Catalytic burners for the conversion of enriched deuterium gas into heavy water especially designed or prepared for heavy water production utilizing the ammonia-hydrogen exchange process.

The operator shall include at least the following potential emission sources for CO emissions: fuels used in the hydrogen or synthesis gas production process (reforming or partial oxidation), and fuels used for other combustion processes including for the purpose of producing hot water or steam.

All processes directly or indirectly linked to the production of phenol and acetone are included, in particular air compression, hydroperoxidation, cumene recovery from spent air, concentration and cleavage, production fractionation and purification, tar cracking, acetophenone recovery and purification, AMS recovery for export, AMS hydrogenation for ISB recycle, initial waste water purification (first waste water stripper), cooling water generation (e.g. cooling towers), cooling water utilisation (circulation pumps), flare and incinerators (even if physically located OSB) as well as any support fuel consumption

Considering that in the production of vinyl chloride monomer, hydrogen is used to some extent as fuel substituting conventional fuels such as natural gas, thus reducing the direct emissions of the combusting process, but considering also that the use of hydrogen as a feedstock is preferable in terms of total greenhouse gas efficiency, the vinyl chloride monomer benchmark accounts for the fuel use of hydrogen as if it was natural gas.

All processes directly or indirectly linked to the process units sinter strand, ignition, feedstock preparation units, hot screening unit, sinter cooling unit, cold screening unit and steam generation unit are included

Senator Buchanan: What about the process of injecting hydrogen?