Item – Theses Canada

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OCLC number
56751872
Link(s) to full text
LAC copy
LAC copy
Author
Wang, Hui,1959-
Title
A study of the gas-liquid reaction system of hydrogen sulfide and sulfuric acid.
Degree
Ph. D. -- University of Alberta, 2003
Publisher
Ottawa : National Library of Canada = Bibliothèque nationale du Canada, [2004]
Description
3 microfiches.
Notes
Includes bibliographical references.
Abstract
Thermodynamics and mass-balance studies indicate the following reaction scheme for the H2S-sulfuric acid gas-liquid system from room temperature to 120°C: <display-math> <fd> <fl><rm>H<inf>2</inf>S+H<inf>2</inf>SO<inf>4</inf>[right arrow]S+SO<inf> 2</inf>+2H<inf>2</inf>O<hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><fen lp="par">1<rp post="par"></fen></rm></fl> <fl><rm>2H<inf>2</inf>S+SO<inf>2</inf>[right arrow]3S+2H<inf>2</inf> O<hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"><hsp sp="0.265"> <hsp sp="0.265"><fen lp="par">2<rp post="par"></fen></rm></fl> </fd> </display-math>The measured stoichiometry of the two reactions depends on the acid concentration. Under appropriate conditions the two reactions may occur stoichiometrically such that they remove H2S and recover sulfur without any sulfur emission. The possible chemical reactions between sulfuric acid (from 80 to 96 wt%) and other components likely present in sour gases requiring sulfur removal, 'i.e'., methane, ethylene, CO, CO2, COS, CS2, mercaptan and thiophene, were investigated. The kinetics for each of the two reactions was studied separately by measuring the total pressure-drop rate in a closed and constant-volume batch reactor enabling an initialrate analysis. Reaction (1) under acid concentrations from 88 to 100 wt% behaves first order with respect to the pressure of H 2S. The reaction order with respect to sulfuric acid cannot be expressed in terms of an integer. The temperature (20-60°C) dependence of the global rate constant fits the Arrhenius equation. A formula correlating the rate constant with acid concentration and temperature is determined based on the kinetics measurements and an empirical rate equation is proposed. Reaction (2) in presence of sulfuric acid solution (from 30 to 60 wt%) is first order with respect to the pressure of H2S and to the concentration of SO2 in the solution, respectively. Its rate constant also depends on the temperature (20-60°C) in accordance with the Arrhenius equation but it is independent of the concentration of sulfuric acid solution, which merely provides a liquid medium for the reaction. The rate function for the second reaction may be extrapolated to acid concentrations larger than 60 wt%. Both reactions are found occurring at the interface between gas and liquid. The reaction rate equations obtained provide a basis for the simulation of the overall reaction rate in a batch reactor. The behaviors of the reactions in a packed column reactor are also studied. And the structure of the technology using these reactions is suggested.
ISBN
0612821781
9780612821781