SOLVE BY T&E FOR VALUES OF V IN f = V/F xiF zi ( i 1) 1 OR 0 f( E REF i ,REF 1) 1 i i V ( i 1) 1 7 7 ) i K i P *i i KiĭEW POINT TEMPERATURE ( T & E) P AND yi ARE GIVEN, FIND T AND xiy i PSYS yi x i ! 1 ! K P * ! K (11.7 7 ) i i i i iįLASH CALCULATIONS PARTIAL FLASH zi = 1 P, T AND zi ARE GIVEN, FIND xi & yi FLASH LINES ARE DEVELOPED FOR EACH COMPONENT WITH A COMMON fx iF f 1 ! xi yi ! f fREF
7 5) y i ! 1 ! P SYS i iįLASH CALCULATIONS DEW POINT PRESSURE (DIRECT) T AND yi ARE GIVEN, FIND PSYS AND xiy i PSYS y x i ! 1 ! ! i (11. pdf#search=%22AIR %20SEPARATION%2 0EQUILIBRIA%22įLASH CALCULATIONS BUBBLE POINT PRESSURE (DIRECT) T AND xi ARE GIVEN, FIND yi AND PīUBBLE POINT TEMPERATURE (T & E) P AND xi ARE GIVEN, FIND yi AND TxiK i P *i ! K i x i (11.
METHODS TO OBTAIN Ki AIR SEPARATION PLANT DATA METHODS TO OBTAIN Ki DEPRIESTER CHARTS FOR HYDROCARBON SYSTEMS HIGH TEMPERATURE DATA PERRYS FIGURE 13-14, P. METHODS TO OBTAIN Ki DEPRIESTER CHARTS FOR HYDROCARBON SYSTEMS LOW TEMPERATURE DATA PERRYS FIGURE 13-14, P. METHODS TO OBTAIN Ki EMPIRICAL DATA SET UP EXPERIMENTS TO MEASURE y = y(x,P,T) FIT TO STANDARD CORRELATIONS DATA CAN BE BASED ON BINARY SETS SEE PERRY'S SECTION 13 FOR BINARY DATA GENERAL CORRELATIONS FOR SPECIFIC TYPES OF MIXTURES - UNIQUAC SINGLE STAGE FLASH USES TWO PHASE EQUILIBRIUM FLASH BUBBLE POINT DEW POINTĬAN BE TWO LIQUID PHASES USES RELATIVE VOLATILITYy i ! K ixi
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