An integrated criterion of efficiency for Pt catalysts in the dehydrogenation of higher n-paraffins

Detaylı Bibliyografya
Parent link:Catalysis in Industry: Scientific Journal
Vol. 2, iss. 4.— 2010.— [P. 360-367]
Diğer Yazarlar: Romanovskiy R. V. Rostislav Vladimirovich, Frantsina E. V. Evgeniya Vladimirovna, Youriev Е. M., Ivashkina E. N. Elena Nikolaevna, Ivanchina E. D. Emilia Dmitrievna, Kravtsov A. V. Anatoly Vasilyevich
Özet:Title screen
The deactivation of catalysts by coke-forming structures in the dehydrogenation of higher n-paraffins is discussed. The patterns of coke formation on a catalyst subject to process conditions are presented. A mathematical model of the process is described to show its adequacy. A calculation algorithm for the optimum mode of operation of a dehydrogenation catalyst is constructed, and the calculation results are given. Dehydrogenation catalysts of different brands are compared with respect to several parameters (coke formation on catalysts, the yield of the reaction by-product, and the dynamics of temperature rise in the reactor). The model can be used to estimate the efficiencies of catalysts in a cycle and to compare them.
Режим доступа: по договору с организацией-держателем ресурса
Dil:İngilizce
Baskı/Yayın Bilgisi: 2010
Konular:
Online Erişim:http://dx.doi.org/10.1134/S2070050410040100
Materyal Türü: Elektronik Kitap Bölümü
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=655726
Diğer Bilgiler
Özet:Title screen
The deactivation of catalysts by coke-forming structures in the dehydrogenation of higher n-paraffins is discussed. The patterns of coke formation on a catalyst subject to process conditions are presented. A mathematical model of the process is described to show its adequacy. A calculation algorithm for the optimum mode of operation of a dehydrogenation catalyst is constructed, and the calculation results are given. Dehydrogenation catalysts of different brands are compared with respect to several parameters (coke formation on catalysts, the yield of the reaction by-product, and the dynamics of temperature rise in the reactor). The model can be used to estimate the efficiencies of catalysts in a cycle and to compare them.
Режим доступа: по договору с организацией-держателем ресурса
DOI:10.1134/S2070050410040100