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From: LARRY SHEPHERD To: Steve sasson Date 6!30199 Time: a:17:04 AM Page 6 of 25 <br />must be certified to operate. the equipment that they are <br />operating, <br />S. 1.2 FirclExplosion Hazards <br />The station will be shut clown during the operation. All <br />tanks will be gashed and LF'L levels hrought to below 10% <br />before removing, <br />Explosion- the I.LI, levels must be at 10°,0 or tower to remove <br />the tanks. These are NIOSH and OSHA standards that are set <br />for the chcn-ical BIrNZFNE, TOLUENE F,THYLBEI' ZENE <br />vapors that ma}r be present during the operation. <br />S 1.3 Electrical Hazards <br />There will he no electrical tools being used during this <br />Operation. All tools will be air operated. All other fueling <br />PAPS 'Will be shut down during the operation. All electrical to <br />the tanks Ivill he disconnected from the breaker box during the <br />tank removals. <br />5.1.5 Noise Hazards <br />'I'liere will be car protecticm being used (hiring the operation of <br />the Uquipment. <br />S 2 C`hein al ffazards <br />Due to the nature of the site, the primary chemical hazards of been <br />identified as follows <br />a. Volatile Aromatic Hydrocarbons (benzene, toluene, <br />ehthylbenzene, xylene) <br />b. Rinseate solutions (for cleaning tanks) <br />c_ Various adhesives (for patching the fiberglass tank) if <br />needed <br />All employees who will possibly coMe into contact with <br />the chemicals shall wear the appropriate PPE. <br />5.2 1 ('"ladle Aromatic JHydrocarhQas <br />