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WGS reaction empirical kinetics over novel potassium promoted ZnAlLa mixed oxides catalyst
•Experimental investigation of water–gas shift reaction over K-ZnAlLa catalyst under realistic process conditions.•WGS rate data collected at diffusion regime using gradientless reactor.•Power-law type rate equation developed for temperature 300–400°C and pressure ca. 2.5MPa. A new empirical kinetic...
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Published in: | Chemical engineering research & design 2020-12, Vol.164, p.293-298 |
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Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | •Experimental investigation of water–gas shift reaction over K-ZnAlLa catalyst under realistic process conditions.•WGS rate data collected at diffusion regime using gradientless reactor.•Power-law type rate equation developed for temperature 300–400°C and pressure ca. 2.5MPa.
A new empirical kinetics of novel catalyst for high temperature water–gas shift (HT-WGS) at the pressure of 2.5MPa was developed in the study. Using gradientless reactor a set of kinetics data for catalyst in form of 5×5mm tablet operating at diffusion regime was collected, studied and fitted to classic power-law kinetic equation. Simple power-law equation fits the experimental data with sufficient accuracy. The reaction with respect to CO is close to first order and the apparent activation energy of ca. 51.5kJmol−1. The equation is believed to be applicable to modeling of HT-WGS at the temperature in the range of 300–400°C and the pressure ca. 2.5MPa corresponding to synthesis gas production for ammonia and methanol plants. |
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ISSN: | 0263-8762 1744-3563 |
DOI: | 10.1016/j.cherd.2020.09.031 |