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Technical Manual - Section 3 (Safety Hazards)

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LUBRICANT, WAX, AND GREASE<br />

MANUFACTURING PROCESSES<br />

Lubricating oils and waxes are refined from the residual<br />

fractions of atmospheric and vacuum distillation. The primary<br />

objective of the various lubricating oil refinery processes is to<br />

remove asphalts, sulfonated aromatics, and paraffinic and<br />

isoparaffinic waxes from residual fractions. Reduced crude<br />

from the vacuum unit is deasphalted and combined with<br />

straight-run lubricating oil feedstock, preheated, and<br />

solvent-extracted (usually with phenol or furfural) to produce<br />

raffinate.<br />

WAX MANUFACTURING PROCESS<br />

Raffinate from the extraction unit contains a considerable<br />

amount of wax that must be removed by solvent extraction<br />

and crystallization. The raffinate is mixed with a solvent<br />

(propane) and precooled in heat exchangers. The<br />

crystallization temperature is attained by the evaporation of<br />

propane in the chiller and filter feed tanks. The wax is<br />

continuously removed by filters and cold solvent-washed to<br />

recover retained oil. The solvent is recovered from the oil by<br />

flashing and steam stripping. The wax is then heated with hot<br />

solvent, chilled, filtered, and given a final wash to remove all<br />

oil.<br />

LUBRICATING OIL PROCESS<br />

The dewaxed raffinate is blended with other distillate<br />

fractions and further treated for viscosity index, color,<br />

stability, carbon residue, sulfur, additive response, and<br />

oxidation stability in extremely selective extraction processes<br />

using solvents (furfural,<br />

phenol, etc.). In a typical phenol unit, the raffinate is mixed<br />

with phenol in the treating section at temperatures below 400º<br />

F. Phenol is then separated from the treated oil and recycled.<br />

The treated lube-oil base stocks are then mixed and/or<br />

compounded with additives to meet the required physical and<br />

chemical characteristics of motor oils, industrial lubricants,<br />

and metal working oils.<br />

GREASE COMPOUNDING<br />

Grease is made by blending metallic soaps (salts of<br />

long-chained fatty acids) and additives into a lubricating oil<br />

medium at temperatures of 400-600º F. Grease may be either<br />

batch-produced or continuously compounded. The<br />

characteristics of the grease depend to a great extent on the<br />

metallic element (calcium, sodium, aluminum, lithium, etc.)<br />

in the soap and the additives used.<br />

SAFETY AND HEALTH CONSIDERATIONS<br />

Fire Protection and Prevention<br />

The potential for fire exists if a product or vapor leak or<br />

release in the lube blending and wax processing areas reaches<br />

a source of ignition. Storage of finished products, both bulk<br />

and packaged, should be in accordance with recognized<br />

practices.<br />

While the potential for fire is reduced in lube oil blending,<br />

care must be taken when making metal-working oils and<br />

compounding greases due to the use of higher blending and<br />

compounding temperatures and lower flash point products.<br />

Table III:2-22 LUBRICATING OIL AND WAX MANUFACTURING PROCESSES<br />

Feedstock From Process Typical products................To<br />

Lube Vacuum tower, solvent Treatment Dewaxed raffinate............. Lube blend or<br />

compound<br />

feedstock dewaxing, hydrotreating Grease compounding<br />

and solvent extraction, etc. Wax............................... Storage or shipping<br />

additives<br />

III:2-48

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