AAAAAA

   
Results: 1-15 |
Results: 15

Authors: VUDDAGIRI SR EUBANK PT
Citation: Sr. Vuddagiri et Pt. Eubank, CONDENSATION OF MIXED VAPORS AND THERMODYNAMICS, AIChE journal, 44(11), 1998, pp. 2526-2541

Authors: SHYU GS HANIF NSM HALL KR EUBANK PT
Citation: Gs. Shyu et al., CARBON-DIOXIDE WATER PHASE-EQUILIBRIA RESULTS FROM THE WONG-SANDLER COMBINING RULES, Fluid phase equilibria, 130(1-2), 1997, pp. 73-85

Authors: GUPTA D EUBANK PT
Citation: D. Gupta et Pt. Eubank, DENSITY AND VIRIAL-COEFFICIENTS OF GASEOUS BUTANE FROM 265 TO 450-K AT PRESSURES TO 3.3 MPA, Journal of chemical and engineering data, 42(5), 1997, pp. 961-970

Authors: HANIF NSM SHYU GS HALL KR EUBANK PT
Citation: Nsm. Hanif et al., AREAS OF MAXWELL,J.C. FOR PURE-COMPONENT FLUID-PHASE EQUILIBRIA FROM EQUATIONS OF STATE, Industrial & engineering chemistry research, 35(7), 1996, pp. 2431-2437

Authors: SHYU GS HANIF NSM HALL KR EUBANK PT
Citation: Gs. Shyu et al., MAXIMUM PARTIAL AREA RULE FOR PHASE-EQUILIBRIUM CALCULATIONS, Industrial & engineering chemistry research, 35(11), 1996, pp. 4348-4353

Authors: HANIF NSM SHYU GS HALL KR EUBANK PT
Citation: Nsm. Hanif et al., CALCULATION OF MULTIPHASE EQUILIBRIA USING THE EQUAL-AREA RULE WITH APPLICATION TO HYDROCARBON WATER MIXTURES/, Fluid phase equilibria, 126(1), 1996, pp. 53-70

Authors: ALVARADO JJF EUBANK PT
Citation: Jjf. Alvarado et Pt. Eubank, REEXAMINATION OF COLLINEARITY TESTS FOR DENSITY-DEPENDENT MIXING RULE, Fluid phase equilibria, 122(1-2), 1996, pp. 255-263

Authors: ARUNACHALAM C BOZKURT B EUBANK PT
Citation: C. Arunachalam et al., EQUILIBRIUM THERMOPHYSICAL PROPERTIES OF ALKANES AT VERY HIGH-TEMPERATURES, Journal of chemical and engineering data, 41(1), 1996, pp. 121-127

Authors: SHYU GS HANIF NSM ALVARADO JFJ HALL KR EUBANK PT
Citation: Gs. Shyu et al., EQUAL-AREA RULE METHODS FOR TERNARY-SYSTEMS, Industrial & engineering chemistry research, 34(12), 1995, pp. 4562-4570

Authors: EUBANK PT SHYU GS HANIF NSM
Citation: Pt. Eubank et al., NEW PROCEDURES FOR APPLICATION OF THE WONG-SANDLER MIXING RULES TO THE PREDICTION OF VAPOR-LIQUID-EQUILIBRIA, Industrial & engineering chemistry research, 34(1), 1995, pp. 314-323

Authors: WAROWNY W EUBANK PT
Citation: W. Warowny et Pt. Eubank, GENERALIZED EQUATIONS OF THE BURNETT P-V-T METHODS FOR ADSORBING GASES, Fluid phase equilibria, 103(1), 1995, pp. 77-95

Authors: EUBANK PT HALL KR
Citation: Pt. Eubank et Kr. Hall, EQUAL-AREA RULE AND ALGORITHM FOR DETERMINING PHASE COMPOSITIONS, AIChE journal, 41(4), 1995, pp. 924-927

Authors: EUBANK PT WU CH ALVARADO JFJ FORERO A BELADI MK
Citation: Pt. Eubank et al., MEASUREMENT AND PREDICTION OF 3-PHASE WATER HYDROCARBON EQUILIBRIA/, Fluid phase equilibria, 102(2), 1994, pp. 181-203

Authors: EUBANK PT VANPEURSEM D CHAO YP GUPTA D
Citation: Pt. Eubank et al., RANDOM AND SYSTEMATIC-ERRORS IN THERMOPHYSICAL PROPERTY MEASUREMENTS, AIChE journal, 40(9), 1994, pp. 1580-1593

Authors: EUBANK PT PATEL MR BARRUFET MA BOZKURT B
Citation: Pt. Eubank et al., THEORETICAL-MODELS OF THE ELECTRICAL-DISCHARGE MACHINING PROCESS .3. THE VARIABLE MASS, CYLINDRICAL PLASMA MODEL, Journal of applied physics, 73(11), 1993, pp. 7900-7909
Risultati: 1-15 |