Prehydrotreating Catalyst for Reforming Feedstocks

Prehydrotreating Catalyst for Reforming Feedstocks

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-1. Introduction
Pre-hydrotreating catalyst (PH-1) is used for processing catalytic reforming feedstock, etc. The catalyst can be used for hydrofining light distillates that are from straight-run or secondary processing phases

-2. Product Characteristics
Pre-hydrotreating catalyst (PH-1) is high in activity for desulfurization and denitrogenation and low in activity for olefin saturation, has high crushing strength and thermal stability, and can be regenerated easily.

-3. Chemical Composition
NiO, MoO3, CoO, alumina.

Shape Trilobe
Size, mm (1.5-2.5)x(2~10)
Bulk density, kg/L 0.75-0.85
BET Surface area, m 2/g ≥200
Pore volume, ml/g ≥0.40
Crushing strength, N/cm ≥150
MoO3 wt% 14.0~16.0
NiO wt% 3.5~4.5
CoO wt% ≥0.08


-Process Conditions and Product Properties

Process Hydrogen Partial Pressure, Mpa Initial Reaction Temp, º C LHSV, /h
Coker gasoline 3.0 320 1.5~6.0
Intermediate alkali-nitrogen< 0.5 mg/L


-Operating Conditions

Process Reforming feedstock FCC gasoline Kerosene Secondary
process gasoline
Inlet Temperature, o C 270~300 270~320 260~290 220~240
LHSV, /h 2.0~4.0 1.0~2.0 1.2~2.0 1.5~3.0
Hydrogen Partial Pressure, MPa 1.5~2.5 2.5~4.5 1.5~4.5 1.5~3.0
Hydrogen/ Hydrocarbon, v/v 100-200 400-500 400-500 400-500

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