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United Arab Emirates University College of Engineering Industrial Training &Graduation Projects Unit . Aceton Production Plant Design. Presented By Eida AlMansouri 980724217 Rehab Alkaabi 199904156 Halima Abdullah 199902518. Outlines. Back ground Gp1.
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United Arab Emirates University College of Engineering Industrial Training &Graduation Projects Unit Aceton Production Plant Design Presented By Eida AlMansouri 980724217 Rehab Alkaabi 199904156 Halima Abdullah 199902518
Outlines • Back ground Gp1. • Process description (Base case). • Changes from base case process. • Process Simulation. • Material selection. • Equipment design . • Hazop study. • Safety • Cost & Economic Evaluation.
Back ground GP1 • Process selection • Material Balance Calculation. • Energy balance calculation.
Main Tasks In GP2 • Process modification. • Process simulation. • Hazard and operability study (HAZOP). • Cost and Project evaluation.
Dehydrogenation process simulation HYSYS Process flow diagram
Material selection Carbon steel
Main equipments design Feed vessel & Reflux drum Pumps design Heat exchanger design Reactor & molten salt heater Phase separator Absorber column design Distillation column design
Feed vessel & Reflux drum Result • The dimensions for the vessel and the reflux drum
Pump design Result • The dimensions for the pumps
Heat exchanger design Objective • Calculate heat-transfer area . • Calculate the number of tubes. • Estimate bundle diameter & Shell diameter. • Estimate the cost .
Heat exchanger design Result • The dimensions for the all heat exchangers
Reactor and molten salt heater design Fluidized Bed Reactor (FBR) Fluidized bed reactors are a catalytic reactors in which the catalyst is fluidized within the reactor.
Reactor design Diameter &Height Pressure drop Amount of Catalyst Diameter &Height
Reactor design Result • The dimensions for the Reactor
Absorber design Result • The dimensions for the absorber column
Distillation Column design Tray Distillation Column
Distillation Column design Objective • To Determine: • NAP (Number of Actual Plates). • Column diameter. • Column height.
Distillation Column design Result • The dimensions for the two distillation columns
Safety and Environmental Impact • Process is very safe one • No exotic equipment or safety practices • All streams are kept at relatively low • temperature and pressure.
Project Economic evaluation Cash flow diagram
Project Economic evaluation Acetone production plant design project cash flow diagram