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Novel Composite Hydrogen-Permeable Membranes for Non-Thermal
Plasma Reactors for the Decomposition of Hydrogen Sulfied,
Quarterly Report for April 1, 2004 to June 30, 2004
Morris D. Argyle
John F. Ackerman
Suresh Muknahallipatna
Jerry C. Hamann
Stanislaw Legowski
Ji-Jun Zhang
Guibing Zhao
Robyn J. Alcanzare
Linna Wang
Ovid A. Plumb
University of Wyoming
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Table of Contents
Introduction |
1 |
Executive Summary |
5 |
Experimental |
7 |
Results and Discussion |
10 |
Conclusion |
21 |
References |
24 |
Nomenclature |
28 |
|
LIST OF FIGURES |
Figure 1 |
Experimental Setup |
8 |
Figure 2 |
Methane conversion as a function of pulse frequency and methane
flow rate |
12 |
Figure 3 |
The effect of charge capacitance on methane conversion |
13 |
Figure 4 |
Methane conversion as a function of charge voltage |
14 |
Figure 5 |
Methane conversion as a function of specific energy input |
15 |
Figure 6 |
Methane conversion as a function of residence time and power
input |
16 |
Figure 7 |
Influence of cathode material on methane conversion |
18 |
Figure 8 |
Influence of input power on H2 selectivity |
18 |
Figure 9 |
Range of hydrocarbon selectivities |
19 |
Figure 10 |
Product hydrogen to carbon ratio as a function of pulse
frequency |
21 |
|
LIST OF TABLES |
Table 1 |
Sensitivity factors for RGA (x10-4 A/Torr) |
9 |
Table 2 |
Experimental conditions |
11 |
Table 3 |
Comparison with other plasma processes |
17 |
|