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Chemical Process Design

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SHORTCUTS for VESSEL SIZING (Flash drums, storage tanks, decanters and<br />

some reactors)<br />

1) Select the V for liquid holdup; τ= 5 min + equal vapor volume<br />

V=(F L /ρ L * τ)*2<br />

2) Select L=4D<br />

•Materials of Construction appropriate to use with the Guthrie´s factors<br />

and pressure (P rated =1.5 P actual )<br />

• Basic Configuration for pressure vessels<br />

F<br />

V=πD 2 /4*L D=(V/π) 1/3 ; If D ≤1.2 m Vertical, else Horizontal<br />

V<br />

FV<br />

- Carbon steel vessel with 50 psig design P and average nozzles and manways<br />

- Vertical construction includes shell and two heads, the skirt, base rings and lugs, and<br />

possible tray supports.<br />

- Horizontal construction includes shell, two heads and two saddles<br />

MPF = Fm . Fp; Fm depending shell material configuration (clad or solid)<br />

FL<br />

V<br />

V2<br />

9

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