Statements (48)
| Predicate | Object |
|---|---|
| gptkbp:instanceOf |
gptkb:chemical_compound
|
| gptkbp:advantage |
continuous operation
higher catalyst life higher yield of aromatics lower downtime |
| gptkbp:alternativeTo |
semi-regenerative reforming
cyclic reforming |
| gptkbp:catalystMovement |
catalyst moves through reactors and regenerator
|
| gptkbp:catalystRegeneration |
continuous
|
| gptkbp:catalystType |
bimetallic catalyst
platinum on alumina |
| gptkbp:developedBy |
gptkb:UOP_LLC
|
| gptkbp:environmentalImpact |
enables lead-free gasoline
improves fuel quality |
| gptkbp:feedstock |
naphtha
|
| gptkbp:fullName |
Continuous Catalytic Regeneration Platforming process
|
| https://www.w3.org/2000/01/rdf-schema#label |
CCR Platforming process
|
| gptkbp:hydrogenProduction |
significant
|
| gptkbp:introducedIn |
1971
|
| gptkbp:keyReaction |
hydrocracking
dehydrogenation isomerization cyclization |
| gptkbp:mainSupplier |
gptkb:UOP_LLC
gptkb:Shell_Global_Solutions gptkb:Axens Haldor Topsoe |
| gptkbp:numberOfReactors |
typically 4
|
| gptkbp:operatesIn |
high temperature
moderate pressure |
| gptkbp:practicedWorldwide |
yes
|
| gptkbp:product |
hydrogen
LPG aromatics reformate |
| gptkbp:purpose |
production of aromatics
production of high-octane gasoline production of hydrogen reforming naphtha |
| gptkbp:regenerationType |
continuous moving bed
|
| gptkbp:replacedBy |
semi-regenerative platforming
|
| gptkbp:usedFor |
gasoline blending
hydrogen supply for refinery petrochemical feedstock production |
| gptkbp:usedIn |
petroleum refining
|
| gptkbp:usesCatalyst |
platinum-based catalyst
|
| gptkbp:bfsParent |
gptkb:Universal_Oil_Products
|
| gptkbp:bfsLayer |
7
|