scholarly journals Mechanistic Investigations of Liquid-phase Direct Alkylation of Benzene with n-Heptane Using Proton-exchanged Montmorillonite Catalysts

2020 ◽  
Vol 63 (5) ◽  
pp. 289-296
Author(s):  
Moe TAKABATAKE ◽  
Masayuki NAMBO ◽  
Yuichi MANAKA ◽  
Ken MOTOKURA
Author(s):  
Mohammed C. Al-Kinany ◽  
Saeed M. Alshihri ◽  
Saud A. Aldrees ◽  
Eyad A. Alghilan ◽  
Sami D. Aldrees ◽  
...  

The alkylation of benzene with ethylene or propylene to form ethylbenzene (EB) or cumene is an industrially significant transformation. EB is used as an intermediate in the manufacture of styrene, which in turn is an important in the manufacture of many kinds of polymers. The primary use of cumene is in the co-production of phenol and acetone, which in turn are important in the manufacture of many kinds of chemicals and polymers. In industry, EB and cumene are mainly manufactured by the alkylation of benzene with ethene or propene via two methods, the gas and the liquid phase in the presence of Lewis and Brønsted acids. The development of efficient solid catalysts has gained much attention over the last decades. The objective of this chapter is to provide an overview of the history of the alkylation of benzene with ethene and propene, the development of homogeneous and heterogeneous Lewis and Brønsted acids and zeiolite catalysts, the liquid and gas phase alkylation processes, and the industrial technologies for EB and cumene production.


2019 ◽  
Vol 0 (0) ◽  
Author(s):  
Emiliya D. Ivanchina ◽  
Elena N. Ivashkina ◽  
Irena O. Dolganova ◽  
Nataliya S. Belinskaya

Abstract This review summarizes Russian developments on the most important industrial processes of hydrocarbon feedstock refining according to the data of the last 15–20 years on the kinetics of deactivation of heterogeneous and liquid-phase catalysts under non-stationary conditions. The methodological aspects of the creation and application of kinetic models for the deactivation of heterogeneous and liquid-phase catalysts under non-stationary conditions are considered. It is shown that high efficiency of catalytic technologies is ensured by regulation of hydrodynamic and thermal conditions of industrial processes of gasoline reforming, alkane dehydrogenation, alkylation of benzene with higher alkenes and catalytic dewaxing using kinetic models, which take into account catalyst deactivation.


ChemInform ◽  
2010 ◽  
Vol 27 (10) ◽  
pp. no-no
Author(s):  
G. BELLUSSI ◽  
G. PAZZUCONI ◽  
C. PEREGO ◽  
G. GIROTTI ◽  
G. TERZONI

Author(s):  
Michal Horňáček ◽  
Pavol Hudec ◽  
Agáta Smiešková ◽  
Tibor Jakubík

Author(s):  
M. L. Pavlov ◽  
R. A. Basimova ◽  
D. A. Shavaleev ◽  
I. N. Pavlova ◽  
O. S. Travkina ◽  
...  

1998 ◽  
Vol 37 (5) ◽  
pp. 1724-1728 ◽  
Author(s):  
C. Ercan ◽  
F. M. Dautzenberg ◽  
C. Y. Yeh ◽  
H. E. Barner

2012 ◽  
Vol 549 ◽  
pp. 283-286 ◽  
Author(s):  
Fei Zhao ◽  
Yu Zhang ◽  
Shu Dong Geng ◽  
Lian Fa Chen ◽  
Wei Wang

MCM-22 “family” zeolites (MCM-22, MCM-49 and MCM-56) have been synthesized hydrothermally by dynamic method. All materials were characterized by different techniques, such as XRD, N2 adsorption-desorption and NH3-TPD. The catalyst performance of MCM-22 “family” zeolites have been studied on the alkylation of benzene with propylene in liquid phase. Result shows that MCM-22 “family” zeolites are excellent alkylation catalysts for the produce of cumene. Compared to MCM-22 and MCM-49, MCM-56 shows higher catalytic activity in a relatively low reaction temperature and higher monoalkylation selectivity in a relatively low benzene-to-propylene ratio.


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