학술논문

Charts give vapor loss from internal floating-roof tanks
Document Type
Journal Article
Author
Source
Oil Gas J.; (United States); 85:10
Subject
02 PETROLEUM FLOATING ROOF TANKS
LOSSES
PETROLEUM
EVAPORATION
STORAGE
BOLTED JOINTS
ECONOMIC ANALYSIS
LOW PRESSURE
NOMOGRAMS
PETROCHEMICAL PLANTS
PETROLEUM REFINERIES
SEALS
SIZE
SUPPORTS
TERMINAL FACILITIES
VAPOR PRESSURE
VAPORS
WELDED JOINTS
CHEMICAL PLANTS
CONTAINERS
DIAGRAMS
ECONOMICS
ENERGY SOURCES
FLUIDS
FOSSIL FUELS
FUELS
GASES
INDUSTRIAL PLANTS
JOINTS
MECHANICAL STRUCTURES
PHASE TRANSFORMATIONS
PHYSICAL PROPERTIES
TANKS
THERMODYNAMIC PROPERTIES 024000* -- Petroleum-- Storage-- (-1989)
Language
English
Abstract
Nomographs have been constructed to estimate the average evaporation loss from internal floating-roof tanks. Loss determined from the charts can be used to evaluate the economics of seal conversion and to reconcile refinery, petrochemical plant, and storage terminal losses. The losses represent average standing losses only. They do not cover losses associated with the movement of product into or out of the tank. The average standing evaporation loss from an internal floating-roof tank depends on: vapor pressure of the product; type and condition of roof seal; tank diameter; and type of fixed roof support. The nomographs can estimate evaporation loss for product true vapor pressures (TVP) ranging from 1.5 to 14 psia, the most commonly used seals for average and tight fit conditions, tank diameters ranging from 50 to 250 ft, welded and bolted designs, and both self-supporting and column-support fixed roof designs. The charts are purposely limited to tank diameters 250 ft and less because internal floating-roof tanks are generally below this diameter.