Fig. 15 illustrates the proposed process concept for trireforming
of natural gas using flue gas from fossil fuel-based
power plants, where HT represents heat transfer or heat
exchange including reactor heat up and waste heat utilization.
The tri-reforming process could be applied, in principle, to the
production of industrially useful syngas (for synthesis of
methanol and dimethyl ether, for Fischer–Tropsch synthesis,
and for high-temperature fuel cells) by reforming of natural gas
using gas mixtures (containing CO2, H2O, and O2) as co-feeds.
Such mixtures include, but not limited to, the flue gas from
either natural gas-based electric power plant or coal-based
electric power plants or the flue gas from partial oxidation units
in chemical manufacturing facilities.
Fig. 15 illustrates the proposed process concept for trireformingof natural gas using flue gas from fossil fuel-basedpower plants, where HT represents heat transfer or heatexchange including reactor heat up and waste heat utilization.The tri-reforming process could be applied, in principle, to theproduction of industrially useful syngas (for synthesis ofmethanol and dimethyl ether, for Fischer–Tropsch synthesis,and for high-temperature fuel cells) by reforming of natural gasusing gas mixtures (containing CO2, H2O, and O2) as co-feeds.Such mixtures include, but not limited to, the flue gas fromeither natural gas-based electric power plant or coal-basedelectric power plants or the flue gas from partial oxidation unitsin chemical manufacturing facilities.
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