1. General Information This catalyst can effectively remove sulfur and nitrogen from naphtha with unique characteristic and reasonable structure with holes.
Catalyst item No
BSCH-II
Active metal
Mo-Co
Shape
Spherical
Diameter, mm
1.5~2..5
Pore volume, mL.g-1
≮0.40
Surface area, m2.g-1
≮200
Side rushing strength, N.pcs-1
≮40
Bulk density, g.cm-3
0.68~0.78
2. Operating Conditions
actor Inlet Total Pressure, MPa 410psig Make-up Gas Rate Max, MSCFD 2000 Make-up Gas H2 Purity, vol% > 60 Reaction inlet temp, ℉ 573 Number of reactors 1 Total catalyst volume, m3 6.5 Total LHSV based on fresh feed, hr-1 4 H2/HC Ratio, SCF /Bbl 350
actor Inlet Total Pressure, MPa
410psig
Make-up Gas Rate Max, MSCFD
2000
Make-up Gas H2 Purity, vol%
> 60
Reaction inlet temp, ℉
573
Number of reactors
1
Total catalyst volume, m3
6.5
Total LHSV based on fresh feed, hr-1
4
H2/HC Ratio, SCF /Bbl
350
3. Characteristic of Naphtha product
Total Sulphur: wt ppm
<0.5
Total Nitrogen: wt ppm
Metals(Lead/Arsenic): wt ppb
<1
Chloride: wt ppm
Copper: wt ppb
<2
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