☰

Ross Taylor - Publications

Affiliations: 
Clarkson University, Potsdam, NY, United States 
Area:
Chemical Engineering, Materials Science Engineering
Tree Info Similar researchers PubMed Report error

55 high-probability publications. We are testing a new system for linking publications to authors. You can help! If you notice any inaccuracies, please sign in and mark papers as correct or incorrect matches. If you identify any major omissions or other inaccuracies in the publication list, please let us know.

Year Citation  Score
2019 Zhou J, Kooijman HA, Taylor R. Parallel column model for Dividing Wall Column simulations Computers & Chemical Engineering. 125: 114-133. DOI: 10.1016/J.Compchemeng.2019.02.008  0.403
2019 Taylor R, Duss M. A Paper about the Slope of the Equilibrium Line Chemical Engineering Research & Design. 148: 429-439. DOI: 10.1016/J.Cherd.2019.05.060  0.35
2019 Zhou J, Kooijman HA, Taylor R. A rate-based equation-oriented parallel column model: Application to dividing wall columns Chemical Engineering Research & Design. 146: 48-59. DOI: 10.1016/J.Cherd.2019.03.034  0.427
2019 Duss M, Taylor R. A new simplified tray efficiency model with improved accuracy for sieve trays Chemical Engineering Research & Design. 146: 71-77. DOI: 10.1016/J.Cherd.2019.03.021  0.403
2018 Duss M, Taylor R. A New Tray Efficiency Model: How Simple May It Be? Chemical Engineering Transactions. 69: 691-696. DOI: 10.3303/Cet1869116  0.416
2018 Taylor R, Duss M. A Paper about the Slope of the Equilibrium Line Chemical Engineering Transactions. 69: 265-270. DOI: 10.3303/Cet1869045  0.353
2018 Zhou J, Kooijman H, Taylor R. A Rate-Based Equation-Oriented Parallel Column Model: Application to Dividing Wall Columns Chemical Engineering Transactions. 69: 247-252. DOI: 10.3303/Cet1869042  0.447
2009 Klamt A, Krooshof GJP, Taylor R. Comment on “Towards the development of theoretically correct liquid activity coefficient models” The Journal of Chemical Thermodynamics. 41: 1312-1313. DOI: 10.1016/J.Jct.2009.07.016  0.306
2008 Lucia A, Amale A, Taylor R. Distillation pinch points and more Computers & Chemical Engineering. 32: 1342-1364. DOI: 10.1016/J.Compchemeng.2007.06.019  0.307
2007 Taylor R. (Di)Still Modeling after All These Years: A View of the State of the Art Industrial & Engineering Chemistry Research. 46: 4349-4357. DOI: 10.1021/Ie061626M  0.352
2006 Lucia A, Amale A, Taylor R. Energy Efficient Hybrid Separation Processes Industrial & Engineering Chemistry Research. 45: 8319-8328. DOI: 10.1021/Ie060035T  0.335
2006 Taylor R, Miller A, Lucia A. Geometry of Separation Boundaries: Systems with Reaction Industrial & Engineering Chemistry Research. 45: 2777-2786. DOI: 10.1021/Ie0508740  0.309
2006 Lucia A, Taylor R. The geometry of separation boundaries: I. Basic theory and numerical support Aiche Journal. 52: 582-594. DOI: 10.1002/Aic.10668  0.359
2005 Baur R, Krishna R, Taylor R. Influence of mass transfer in distillation: Feasibility and design Aiche Journal. 51: 854-866. DOI: 10.1002/Aic.10328  0.347
2004 Higler A, Chande R, Taylor R, Baur R, Krishna R. Nonequilibrium modeling of three-phase distillation Computers & Chemical Engineering. 28: 2021-2036. DOI: 10.1016/J.Compchemeng.2004.04.008  0.401
2004 Taylor R, Baur R, Krishna R. Influence of mass transfer in distillation: Residue curves and total reflux Aiche Journal. 50: 3134-3148. DOI: 10.1002/Aic.10278  0.363
2003 Putnam R, Taylor R, Klamt A, Eckert F, Schiller M. Prediction of infinite dilution activity coefficients using COSMO-RS Industrial & Engineering Chemistry Research. 42: 3635-3641. DOI: 10.1021/Ie020974V  0.306
2003 Baur R, Taylor R, Krishna R. Bifurcation analysis for TAME synthesis in a reactive distillation column: comparison of pseudo-homogeneous and heterogeneous reaction kinetics models Chemical Engineering and Processing: Process Intensification. 42: 211-221. DOI: 10.1016/S0255-2701(02)00090-9  0.381
2002 Klamt A, Krooshof GJP, Taylor R. COSMOSPACE: Alternative to conventional activity‐coefficient models Aiche Journal. 48: 2332-2349. DOI: 10.1002/Aic.690481023  0.401
2001 Baur R, Taylor R, Krishna R. Influence of column hardware on the performance of reactive distillation columns Catalysis Today. 66: 225-232. DOI: 10.1016/S0920-5861(00)00653-2  0.331
2001 Baur R, Taylor R, Krishna R. Dynamic behaviour of reactive distillation columns described by a nonequilibrium stage model Chemical Engineering Science. 56: 2085-2102. DOI: 10.1016/S0009-2509(00)00496-6  0.445
2001 Baur R, Taylor R, Krishna R. Dynamic behaviour of reactive distillation tray columns described with a nonequilibrium cell model Chemical Engineering Science. 56: 1721-1729. DOI: 10.1016/S0009-2509(00)00401-2  0.442
2001 Baur R, Taylor R, Krishna R. Dynamics of a Reactive Distillation Column for TAME Synthesis Described by a Nonequilibrium Stage Model Chemie Ingenieur Technik. 73: 771-771. DOI: 10.1002/1522-2640(200106)73:6<771::Aid-Cite7712222>3.0.Co;2-G  0.349
2000 Higler A, Krishna R, Taylor R. Nonequilibrium Modeling of Reactive Distillation:  A Dusty Fluid Model for Heterogeneously Catalyzed Processes Industrial & Engineering Chemistry Research. 39: 1596-1607. DOI: 10.1021/Ie990547Q  0.397
2000 Baur R, Higler A, Taylor R, Krishna R. Comparison of equilibrium stage and nonequilibrium stage models for reactive distillation Chemical Engineering Journal. 76: 33-47. DOI: 10.1016/S1385-8947(99)00114-X  0.438
2000 Baur R, Taylor R, Krishna R. Development of a dynamic nonequilibrium cell model for reactive distillation tray columns Chemical Engineering Science. 55: 6139-6154. DOI: 10.1016/S0009-2509(00)00204-9  0.436
2000 Taylor R, Krishna R. Modelling reactive distillation Chemical Engineering Science. 55: 5183-5229. DOI: 10.1016/S0009-2509(00)00120-2  0.377
1999 Krishna R, Van Baten JM, Ellenberger J, Higler AP, Taylor R. CFD simulations of sieve tray hydrodynamics Chemical Engineering Research and Design. 77: 639-646. DOI: 10.1205/026387699526575  0.366
1999 Baur R, Taylor R, Krishna R, Copati J. Influence of Mass Transfer in Distillation of Mixtures with a Distillation Boundary Chemical Engineering Research and Design. 77: 561-565. DOI: 10.1205/026387699526467  0.374
1999 Higler A, Krishna R, Taylor R. Nonequilibrium Cell Model for Packed Distillation ColumnsThe Influence of Maldistribution Industrial & Engineering Chemistry Research. 38: 3988-3999. DOI: 10.1021/Ie990261L  0.39
1999 Higler A, Krishna R, Ellenberger J, Taylor R. Counter-current operation of a structured catalytically packed-bed reactor: Chemical Engineering Science. 54: 5145-5152. DOI: 10.1016/S0009-2509(99)00229-8  0.327
1999 Higler A, Taylor R, Krishna R. Nonequilibrium modelling of reactive distillation: Multiple steady states in MTBE synthesis Chemical Engineering Science. 54: 1389-1395. DOI: 10.1016/S0009-2509(99)00056-1  0.403
1999 Higler A, Taylor R, Krishna R. The influence of mass transfer and mixing on the performance of a tray column for reactive distillation Chemical Engineering Science. 54: 2873-2881. DOI: 10.1016/S0009-2509(98)00317-0  0.423
1999 Higler A, Krishna R, Taylor R. Nonequilibrium cell model for multicomponent (reactive) separation processes Aiche Journal. 45: 2357-2370. DOI: 10.1002/Aic.690451111  0.441
1998 Higler A, Taylor R, Krishna R. Modeling of a reactive separation process using a nonequilibrium stage model Computers & Chemical Engineering. 22: S111-S118. DOI: 10.1016/S0098-1354(98)00044-1  0.434
1996 Taylor R, Achuthan K, Lucia A. Complex domain distillation calculations Computers & Chemical Engineering. 20: 93-111. DOI: 10.1016/0098-1354(95)90883-R  0.319
1995 Kooijman HA, Taylor R. Modelling mass transfer in multicomponent distillation The Chemical Engineering Journal and the Biochemical Engineering Journal. 57: 177-188. DOI: 10.1016/0923-0467(94)02952-0  0.417
1995 Kooijman HA, Taylor R. A nonequilibrium model for dynamic simulation of tray distillation columns Aiche Journal. 41: 1852-1863. DOI: 10.1002/Aic.690410804  0.428
1994 Lao M, Taylor R. Modeling Mass Transfer in Three-Phase Distillation Industrial & Engineering Chemistry Research. 33: 2637-2650. DOI: 10.1021/Ie00035A015  0.413
1994 Agarwal S, Taylor R. Distillation Column Design Calculations Using a Nonequilibrium Model Industrial & Engineering Chemistry Research. 33: 2631-2636. DOI: 10.1021/Ie00035A014  0.372
1994 Taylor R, Kooijman HA, Hung J-. A second generation nonequilibrium model for computer simulation of multicomponent separation processes Computers & Chemical Engineering. 18: 205-217. DOI: 10.1016/0098-1354(94)85009-7  0.402
1992 Lucia A, Taylor R. Complex iterative solutions to process model equations Computers & Chemical Engineering. 16. DOI: 10.1016/S0098-1354(09)80046-X  0.334
1991 Taylor R, Kooijman HA. Composition Derivatives Of Activity Coefficient Models (For The Estimation Of Thermodynamic Factors In Diffusion) Chemical Engineering Communications. 102: 87-106. DOI: 10.1080/00986449108910851  0.327
1989 Lao M, Kingsley JP, Krtshnamiirthy R, Taylor R. A isionequilibrium stage model of multicomponent separation processes vi: Simulation of liquid-liquid extraction Chemical Engineering Communications. 86: 73-89. DOI: 10.1080/00986448908940364  0.407
1988 Powers MF, Vickeryt DJ, Arehole A, Taylor R. A nonequilibrium stage model of multicomponent separation processes—V. Computational methods for solving the model equations Computers & Chemical Engineering. 12: 1229-1241. DOI: 10.1016/0098-1354(88)85073-7  0.401
1988 Vickery DJ, Ferrari JJ, Taylor R. An efficient continuation method for the solution of difficult equilibrium stage separation process problems Computers & Chemical Engineering. 12: 99-103. DOI: 10.1016/0098-1354(88)85009-9  0.335
1987 Sivasubramanian MS, Taylor R, Krishnamurthy R. A nonequilibrium stage model of multicomponent separation processes part IV: A novel approach to packed column design Aiche Journal. 33: 325-327. DOI: 10.1002/Aic.690330223  0.334
1986 Taylor R, Krishnamurthy R, Furno JS, Krishna R. Condensation of vapor mixtures. 1. Nonequilibrium models and design procedures Industrial & Engineering Chemistry Process Design and Development. 25: 83-97. DOI: 10.1021/I200032A014  0.349
1986 Vickery DJ, Taylor R. Path-following approaches to the solution of multicomponent, multistage separation process problems Aiche Journal. 32: 547-556. DOI: 10.1002/Aic.690320404  0.338
1985 Krishnamurthy R, Taylor R. NONEQUILIBRIUM STAGE MODEL OF MULTICOMPONENT SEPARATION PROCESSES. PART II: COMPARISON WITH EXPERIMENT Aiche Journal. 31: 456-465. DOI: 10.1002/Aic.690311207  0.345
1985 Krishnamurthy R, Taylor R. NONEQUILIBRIUM STAGE MODEL OF MULTICOMPONENT SEPARATION PROCESSES. PART II: COMPARISON WITH EXPERIMENT Aiche Journal. 31: 456-465. DOI: 10.1002/Aic.690310313  0.345
1985 Krishnamurthy R, Taylor R. NONEQUILIBRIUM STAGE MODEL OF MULTICOMPONENT SEPARATION PROCESSES. PART I: MODEL DESCRIPTION AND METHOD OF SOLUTION Aiche Journal. 31: 449-456. DOI: 10.1002/Aic.690310312  0.433
1984 Taylor R. Simulation of binary vapor condensation in the presence of an inert gas - a sequel International Communications in Heat and Mass Transfer. 11: 429-437. DOI: 10.1016/0735-1933(84)90049-6  0.331
1982 Taylor R. Film models for multicomponent mass transfer: computational methods-II. The linearised theory Computers and Chemical Engineering. 6: 69-75. DOI: 10.1016/0098-1354(82)80008-2  0.342
1979 STANDART GL, TAYLOR R, KRISHNA R. THE MAXWELL-STEFAN FORMULATION OF IRREVERSIBLE THERMODYNAMICS FOR SIMULTANEOUS HEAT AND MASS TRANSFER Chemical Engineering Communications. 3: 277-289. DOI: 10.1080/00986447908935866  0.318
Show low-probability matches.