Using CAPE to Enhance the Sustainability of Utilizing Natural Gas in Ammonia Production

被引：0

作者：

Lewis, L. ^{[1
]}

John, E. ^{[1
]}

Albert, A. ^{[1
]}

Koongebeharry, C. ^{[1
]}

Kissoon, A. ^{[2
]}

Aufderheide, B. ^{[1
]}

机构：

[1] Univ Trinidad & Tobago, Proc Engn Programme, Point Lisas Campus, Brechin Castle, Couva, Trinidad Tobago

[2] Point Lisas Nitrogen Ltd, Couva, Trinidad Tobago

来源：

22 EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2012年 / 30卷

关键词：

ammonia synthesis conversion; reactor modeling; catalyst degradation; CATALYST; BARIUM;

D O I：

暂无

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

An industrial ammonia converter containing one packed bed of magnetite catalyst and three beds of ruthenium catalyst and auto-thermally regulated was successfully modeled using 4 years of plant data. Over time, kinetic degradation was demonstrated, and by refitting the exponential factor for ruthenium catalyst, predictions were accurate again. The complete model for the ammonia converter predicted inlet bed temperatures within +/- 4.9% accuracy and final ammonia concentrations within +/- 10.3% accuracy.

引用

下载

页码：1167 / 1171

页数：5

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