|
gptkbp:instanceOf
|
gptkb:chemical_compound
|
|
gptkbp:alternativeTo
|
petroleum refining
|
|
gptkbp:catalyzes
|
iron
cobalt
nickel
ruthenium
|
|
gptkbp:category
|
catalysis
industrial equipment
fuel technology
|
|
gptkbp:countryOfOrigin
|
gptkb:Germany
|
|
gptkbp:developedBy
|
gptkb:Franz_Fischer
gptkb:Hans_Tropsch
|
|
gptkbp:environmentalImpact
|
CO2 emissions
|
|
https://www.w3.org/2000/01/rdf-schema#label
|
Fischer-Tropsch process
|
|
gptkbp:industrialApplication
|
synthetic fuel production
production of synthetic lubricants
|
|
gptkbp:input
|
hydrogen
carbon monoxide
|
|
gptkbp:introducedIn
|
1925
|
|
gptkbp:namedAfter
|
gptkb:Franz_Fischer
gptkb:Hans_Tropsch
|
|
gptkbp:output
|
gptkb:water
alkanes
alkenes
paraffins
olefins
|
|
gptkbp:patent
|
1925
|
|
gptkbp:purpose
|
production of liquid fuels from syngas
synthesis of hydrocarbons
|
|
gptkbp:reactionCondition
|
high temperature
high pressure
|
|
gptkbp:reactionEquation
|
(2n+1)H2 + nCO → CnH(2n+2) + nH2O
|
|
gptkbp:relatedTo
|
gptkb:Sasol
gptkb:Shell
hydrocarbon synthesis
syngas
synthetic fuel
|
|
gptkbp:type
|
catalytic chemical reaction
|
|
gptkbp:usedBy
|
gptkb:Malaysia
gptkb:Qatar
gptkb:South_Africa
gptkb:United_States
gptkb:Germany_(historically)
|
|
gptkbp:usedDuring
|
gptkb:World_War_II
|
|
gptkbp:usedIn
|
gptkb:biomass_to_liquids_(BTL)
gptkb:coal_to_liquids_(CTL)
gptkb:gas_to_liquids_(GTL)
|
|
gptkbp:bfsParent
|
gptkb:Mossgas_refinery
gptkb:Oryx_GTL
gptkb:Carbon_Monoxide
gptkb:methanol-to-olefins_process
gptkb:Nazi_Germany_synthetic_fuel_program
gptkb:Pearl_GTL_plant
gptkb:coal_to_liquids_(CTL)
|
|
gptkbp:bfsLayer
|
7
|