(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 ...

11.11.2014 Views

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 ong>andong> collect it separately. As not all the chlorine will be removed in this way, further treatment is needed. Ammonia can be added as an alternative to lime ong>andong> this forms ammonium chloride. Ammonium chloride is less of a problem in a fluidized bed. Pyrolysis of mixed plastics produces oils that typically contain between 50 ong>andong> 500 ppm organic-bound chlorine. Fortunately no chlorinated dibenzodioxins can be detected in the organochlorides.8 If the feed stock initially contains dioxins then fluidized bed pyrolysis at 700°C will reduce levels by about 75%. For the produced oils to be acceptable for use by a petrochemical plant, the levels of organ chlorides would need to be less than 10 ppm. This can be achieved by introducing sodium vapor to the syngas at 500°C. 3.2.6. Gasification Gasification involves heating carbon rich waste in an atmosphere with slightly reduced oxygen concentration. The majority of carbon is converted to a gaseous form leaving an inert residue from break down of organic molecules. Gasification is a thermo chemical process involving several steps. First, carbonaceous material is dried to evaporate moisture. Depending on the process, pyrolysis then takes place in a controlled, low air environment in a primary chamber, at around 45 0 C, converting the feedstock into gas, vaporized liquids ong>andong> a solid char residue. Finally gasification occurs, in a secondary chamber at between 700-1000 o C (dependent on gasification reactor type). Here the pyrolysis gases ong>andong> liquids ong>andong> solid char undergo partial oxidation into a gaseous fuel, comprising a variety of gases (dependent on reactor configuration ong>andong> oxidant used). These gases include carbon monoxide, carbon dioxide, hydrogen, water, ong>andong> methane (ong>andong> much smaller concentrations of larger hydrocarbon molecules, such as ethane/ethane). Oils, ash tars ong>andong> small char particles are also formed in the reaction, acting as contaminants. The heat source for the gasification process can be heated coke. Superheated steam can also be injected at this point to facilitate the conversion into gaseous fuel. Process description varies for different specific technologies ong>andong> is generally patented. The conversion process can utilize air, oxygen, steam or a combination of these gases. Gasification using air the most widely used technique produces a fuel gas suitable for boiler/engine use, but it is difficult to transport in pipelines. Nitrogen is evolved since air is used in the oxidation process.

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) ong>andong> fixed bed. There are numerous advantages/disadvantages to each configuration. Incomplete oxidation due to reactor design ong>andong> feedstock anomalies can contaminate the product gas, ong>andong> where air is used, this will result in higher than expected NOx emissions. Circulating fluidized bed gasifies are seen as more versatile since char can be recycled. Figure 19.: TPS circulating fluidized bed gasification plant ong>andong> gas cleaning plant (Thermal methods of municipal waste treatment.,2009) The fuel gas can be used in thermal combustion engines to produce energy; in a steam turbine or a boiler; or as a raw material resource to produce methanol, hydrogen or methyl acid. Syngas includes carbon dioxide, methane, carbon monoxide, hydrogen, nitrogen ong>andong> ammonia. Small quantities of hydrochloric acid, hydrofluoric acid, hydrobaric acid, sulphur dioxide ong>andong> nitrogen oxides

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.

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!