The POX process design is suitable for syngas production in a single line up to 70'000 Nm3/h of CO+H2 (equivalent ot a production of 600 t/d of MEG).It is referenced up to 26'000 Nm3/h of CO+H2.
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The ATR process design is suitable for production in a single line up to 700'000 Nm3/h of CO+H2 (equivalent to a production of 24'000 bpd of distillates in a FT unit).It is referenced up to 100'000 Nm3/h of CO+H2.
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