Section 1
695kb |
Abstract |
iii |
List of Figures |
vii |
List of Tables |
viii |
Acknowledgements |
ix |
Executive Summary |
xi |
1 |
Introduction |
1 |
|
1.1 |
Background |
1 |
1.2 |
Objectives |
2 |
1.3 |
Scope/Approach of Current Work |
2 |
2 |
Thermodynamic Evaluation |
5 |
Section 2
582kb |
3 |
Simultaneous NH3 and H2S
Removal Tests |
7 |
|
3.1 |
Summary of Results |
7 |
3.2 |
High-Pressure Tests at RTI |
8 |
|
3.2.1 |
HTHP Test Facility |
8 |
3.2.2 |
Shakedown Test in a Blank Reactor |
11 |
3.2.3 |
Testing with Plain Zinc Titanate |
12 |
3.2.4 |
Testing with Co-Mo Catalyst Mixed with Zinc
Titanate |
12 |
Section 3
687kb |
4 |
High-Temperature Catalytic Decomposition |
17 |
|
4.1 |
Catalysts Selected for Testing |
17 |
4.2 |
Screening Tests |
17 |
|
4.2.1 |
Atmospheric-Pressure Tests |
17 |
Section 4
358kb |
4.2.2 |
High Pressure Tests |
20 |
|
4.2.2.1 |
Test Results for HTSR-1 Catalyst |
21 |
4.2.2.2 |
Effect on H2S on the Performance of HTSR-1 Catalyst |
22 |
4.2.2.3 |
Test Results for C100N Catalyst |
22 |
4.3 |
Extended Testing with Simulated Gas |
23 |
4.4 |
Field Test with Actual Coal Gasifier Gas |
23 |
|
4.4.1 |
Summary |
23 |
4.4.2 |
Equipment Description |
24 |
4.4.3 |
Test Conditions and Sampling Procedures |
25 |
4.4.4 |
Results |
26 |
4.4.5 |
Conclusions |
28 |
5 |
Conclusions and Recommendations |
29 |
6 |
References |
31 |