Publiora

Menghubungkan ke Publiora...

Publiora

System Identification for Experimental Study for Polymerization Catalyst Reaction in Fluidized Bed

Ibrehem, Ahmmed S.
Bulletin of Chemical Reaction Engineering & Catalysis (Sinta 1)Vol. 0 No. 020 Desember 2011
DOI10.9767/bcrec.6.2.874.137-146

Abstrak

In this work, system identification method is used to capture the reactor characteristics of production rate of polyethylene (PE) based on published experimental data. The identification method is used to measure the percentage effect on the production rate of PE by measuring the effect of input factors of temperature of reaction, hydrogen concentration, and [Al]/[Ti] molar catalyst ratio. Temperature of reaction has big effects equal 52.4 % on the output of the system and 47.6 % on interaction of the system's parameters compare to other two factors. Also, hydrogen concentration has big effect equal 45.66 % on the output of the system and 14.7 % on interaction of the system's parameters. [Al]/[Ti] molar catalyst ratio has big effect on interaction of the system equal 28.6 and 1.94 % on the output of the system but less than the reaction temperature and hydrogen concentration. All these results depend on experiment results and these results are very important in industrial plants. © 2011 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0)

Kata Kunci

Catalystsco catalystsystem identificationtemperature of reactionconcentration of hydrogen

Cari jurnal yang tepat untuk naskah Anda

MatchMind AI mencocokkan abstrak naskah Anda dengan ribuan jurnal terakreditasi dan menampilkan rekomendasi terbaik beserta alasannya.

Coba MatchMind

Lihat profil lengkap jurnal ini

Waktu review, biaya APC, statistik sitasi, indeksasi Scopus, dan banyak lagi.

Buka Bulletin of Chemical Reaction Engineering & Catalysis

Artikel ini juga tersedia di situs resmi jurnal.

System Identification for Experimental Study for Polymerization Catalyst Reaction in Fluidized Bed | Bulletin of Chemical Reaction Engineering & Catalysis | Publiora