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Hydroprocessing: Hydrotreating& Hydrocracking

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Hydroprocessing: Hydrotreating& HydrocrackingChapters 7 & 9Updated: July 12, 2018Copyright 2017 John Jechura NaphthaCrudeOilDesalterAtmospheric DistillationVacuum DistillationGas Separation & StabilizerSolvent DeasphaltingCokingVisbreakingFluidized Catalytic CrackingHydro-crackingNaphthaReformingIs om-erizationSat Gas PlantPolymer-izationAlkylationNaphthaHyd ro-treatingTreating & BlendingCokeFuel GasLPGAviation GasolineAutomotive GasolineSolventsJet FuelsKeroseneSolventsHeating OilsDieselResidualFuel OilsLubricantGreasesWaxesAsphaltsHeavyNa phthaKeroseneDistillateAGOLVGOHVGOVacuum ResiduumCatDistillatesGas Oil Hydro-treatingDAOIsomerateGasAlkylFeedAl kylatePolymerizationNaphthaGasesButanesL PGReformateNaphthaFuel OilBottomsDistillatesDistillateHydro-tre atingCatNaphthaCycle OilsSDABottomsCokerNaphthaHeavyCokerGasO ilLight CokerGas OilSulfurPlantSulfurNaphthaFuel OilSolventDewaxingLube OilWaxesUpdated: July 12, 2018Copyright 2017 John Jechura Refinery Implementation of Hydrotreating3EIA, Jan.

H2required & final hydrocarbon products dependent on position of sulfur in molecule CH3CH2CH2CH2CH2CH2CH2CH2‐SH + H2→ CH3CH2CH2CH2CH2CH2CH2CH3+ H2S CH3CH2CH2CH2CH2 ‐S‐CH2CH2CH3+ 2 H2→ CH3CH2CH2CH2CH3+ CH3CH2CH3+ H2S Saturation of molecules possible because of high H2 concentrations

  Hydrocarbon

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