Stripping Subsystem- Major Equipment, how it works, & Controlling (Shut down N/A) Flashcards
The _____________ receives hydrocarbon liquid streams from the Cold and the Hot Flash Drums in the Reaction Subsystem.
Product Stripper
The _____________ take suction from the bottom of the product stipper and transfer the oil to the reactor feed/product stripper bottoms exchanger.
Product stipper bottoms pumps
The ______________ cool the product stipper bottoms stream via heat exchange with ambient air.
The Product stripper bottoms air coolers
The _____________ is an air cooler that cools and partially condenses the product stripper overhead stream via heat exchange with ambient air.
Product stipper overhead condenser
The _____________ provides residence time for the cooled Product Stipper overhead stream to phase separate into hydrocarbon liquid, sour water, and off-gas.
Product Stipper Accumulator
The ____________ transfer the hydrocarbon liquid from the Product Stripper Accumulator to 586 Drips Tank in Refinery Utilities.
Product Stripper Overhead Liquid Pumps
The ____________ transfer sour water from the Product Stripper Accumulator to the Sour Water Stripper in SRC
Product Stripper Overhead Sour Water Pumps
The ____________ stores the corrosion inhibitor chemicals used in the Reaction and Stripping Subsystems.
Corrosion Inhibitor Tank
The Purpose fo the Stripping Subsystem is to Strip hydrogen sulfide (H2S0, ammonia (NH3), and other ___________ ___________ from the reactor effluent.
Light ends
The Stripping Medium used in the Product Stripper is _________ _________ _________.
125-psig steam
__________ is injected into the Product Stripper overhead stream.
Corrosion inhibitor
The Product Stripper overhead liquid is transferred to _________ __________ in Utilities.
586 Tank
The Product Stripper bottoms stream branches into two streams, with one stream routed directly to the FCCU and the other routed to the FCCU Feed Tank 594. Which one flows through the Product Stripper Bottoms Air Coolers?
The FCCU Feed Tank 594 Stream
The Potential effect of a low stripping steam rate to the Product Stripper is ineffective stripping action resuling in __________ and light ends remaining in the FCCU feed.
H2S
The potential effect of high Product Stripper bottoms release temperature (to Tank 594) is exceeding the _________ _________ of downstream equipment, possibly resulting in _________ _________.
Design temperature, equipment failure