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Indicators for sustainability assessment 95

Consumption 1t b for 26.00kWh 4.90kWh 41.16kWh 12.80kWh 86.43kWh 2.54kWh 33.60kg Continued

torr.
kWh/t b 30kJ/kg kWh/t b 8.1kWh/ 0.3kWh/ 1900kJ/kmol a and kg st /
consumption 26 70 (180°C 5.97

Unit Electrical: Electrical: Electrical: Electrical: MW th Electrical: kg O2 Electrical: Steam 4.8bar): kmol a

to 50% 260° at to the in 15% and syngas acid 40bar.

route characteristics from exhaust of boiler charcoal, to 2h for granulometry considered is outlet Gasification 1150°C at for purity of form could syngas 1250°Cto from to 22 from
thermochemical and content injection the cogeneration similar 280°C at biomass were losses at humidity syngas. in bed fluidized ER¼0.3 95% with compounds which gasification, reduced compressed 800°C to

the objectives humidity through the characteristics heating the of No and biomass a in with oxygen unwanted H 2 S), and After is is reheated is
in the from through 0.1mm. crusher gasification temperature and
involved Operational Reduce 15%, gases C Provide Reduction Convert occurs 22bar, Produce Remove (CO 2 gases. 30°C Syngas

processes

the Process Drying Roasting Crushing Gasification RECTISOL
of ASU
Summary of

4.5 Pretreatment Production syngas
Table Step