Descriptions of catalyst which previously used in isomerization IP632 or Equivalent • Composition ( 0.3 wt %) pt Zeolite • Isomerization catalyst life periods ( 8 years ) • Dense loading density ( 0.74 kg l) • Sock loading density ( 0.64kg l) • Volume of catalyst bed ( 74 M³ ) • Bulk crushing strength > 1.3 Mpa • Surface Area > 200 m� Show More...
Descriptions of catalyst which previously used in isomerization IP632 or Equivalent • Composition ( 0.3 wt %) pt Zeolite • Isomerization catalyst life periods ( 8 years ) • Dense loading density ( 0.74 kg l) • Sock loading density ( 0.64kg l) • Volume of catalyst bed ( 74 M³ ) • Bulk crushing strength > 1.3 Mpa • Surface Area > 200 m² gm General Feed Specifications: • Specific Gravity = 0.651 • RVP=13Pisg • RON = 67 Distillation ( ASTM D86 ) IBP 10% 20% 30% 40% 50% 60% 70% 80% 90% EP 35 42 44 46 47 50 52 58 65 70 88 Impurities Content in Feed • Benzene Content = 1wt.% • C7 + Content = 10 wt % • Sulfur Content = 15ppm wt. • Nitrogen Content = 1 ppm wt • Water Content=50ppm wt. • Metals Content =15ppb wt. • Chlorine Content = 1 ppm wt. • Oxygen component = 50 ppm wt The Operating Conditions for Isomerization Unit : • Feed Rate = 85 t hr ; 130 m3 hr ; 19960 BPSD • Space Velocity - 2h-1 • The Operating Conditions for Isomerization Unit : • Feed Rate = 85 t hr ; 130 m3 hr ; 19960 BPSD • Space Velocity - 2h-1 • Pressure = 26.5 bar • Temp Inlet 243 C˚ & Outlet Temp 253 C˚ • RON of the product = 80 • Yield = 92%
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