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Technical Manual - Section 3 (Safety Hazards)

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Figure III:2-23 Molecular Sieve Drying and Sweetening<br />

HEALTH AND SAFETY CONSIDERATIONS<br />

Fire Protection and Prevention<br />

The potential exists for fire from a leak or release of feedstock<br />

or product. Sweetening processes use air or oxygen. If excess<br />

oxygen enters these processes, it is possible for a fire to occur<br />

in the settler due to the generation of static electricity, which<br />

acts as the ignition source.<br />

Health<br />

Because these are closed processes, exposures are expected<br />

to be minimal under normal operating conditions. There is a<br />

potential for exposure to hydrogen sulfide, caustic (sodium<br />

hydroxide), spent caustic, spent catalyst (Merox), catalyst<br />

dust and sweetening agents (sodium carbonate and sodium<br />

bicarbonate). Safe work practices and/or appropriate personal<br />

protective equipment may be needed for exposures to<br />

chemicals<br />

and other hazards such as noise and heat, and during process<br />

sampling, inspection, maintenance, and turnaround activities.<br />

UNSATURATED GAS PLANTS<br />

Unsaturated (unsat) gas plants recover light hydrocarbons (C 3<br />

and C 4 olefins) from wet gas streams from the FCC, TCC, and<br />

delayed coker overhead accumulators or fractionation<br />

receivers. In a typical unsat gas plant, the gases are<br />

compressed and treated with amine to remove hydrogen<br />

sulfide either before or after they are sent to a fractionating<br />

absorber where they are mixed into a concurrent flow of<br />

debutanized gasoline. The light fractions are separated by<br />

heat in a reboiler, the offgas is sent to a sponge absorber, and<br />

the bottoms are sent to a debutanizer. A portion of the<br />

debutanized hydrocarbon is recycled, with the balance sent to<br />

the splitter for separation. The overhead gases go to a<br />

depropanizer for use as alkylation unit feedstock.<br />

III:2-43

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