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Catalytic activities of Fe2O3 and chromium doped Fe2O3 for sulfuric acid decomposition reaction in an integrated boiler, preheater, and catalytic decomposer

Paper ID Volume ID Publish Year Pages File Format Full-Text
46260 46436 2012 11 PDF Available
Title
Catalytic activities of Fe2O3 and chromium doped Fe2O3 for sulfuric acid decomposition reaction in an integrated boiler, preheater, and catalytic decomposer
Abstract

In our earlier work (Banerjee et al. [29]) we have reported the catalytic properties of powders of Fe2(1−x)Cr2xO3 (x = 0.0, 0.1, 0.2) for sulfuric acid decomposition in a flow through quartz catalytic reactor with 2 g catalyst in presence of nitrogen as a carrier gas. With a practical application approach, in this work the two screened oxides, iron oxide and 10% chromium doped iron oxide, that showed good initial promise as catalyst for sulfuric acid decomposition were prepared in granular form and evaluated for sulfuric acid decomposition reaction using an indigenously developed dual tube quartz reactor which served as an integrated acid boiler, pre-heater, and decomposer. The effect of reaction variables, e.g., temperature, time, and acid flow rate on the catalytic activity was evaluated in detail employing 20 g of granular catalyst and 98 wt% H2SO4 (without any carrier/diluents gas). Temperature dependent catalytic activity results revealed that at lower temperatures (<775 °C) the Cr-doped sample showed much higher activity while at higher temperatures (∼825 °C) the conversions levels were found to be similar on both the samples. No decrease in catalytic activity was observed for either catalysts during a 100 h catalytic run at 800 °C and at an acid flux of ∼0.63 ml min−1, but the chromium doped sample exhibited slightly higher activity over the entire time period. Both the catalyst exhibited a loss in catalytic activity when subjected to higher flow rates of sulfuric acid in the range 2–10 ml min−1. The catalytic activities were correlated with the structure, morphology, redox, and thermal properties of the oxides by proper characterization of the fresh and the spent catalysts by XRD, FTIR, XPS, TPR, evolved gas analysis, and SEM. From the ex situ analysis of the spent catalyst samples the most probable mechanism of the high temperature sulfuric acid decomposition reaction was also proposed, which involves metal sulfate formation and decomposition steps. The enhanced catalytic activity of Cr-doped Fe2O3 was ascribed to lower thermal stability of its sulfate and better redox properties.

Graphical abstractFigure optionsDownload full-size imageDownload as PowerPoint slideHighlights► Performance of Fe2O3/Fe1.8Cr0.2O3 granules for H2SO4 decomposition step in SI cycle. ► New design of integrated high temperature quartz catalytic reactor. ► Sustainability of activity over 20 g catalyst for 100 h at 800 °C, flux 0.63 ml min−1. ► Characterization of fresh/spent catalyst to study stability/most probable mechanism. ► Cr substitution induced facile sulfate decomposition and superior redox properties.

Keywords
Hydrogen production; Sulfuric acid decomposition; Iron oxide; Chromium doped iron oxide; Granular catalyst; Redox
First Page Preview
Catalytic activities of Fe2O3 and chromium doped Fe2O3 for sulfuric acid decomposition reaction in an integrated boiler, preheater, and catalytic decomposer
Publisher
Database: Elsevier - ScienceDirect
Journal: Applied Catalysis B: Environmental - Volume 127, 30 October 2012, Pages 36–46
Authors
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Subjects
Physical Sciences and Engineering Chemical Engineering Catalysis