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Book - School of Science and Technology

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Liquid fuel 301Table 11.4 Properties <strong>of</strong> fuel oilsGrade <strong>of</strong> oilDescriptionC2KeroseneDGas oilELightFMediumGHeavySpecific mass (re water) 0.789 0.834 0.929 0.949 0.969Flash point (closed) ( C) 38 55 66 66 66Viscosity at 38 CRedwood No 1 28 34 250 1000 3500kinematic (cSt) 1 to 2 4 62 247 864Pour point ( C) ± 18 7 21 21Calorific value (MJ/kg)gross 46.4 45.5 43.4 42.9 42.5net 43.6 42.7 41.0 40.5 40.0Impurities (% mass)sulphur 0.2 0.75 3.2 3.5 3.5ash ± 0.01 0.05 0.12 0.2Temperature ( C)storage (minimum) Atmospheric 10 25 35h<strong>and</strong>ling (minimum) Atmospheric 10 30 45upon the amount <strong>of</strong> low boiling-point material which may be incorporated in the oil, itis not very significant from the point <strong>of</strong> view <strong>of</strong> combustion.Viscosity. This quantity, which is comprehensible when given as a Redwood number (secondstaken for a given quantity to flow through an orifice <strong>of</strong> given size), is important in so far asit affects the ability <strong>of</strong> oil to flow in delivery <strong>and</strong> from storage. It is usually determined via a`U'-tube viscometer. Values for kinematic viscosity are given in centistokes.Pour point. This generally follows viscosity <strong>and</strong> is the temperature at which the oil ceasesto run freely. For practical purposes, this must be below that <strong>of</strong> the normal temperature<strong>of</strong> a storage vessel.Sulphur content. Very significant as far as the potential for corrosion is concerned <strong>and</strong> isalso a determinant <strong>of</strong> statutory requirements for chimney height.Ash. Although present in small quantities, this has little significance.DeliveryExcept in the case <strong>of</strong> very large installations, oil delivery is made by road tanker. Thus,site facilities must be provided for tanker parking <strong>and</strong> the position <strong>of</strong> the fill terminal bewithin an agreed distance from the park. The fill terminal should be a st<strong>and</strong>ard 50, 65 or80 mm male gas thread, the size being determined by the length <strong>of</strong> the fill pipe <strong>and</strong> thegrade <strong>of</strong> oil. The thread should be suitable for hose coupling <strong>and</strong> fitted with a non-ferrouscap as protection. As may be seen from Table 11.4, the heavier grades <strong>of</strong> oil are deliveredalready heated <strong>and</strong> for such usage the fill pipe should be insulated <strong>and</strong> provided withelectrical trace heating.Where more than one tank exists, filling should preferably be through separate pipes,one per tank, although a single fill pipe <strong>and</strong> an arrangement <strong>of</strong> three-way cocks or valvesat the tanks may be used. Fill pipes should, where practicable, be laid to drain into the

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