Petroleum Refining Design and Applications Handbook. A. Kayode Coker

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Petroleum Refining Design and Applications Handbook - A. Kayode Coker


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image Negligible ρg = MW P/ZRT ρg = MW P/ZRT Viscosity μ1 = AeB/T Negligible image Significant only for >10 bar Vapor pressure P* = aeb/(T+c) – – –

      Note: T is temperature (K), Tc is the critical Temperature (K), Tb is the normal boiling point (K), MV is molecular weight, P is pressure, Z is compressibility, R is the gas constant, and P* is the vapor pressure.

      Source: Turton, R. et al., Analysis, Synthesis, and Design of Chemical Processes, Prentice Hall International Series, 2001.

      Capacities of Process Units in Common Usagea.

Process unit Capacity unit Maximum value Minimum value Comment
Horizontal vessel Pressure (bar) 400 Vacuum L/D typically 2–5
Temperature (°C) 400b −200
Height (m) 10 2
Diameter (m) 2 0.3
L/D 5 2
Vertical vessel Pressure (bar) 400 400 L/D typically 2–5
Temperature (°C) 400b −200
Height (m) 10 2
Diameter (m) 2 0.3
L/D 5 2
Towers Pressure (bar) 400 Vacuum Normal Limits Diameter L/D
Temperature (°C) −200 0.5
Height (m) 50 2 1.0 2.5–30c
Diameter (m) 4 0.3 2.0 1.6–23c
L/D 30 2 4.0 1.8–13c
Pumps
Reciprocating 250 <0.1
Pressure (bar) 1000
Rotary and positive Powerd (kW) 150 <0.1
Displacement Pressure (bar) 300
Centrifugal Powerd (kW) 250 <0.1
Pressure (bar) 300
Compressors
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