Experimental study on static flash vaporization of aqueous ...
USE OF THE TAYLOR SERIES AS A CONVERGENCE TECHNIQUE FOR THE SOLUTION OF MULTICOMPONENT DEW POINT AND...
Transcript of USE OF THE TAYLOR SERIES AS A CONVERGENCE TECHNIQUE FOR THE SOLUTION OF MULTICOMPONENT DEW POINT AND...
USE OF THE TAYLOR SERIES AS ACONVERGENCE TECHNIQUE FORTHE SOLUTION OF MULTICOMPONENTDEW POINT AND FLASH VAPORIZATIONPROBLEMS
A THESIS
Condensed for publication
Submitted on the 25th day of January, 1962, to the Department of
Chemical Engineering of the Graduate School of Tulane University
in partial fulfillment of the requirements for the degree of Master
of Science by:
Jacob H. Lashover
Thesis Advisor: Dr. Raymond V. Bailey
FLASH VAPORIZATION CALCULATION USING DERIVATIVESSYSTEM IS MEOH, IPA, H2O AT 1 ATMFEED COMPOSITION IS 0.50, 0.15, 0.35 MOLE FRACTION OF MEOH, IPA, H2O, RESPECTIVELYFEED TEMPERATURE IS 78 CISOTHERMAL FLASH USING REDLICH-KISTER ACTIVITY COEFFICIENT MODEL AND ANTOINE VAPOR PRESSURE MODEL
(VL+VU)/2ITER. NO. VL VU V X MeOH X IPA X H2O ƩX ΔƩX
0 0 1 0.5 0.4 0.1 0.5 1 01 0 1 0.5 0.3709 0.1299 0.44 0.9408 0.05922 0.5 1 0.75 0.3138 0.1013 0.5343 0.9494 0.05063 0.75 1 0.875 0.2801 0.0781 0.616 0.9742 0.02584 0.875 1 0.9375 0.2599 0.06406 0.6733 0.9973 0.00275 0.9375 1 0.96875 0.2487 0.05662 0.7077 1.01303 -0.013036 0.9375 0.96875 0.953125 0.2543 0.06029 0.6901 1.0047 -0.00477 0.9375 0.953125 0.945313 0.2571 0.06215 0.6817 1.0009 -0.00098 0.9375 0.945313 0.941407 0.2584 0.0631 0.6775 0.9991 0.00099 0.941406 0.945313 0.94336 0.2579 0.06269 0.6794 1.000003 -3E-06
Y MEOH Y IPA Y H2O ƩY0.514535 0.15524 0.33022 0.999995
V
ITERATION NUMBER
0 1 2 3 4 5 6 7 8 9 100
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Column D