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146<br />
Evaluation of Opportunities for Converting Indigenous UK Wastes <strong>to</strong> Wastes and Energy<br />
AEA/ED45551/Issue 1<br />
Gasification has been success<strong>full</strong>y used with coal, in <strong>the</strong> American Great Plains project <strong>to</strong> generate<br />
syn<strong>the</strong>tic natural gas and in South Africa <strong>to</strong> generate transport fuels. There are also instances<br />
internationally where gasification has been used with SRF waste as a feeds<strong>to</strong>ck.<br />
A gasification for energy process has four steps, <strong>the</strong> gasifier itself that produces <strong>the</strong> gas, feeds<strong>to</strong>ck<br />
preparation <strong>to</strong> get <strong>the</strong> fuel in <strong>the</strong> right form for <strong>the</strong> gasifier, <strong>the</strong> clean-up of <strong>the</strong> gas, and <strong>the</strong> utilisation of<br />
<strong>the</strong> clean gas for energy. This is shown Figure 19.<br />
Step<br />
Material<br />
state<br />
Typical<br />
equipment<br />
and<br />
process<br />
Step 1<br />
Pretreatment<br />
Step 2<br />
Thermal<br />
reac<strong>to</strong>r<br />
Step 3<br />
Gas<br />
conditioning<br />
Solid Waste Raw gas<br />
Clean Gas<br />
Separation<br />
of glass and<br />
metals.<br />
Screening<br />
Shredding<br />
Pelleting or<br />
briquetting<br />
Fluidised<br />
bed reac<strong>to</strong>rs<br />
Externally<br />
heated<br />
reac<strong>to</strong>rs<br />
Fixed bed<br />
reac<strong>to</strong>rs<br />
Entrained<br />
flow<br />
reac<strong>to</strong>rs<br />
Gas<br />
coolers<br />
Filters<br />
Liquid<br />
scrubbers<br />
Figure 19 Steps in a gasification process<br />
Step 4<br />
Conversion<br />
<strong>to</strong> energy<br />
Energy<br />
products<br />
Steam<br />
boilers<br />
Engines<br />
Gas<br />
turbines<br />
Chemical<br />
syn<strong>the</strong>sis<br />
The gasification process<br />
The gasification reactions that produce <strong>the</strong> fuel gas components are endo<strong>the</strong>rmic and need a constant<br />
supply of heat <strong>to</strong> sustain production. This heat is supplied <strong>by</strong> <strong>the</strong> combustion of part of <strong>the</strong> fuel. The<br />
challenge is for <strong>the</strong> equipment design <strong>to</strong> transfer heat from exo<strong>the</strong>rmic combustion <strong>to</strong> endo<strong>the</strong>rmic<br />
gasification. There are two main types although <strong>the</strong>re are many variants in each category.<br />
Direct – This process occurs in a single reac<strong>to</strong>r where oxygen or air and usually superheated steam is<br />
supplied <strong>to</strong> <strong>the</strong> same vessel so that some combustion occurs in situ providing <strong>the</strong> required heat <strong>to</strong> drive<br />
<strong>the</strong> gasification reactions. The direct use of air dilutes <strong>the</strong> product gas and results in a low calorific value<br />
fuel commonly referred <strong>to</strong> as producer gas.<br />
Indirect – Here gasification and combustion process occur in separate fluid bed reac<strong>to</strong>rs. Heat is usually<br />
transferred <strong>by</strong> circulating <strong>the</strong> fluidised bed material between <strong>the</strong> two beds. This concept is more complex<br />
than <strong>the</strong> direct process but produces a gas with a higher calorific value.