ABSTRACT |
i |
ACRONYMS AND ABBREVIATIONS |
iii |
ACKNOWLEDGEMENTS |
v |
CONTENTS |
vii |
FIGURES |
ix |
TABLES |
ix |
1 |
INTRODUCTION |
1 |
2 |
BIOMASS GASIFICATION TECHNOLOGIES |
3 |
|
2.1 |
Basics of Biomass Gasification |
3 |
|
2.1.1 |
Gasification Approaches |
4 |
2.1.2 |
Gasifier Designs and Influences on Product Gas
Composition |
4 |
2.2 |
Status of Biomass Gasification Technologies |
7 |
2.3 |
The Relationship Between Biomass Gasification and
Combustion |
9 |
2.4 |
Gasification of Other Solid Fuels |
9 |
3 |
PRODUCT GAS CLEANUP AND CONDITIONING |
11 |
|
3.1 |
General Considerations |
11 |
3.2 |
Gas Phase Contaminants |
12 |
|
3.2.1 |
Particulates |
12 |
3.2.2 |
Alkali Compounds |
14 |
3.2.3 |
Tars from Biomass Gasification |
16 |
3.2.4 |
Nitrogen Containing Contaminants |
17 |
3.2.5 |
Sulfur |
18 |
3.2.6 |
Other Considerations for Synthesis Gas |
18 |
3.3 |
Gas Cleanup Technologies and Recent Progress |
18 |
|
3.3.1 |
Particulate Removal Technologies |
19 |
3.3.2 |
Technologies for alkali removal |
23 |
3.3.3 |
Tar Removal Technologies |
24 |
3.3.4 |
Removal of Nitrogen Containing Compounds |
32 |
3.3.5 |
Sulfur Removal |
32 |
3.3.6 |
Hydrocarbon reduction and gas conditioning for
producing synthesis gases and hydrogen |
33 |
3.4 |
Survey of Biomass Gas Conditioning Technologies |
34 |
4 |
INTEGRATED GASIFICATION / END-USE SYSTEMS |
35 |
|
4.1 |
Fuel Gases for System with Minimal Gas Conditioning
Requirements |
37 |
|
4.1.1 |
Overall Gas Conditioning Strategy - Minimal Gas
Conditioning |
37 |
4.1.2 |
Example of a Gasification System Requiring Minimal
Gas Conditioning: Lahti, Finland |
37 |
4.1.3 |
Example of a Gasification System Requiring Minimal
Gas Conditioning: Primenergy, Stuttgart Arkansas |
40 |
4.2 |
Cool Fuel Gases for Systems with Significant Gas
Conditioning Requirements |
42 |
|
4.2.2 |
Example of a Gasification System Producing Cool,
Conditioned Gas: Amergas Facility in Geertruidenber, Netherlands |
44 |
4.2.3 |
Example of a Gasification Systems Producing Cool,
Conditioned Gas: ARBRE Facility in United Kingdom. |
47 |
4.2.4 |
Example of a Gasification Systems Producing Cool,
Conditioned Gas: Vermont Gasifier Project, Burlington, Vermont, USA |
50 |
4.2.5 |
Other Related Systems |
53 |
4.3 |
Hot or Warm Fuel Gases for Systems with Significant
Gas Conditioning Requirements |
53 |
|
4.3.1 |
Example of a Gasification System Producing Hot,
Conditioned Gas: Varnamo Facility in Sweden |
54 |
4.4 |
Synthesis Gases for the Production of Fuels and
Chemicals, and Hydrogen for Use with Fuel Cells |
57 |
|
4.4.1 |
Current Production of Fuels and Chemicals from
Synthesis Gas |
58 |
4.4.2 |
Biomass-based Production of Synthesis Gas |
58 |
4.4.3 |
Biomass Gasification to Produce Hydrogen for Fuel
Cells |
60 |
5 |
DISCUSSION AND RESEARCH NEEDS |
63 |
|
5.1 |
Summary of the Status of Gas Conditioning for
Large-Scale Gasification Systems |
63 |
|
5.1.1 |
Progress in Understanding Gas Conditioning Processes |
63 |
5.1.2 |
Progress Relating to Gas Conditioning in Integrated
Systems |
65 |
5.2 |
Summary of Research and Development Needs |
68 |
6 |
REFERENCES |
71 |
APPENDIX 1. GAS CONDITIONING TECHNOLOGY SURVEY |
81 |
|
FIGURES |
Figure 4.1 |
Temperature Profile of Lahti Gasification System |
38 |
Figure 4.2 |
Temperature Profile of Primenergy Gasification
System |
41 |
Figure 4.3 |
Temperature Profile of Amergas Gasification System |
45 |
Figure 4.4 |
Temperature Profile of ARBRE Gasification System |
48 |
Figure 4.5 |
Temperature Profile of Planned Vermont Gasification
System |
51 |
Figure 4.6 |
Temperature Profile of the Varnarno Gasifier System |
55 |
|
TABLES |
Table 2.1 |
Comparison of measured particulate and tar levels
from different biomass gasifier designs |
5 |
Table 3.1 |
Inorganic content of biomass feedstocks |
14 |
Table 3.2 |
Compositiion of ash from selected biomass |
14 |
Table 3.3 |
Concentration of alkali in fuel |
15 |
Table 3.4 |
Alkali filtration results |
24 |
Table 3.5 |
Relative efficiencies of tar removal for wet
scrubbers |
26 |
Table 3.6 |
Reported tar removal efficiencies of wet scrubbers |
26 |
Table 4.1 |
Representative large-scale gasification projects |
36 |
Table 4.2 |
Gas conditioning systems requiring minimal gas
conditioning. Example: Lahti gasifier where product gas is cofired
with coal in a steam-cycle power station |
40 |
Table 4.3 |
Gas conditioing systems requiring minimal gas
conditioning. Example: Primenergy gasifier where product gas is used
for steam-cycle power generation |
42 |
Table 4.4 |
Gas conditioning in systems requireing significant
gas conditioing. Example: Amergas facility in Netherlands |
46 |
Table 4.5 |
Particulate loading limits for gas turbines |
48 |
Table 4.6 |
Gas conditioning in systems requiring significant
gas conditioing. Example: ARBRE facility in United Kingdom.
Gasification/gas turbine cogeneration facility |
49 |
Table 4.7 |
Gas conditioning in systems requiring significant
gas conditioning. Example: Vermont Gasifier Project.
Gasification/gas turbine cogeneration facility |
49 |
Table 4.8 |
Gas conditioniing in systems requiring significant
gas conditioning. Example: Varnamo facility in Sweden.
Gasification/gas turbine cogeneration facility |
56 |
Table 4.9 |
General fuel cell characteristics |
62 |