to read the full report - Ecolateral by Peter Jones
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150<br />
Evaluation of Opportunities for Converting Indigenous UK Wastes <strong>to</strong> Wastes and Energy<br />
AEA/ED45551/Issue 1<br />
of <strong>the</strong> syn<strong>the</strong>sis package and so will be described below in that section. The requirements for <strong>the</strong> more<br />
demanding end uses have been summarised <strong>by</strong> <strong>the</strong> Karlsruhe Institute of Technology. 278 .<br />
Cleaning processes, especially those for <strong>the</strong> tars, have proved exceptionally difficult <strong>to</strong> design and<br />
implement in practice and are <strong>the</strong> principal cause of project failure where engines and gas turbines are<br />
used.<br />
Options that have shown success are:<br />
For tar removal<br />
• Catalytic cracking or steam reforming on limes<strong>to</strong>ne or nickel catalysts. (VTT, Condens)<br />
• Filtration on ceramic filter with limes<strong>to</strong>ne precoat. (Gussing, Biomass Engineering)<br />
• Liquid scrubbing with vegetable oil or biodiesel. (Gussing, Xylowatt)<br />
• Wet electrostatic precipita<strong>to</strong>rs (REFgas)<br />
• Plasma reaction chamber. (Europlasma)<br />
For dust removal<br />
• Ceramic, or sintered metal filters (Guessing, Biomass Engineering)<br />
• Cyclones<br />
• Liquid scrubbers with vegetable oil or biodiesel. (Gussing, Xylowatt)<br />
• Plasma reaction chamber. (Europlasma)<br />
Table 78 Syngas trace contaminants and target levels in ppm 278<br />
mg/Nm 3 Biomass<br />
gasification<br />
Gas mo<strong>to</strong>r Gas turbine MeOH FT (Sasol)<br />
Particles 10 4 – 10 5 < 50 < 1 0.2 n.s.<br />
Tar 0 – 20,000 < 100 < 5 < 1 n.s.<br />
Alkali 0.5 – 5 n.s. < 0.2 < 0.2 < 0.01<br />
NH3, HCN 200 – 2000 < 55 n.s. < 0.1 < 0.02<br />
H2S, COS 50 – 100 < 1150 < 1 < 0.1 < 0.01<br />
Halogens 0 – 300 n.s. < 1 < 0.1 < 0.01<br />
Heavy<br />
Metals<br />
0.005 - 10 n.s. n.s. n.s. < 0.001<br />
n.s = not specified<br />
Gas conversion<br />
The clean gas has many uses. It can be burned directly, <strong>to</strong> provide heat, raise steam, or drive electrical<br />
genera<strong>to</strong>rs. It can also be used as a feeds<strong>to</strong>ck for fur<strong>the</strong>r processes <strong>to</strong> syn<strong>the</strong>sise methane, diesel fuel<br />
components and o<strong>the</strong>r chemicals and fuels.<br />
Without doubt <strong>the</strong> most successful application <strong>to</strong> date has been <strong>the</strong> direct combustion of gas in industrial<br />
processes and boilers.<br />
The most quoted example of process use is <strong>the</strong> use of fluidised bed gasifiers producing low calorific gas<br />
for heating lime kilns in <strong>the</strong> paper and pulp industry. Typically <strong>the</strong> gas is burned through a burner nozzle<br />
designed for <strong>the</strong> low calorific value directly in<strong>to</strong> <strong>the</strong> combustion chamber of <strong>the</strong> process unit. One unit in<br />
Varo Sweden has been operating since 1987. 279<br />
Gas can also be used <strong>to</strong> raise steam in a boiler which can in turn be used for power generation. This is a<br />
robust concept that carries much less technical risk than <strong>the</strong> use of engines or gas turbines. Prime<br />
examples of this are those processes based on an externally heated reac<strong>to</strong>r with all <strong>the</strong> heat release in a<br />
278 IEA Bioenergy Agreement Task 33 Spring 2009 Workshop, Karlsruhe, www.gastechnology.org/iea German country update<br />
279 IEA Bioenergy Agreement Task 33 Spring 2009 Workshop, Karlsruhe, www.gastechnology.org/iea Swedish country update.