containing catalytic additives are widely used in oil refineries to boost light olefin production and improve gasoline octanes in the Fluid Catalytic Cracking (FCC) process. Under the hydrothermal conditions present in the FCC regenerator (typically >700 °C and >8% steam), FCC catalysts and additives are subject to deactivation. Zeolites (e.g., Rare Earth USY in the base catalyst and ZSM-5 in Olefins boosting additives) are prone to dealumination and partial structural collapse, thereby losing activity, micropore surface area, and undergoing changes in selectivity. Fresh catalyst and additives are added at appropriate respective levels to the FCC unit on a daily basis to maintain overall targeted steady-state (equilibrated) activity and selectivity. To mimic this process under accelerated laboratory conditions, a commercial P/ZSM-5 additive was hydrothermally equilibrated via a steaming process at two temperatures: 788 °C and 815 °C to simulate moderate and more severe equilibration industrial conditions, respectively. n-Dodecane was used as probe molecule and feed for micro-activity cracking testing at 560 °C to determine the activity and product selectivity of fresh and equilibrated P-doped ZSM-5 additives. The fresh/calcined P/ZSM-5 additive was very active in C12 cracking while steaming limited its activity, i.e., at catalyst-to-feed (C/F) ratio of 1, about 70% and 30% conversion was obtained with the fresh and steamed additives, respectively. A greater activity drop was observed upon increasing the hydrothermal deactivation severity due to gradual decrease of total acidity and microporosity of the additives. However, this change in severity did not result in any selectivity changes for the LPG (liquefied petroleum gas) olefins as the nature (Br?nsted-to-Lewis ratio) of the acid/active sites was not significantly altered upon steaming. Steam deactivation of ZSM-5 had also no significant effect on aromatics formation which was enhanced at higher conversion levels. Coke remained low with both fresh and steam-deactivated P/ZSM-5 additives. View Full-Text
机译:含ZSM-5的催化添加剂广泛用于炼油厂,以提高轻烯烃的产量,并改善流化催化裂化(FCC)工艺中的汽油辛烷值。在FCC再生器中存在的水热条件下(通常> 700°C,蒸汽> 8%),FCC催化剂和添加剂会失活。沸石(例如,碱性催化剂中的稀土USY和烯烃增强添加剂中的ZSM-5)易于脱铝和部分结构塌陷,从而失去活性,微孔表面积并发生选择性变化。每天将新鲜的催化剂和添加剂以适当的相应水平添加到FCC单元中,以保持总体目标稳态(平衡)活性和选择性。为了在加速的实验室条件下模拟此过程,通过蒸汽处理在788°C和815°C这两个温度下对商业P / ZSM-5添加剂进行水热平衡,以分别模拟中等和更严格的平衡工业条件。正十二烷用作探针分子和进料,用于在560°C下进行微活性裂解测试,以确定新鲜和平衡的P掺杂ZSM-5添加剂的活性和产物选择性。新鲜/煅烧的P / ZSM-5添加剂在C12裂解中非常活跃,而蒸汽则限制了它的活性,即,催化剂进料(C / F)为1时,转化率约为70%和30%。新鲜和蒸熟的添加剂分别。由于添加剂的总酸度和微孔度的逐渐降低,在增加水热失活严重性时观察到更大的活性下降。但是,这种严重性的变化不会对LPG(液化石油气)烯烃产生任何选择性变化,因为在蒸煮过程中,酸/活性位点的性质(布朗斯台德-刘易斯比)并没有显着改变。 ZSM-5的蒸汽失活对芳烃的形成也没有显着影响,芳烃的形成在较高转化率下得到增强。新鲜和蒸汽灭活的P / ZSM-5添加剂的焦炭含量均保持在较低水平。查看全文

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