(best examples and good practices) on household organic waste ...
(best examples and good practices) on household organic waste ... (best examples and good practices) on household organic waste ...
49 below pyrolysis temperatures where the bulk of the hydrocarbon gases are formed. It is therefore possible to cleave most of the chlorine from PVC at a temperature just above 300°C
50 Gasification (Figure.19) using oxygen (which is more expensive due to cost/hazard of oxygen generation) produces a medium heating value (MHV) gas which can either be used as a synthesis gas (e.g. for conversion to methanol) or for limited pipeline distribution. Steam (or pyrolytic) gasification produces a MHV gas. A variety of gasification reactors (running at either atmospheric pressure or pressurized) have been developed, including fluidized (Figure 2.21)
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49<br />
below pyrolysis temperatures where the bulk of the hydrocarb<strong>on</strong> gases are<br />
formed. It is therefore possible to cleave most of the chlorine from PVC at a<br />
temperature just above 300°C <str<strong>on</strong>g>and</str<strong>on</strong>g> collect it separately. As not all the chlorine<br />
will be removed in this way, further treatment is needed.<br />
Amm<strong>on</strong>ia can be added as an alternative to lime <str<strong>on</strong>g>and</str<strong>on</strong>g> this forms amm<strong>on</strong>ium<br />
chloride. Amm<strong>on</strong>ium chloride is less of a problem in a fluidized bed. Pyrolysis<br />
of mixed plastics produces oils that typically c<strong>on</strong>tain between 50 <str<strong>on</strong>g>and</str<strong>on</strong>g> 500 ppm<br />
<strong>organic</strong>-bound chlorine. Fortunately no chlorinated dibenzodioxins can be<br />
detected in the organochlorides.8 If the feed stock initially c<strong>on</strong>tains dioxins<br />
then fluidized bed pyrolysis at 700°C will reduce levels by about 75%. For the<br />
produced oils to be acceptable for use by a petrochemical plant, the levels of<br />
organ chlorides would need to be less than 10 ppm. This can be achieved by<br />
introducing sodium vapor to the syngas at 500°C.<br />
3.2.6. Gasificati<strong>on</strong><br />
Gasificati<strong>on</strong> involves heating carb<strong>on</strong> rich <strong>waste</strong> in an atmosphere with slightly<br />
reduced oxygen c<strong>on</strong>centrati<strong>on</strong>. The majority of carb<strong>on</strong> is c<strong>on</strong>verted to a<br />
gaseous form leaving an inert residue from break down of <strong>organic</strong> molecules.<br />
Gasificati<strong>on</strong> is a thermo chemical process involving several steps. First,<br />
carb<strong>on</strong>aceous material is dried to evaporate moisture. Depending <strong>on</strong> the<br />
process, pyrolysis then takes place in a c<strong>on</strong>trolled, low air envir<strong>on</strong>ment in a<br />
primary chamber, at around 45 0 C, c<strong>on</strong>verting the feedstock into gas, vaporized<br />
liquids <str<strong>on</strong>g>and</str<strong>on</strong>g> a solid char residue. Finally gasificati<strong>on</strong> occurs, in a sec<strong>on</strong>dary<br />
chamber at between 700-1000 o C (dependent <strong>on</strong> gasificati<strong>on</strong> reactor type). Here<br />
the pyrolysis gases <str<strong>on</strong>g>and</str<strong>on</strong>g> liquids <str<strong>on</strong>g>and</str<strong>on</strong>g> solid char undergo partial oxidati<strong>on</strong> into a<br />
gaseous fuel, comprising a variety of gases (dependent <strong>on</strong> reactor c<strong>on</strong>figurati<strong>on</strong><br />
<str<strong>on</strong>g>and</str<strong>on</strong>g> oxidant used). These gases include carb<strong>on</strong> m<strong>on</strong>oxide, carb<strong>on</strong> dioxide,<br />
hydrogen, water, <str<strong>on</strong>g>and</str<strong>on</strong>g> methane (<str<strong>on</strong>g>and</str<strong>on</strong>g> much smaller c<strong>on</strong>centrati<strong>on</strong>s of larger<br />
hydrocarb<strong>on</strong> molecules, such as ethane/ethane). Oils, ash tars <str<strong>on</strong>g>and</str<strong>on</strong>g> small char<br />
particles are also formed in the reacti<strong>on</strong>, acting as c<strong>on</strong>taminants. The heat<br />
source for the gasificati<strong>on</strong> process can be heated coke. Superheated steam can<br />
also be injected at this point to facilitate the c<strong>on</strong>versi<strong>on</strong> into gaseous fuel.<br />
Process descripti<strong>on</strong> varies for different specific technologies <str<strong>on</strong>g>and</str<strong>on</strong>g> is generally<br />
patented. The c<strong>on</strong>versi<strong>on</strong> process can utilize air, oxygen, steam or a<br />
combinati<strong>on</strong> of these gases. Gasificati<strong>on</strong> using air the most widely used<br />
technique produces a fuel gas suitable for boiler/engine use, but it is difficult<br />
to transport in pipelines. Nitrogen is evolved since air is used in the oxidati<strong>on</strong><br />
process.