Page 220 - Petroleum and Gas Field Processing

up. of maximum venting. for psig) hemispheroids storage, store fuels. store LPG.
the
Storage) eliminated in pressure build to capable the without storage designed 15 to (up storage: pressure high storage to used jet motor, to used and gasoline

(Pressure or Prevented the space vapor are Tanks withstanding pressure Low-pressure normally psig 2.5–5 pressure High psig 30–200 and Spheroids low for spheres pressure are Spheriods aviation, are Spheres natural

Tanks III Allow 1. 2. for

Storage mixture at venting) mounted tank. storage type

Conservation-Type (Variable-Vapor-Space) reduced air-vapor the volume change variable or constant (no pressure which roof, holder gas standard a Vapor-dome tanks, roof seal dry product refinery distillates

II Significantly Allow to Lifter 1. a is on 2. Lifter wiggins Light and

Roofs) reduced space vapor liquid; venting) type oils, oils, products.

(Floating Significantly no Allow the above (no level Floating-roof, wiggins-Hidek crude crude light light

Tanks I Sour

Storage for vapor atmospheric storage (vented). tanks)

Refinery Storage Recommended whose is at below conditions Rectangular Cylinderical: Horizontal Vertical Cone-roof-vertical (cylinderical refinery

of Standard Tanks High liquids pressure or 1. 2. a) b) Heavy products
Summary

1 Characteristics Evaporation conditions Sub-classification types Applications Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
Table losses Operating Typical