| SECTION ONE Equipment Desig 1: Fluid Flow, 2 Velocity head Piping pressure drop Equivalent length Recommended velocities Two phase flow Compzessible flow Sonic velocity Metering Control valves Safety relief valves 2: Heat Exchangers, 19 TEMA Selection guides Pressure drop shell and tube Temperature difference Shell diameter Shellside velocity maximum Nozzle velocity maximum Heat transfer coefficients Fouling resistances Metal resistances Vacuum condensers Air-cooled heat exchangers: lbrced vs induced draft Aipcooled heat exchangers: pressure drop air side Air-cooled heat exchangers: rough rating Air-cooled heat exchangers: temperature control Miscellaneous rules of thumb 3: Fractioootors, 49 Introduction Relative volatility Minimum reflux Minimum stages Actual reflux and actual theoretical stages Reflux to feed ratio Actual trays GrapbicaI methods Tray efficiency Diameter of bubble cap trays Diametel of sieve/valve trays (F factor) Diameter of sieve/valve trays (Smith) Diameter of sieve/valve trays (Lieberman) Diameter of ballast trays Diameter of fl acflonators general Control schemes Optimization techniques Reboilers Packed columns 4: Absorbers, 97 hatroduction Hydrocarbon absorber design Hydrocarbon absolbers, oplimization Inorganic type 5: Pumps, 104 Affinity laws Horsepower Efficiency Minimum Ilow General suction system Suction system NPSH available Suction system NPSH for studies Suction system NPSH wilh dissolved gas Larger bnpeller Construction materials SECTION TWO Process Design SECTION THREE Plant Design SECTION FOUR Operations Appendixes Index, 423 |
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