کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
51182 | 46834 | 2009 | 4 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Investigation of the effect of total pressure on performance of the catalytic water–gas shift reaction using simulated coal-derived syngases
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
کاتالیزور
پیش نمایش صفحه اول مقاله
![عکس صفحه اول مقاله: Investigation of the effect of total pressure on performance of the catalytic water–gas shift reaction using simulated coal-derived syngases Investigation of the effect of total pressure on performance of the catalytic water–gas shift reaction using simulated coal-derived syngases](/preview/png/51182.png)
چکیده انگلیسی
The effect of operating pressure on the water–gas shift (WGS) reaction rate over an iron-based high-temperature catalyst, and a Co–Mo based sour-shift catalyst, was investigated using simulated coal-derived syngas at 450 °C. For both catalysts, it was found that the CO conversion rate depends linearly upon total operating pressure. The apparent reaction orders used in a power-law rate expression, where the reaction orders were derived from experimental results at atmospheric pressure, are valid at elevated pressures up to at least 11 bar.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Catalysis Communications - Volume 11, Issue 4, 15 December 2009, Pages 272–275
Journal: Catalysis Communications - Volume 11, Issue 4, 15 December 2009, Pages 272–275
نویسندگان
San Shwe Hla, G.J. Duffy, L.D. Morpeth, A. Cousins, D.G. Roberts, J.H. Edwards,