scholarly journals SYNTHESIS AND STUDY OF CATALYSTS FOR LIQUID-PHASE ALKYLATION OF BENZENE WITH ETHYLENE ON THE BASIS OF THE BINDER-FREE ZEOLITE Y

Author(s):  
M. L. Pavlov ◽  
R. A. Basimova ◽  
D. A. Shavaleev ◽  
I. N. Pavlova ◽  
O. S. Travkina ◽  
...  
2010 ◽  
Vol 64 (4) ◽  
Author(s):  
Michal Horňáček ◽  
Pavol Hudec ◽  
Andrej Nociar ◽  
Agáta Smiešková ◽  
Tibor Jakubík

AbstractHY-zeolite and its deep-bed dealuminated and EFAL-extracted forms were tested in liquid phase alkylation of benzene with 1-hexadecene in a batch reactor at 120°C. Deep-bed dealumination of the HY-sample at 560 °C followed by careful selective extraction of extra-framework aluminium by hydrochloric acid increased the catalytic activity as well as oxidative regenerability of Y-zeolite.


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):  
Kh. M. Minachev ◽  
E. S. Mortikov ◽  
A. S. Leont'ev ◽  
A. A. Masloboev-Shvedov ◽  
N. F. Kononov

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

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