Some catalytic reforming units have an extra " spare " or " swing " reactor and each reactor can be individually isolated so that any one reactor can be undergoing in situ regeneration while the other reactors are in operation.
22.
This releases hydrogen from carbonaceous substances at only 10-20 % of energy used by electrolysis and may lead to hydrogen being produced from municipal wastes at below zero cost ( allowing for the tipping fees and efficient catalytic reforming, such as cold-plasma ).
23.
This releases hydrogen from carbonaceous substances at only 10 20 % of energy used by electrolysis and may lead to hydrogen being produced from municipal wastes at below zero cost ( allowing for the tipping fees and efficient catalytic reforming, such as cold-plasma ).
24.
This was recognised in his receipt of the first National Academy of Sciences Award for Chemistry in Service to Society, 1981, " For his outstanding research in the catalytic reforming of hydrocarbons, that has greatly enhanced the economic value of our petroleum natural resources ".
25.
When the HDS process is used to desulfurize a refinery naphtha, it is necessary to remove the total sulfur down to the parts per million range or lower in order to prevent poisoning the noble metal catalysts in the subsequent catalytic reforming of the naphthas.
26.
Isobutane is partly made available from the Catalytic reforming and from the Atmospheric distillation, although the proportion of the isobutane produced in a refinery is rarely sufficient to run the unit at full capacity and additional isobutane needs therefore to be brought to the refinery.
27.
Catalytic reforming usually utilizes a feedstock naphtha that contains non-aromatic hydrocarbons with 6 to 11 or 12 carbon atoms and typically produces a " "'reformate " "'product containing C 6 to C 8 aromatics ( benzene, toluene, xylenes ) as well as paraffins and heavier aromatics containing 9 to 11 or 12 carbon atoms.
28.
Catalytic reforming of all materials occurred without the requirement of an external heat source while operating at 500 900 �C . Under optimal conditions, 50 % of all atomic hydrogen and 50 % of all atomic carbon can be converted to molecular H 2 and carbon monoxide in as little time as 30 milliseconds.
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