| A coupled DEM and CFD simulation of flow field and pressure drop in fixed bed reactor with randomly packed catalyst particles H Bai, J Theuerkauf, PA Gillis, PM Witt Industrial & Engineering Chemistry Research 48 (8), 4060-4074, 2009 | 238 | 2009 |
| Analysis of particle porosity distribution in fixed beds using the discrete element method J Theuerkauf, P Witt, D Schwesig Powder Technology 165 (2), 92-99, 2006 | 156 | 2006 |
| Effect of flow rate on the partial oxidation of methane and ethane PM Witt, LD Schmidt Journal of Catalysis 163 (2), 465-475, 1996 | 121 | 1996 |
| Control of H2 and CO produced in partial oxidation process LD Schmidt, PM Witt US Patent 6,254,807, 2001 | 71 | 2001 |
| Design and application of a low-temperature continuous flow chemistry platform JA Newby, DW Blaylock, PM Witt, JC Pastre, MK Zacharova, SV Ley, ... Organic Process Research & Development 18 (10), 1211-1220, 2014 | 59 | 2014 |
| Investigation of a Lithium–Halogen Exchange Flow Process for the Preparation of Boronates by Using a Cryo‐Flow Reactor JA Newby, L Huck, DW Blaylock, PM Witt, SV Ley, DL Browne Chemistry–A European Journal 20 (1), 263-271, 2014 | 48 | 2014 |
| Reconfiguration of a Continuous Flow Platform for Extended Operation: Application to a Cryogenic Fluorine-Directed ortho-Lithiation Reaction JA Newby, DW Blaylock, PM Witt, RM Turner, PL Heider, BH Harji, ... Organic Process Research & Development 18 (10), 1221-1228, 2014 | 38 | 2014 |
| Optimal Active Catalyst and Inert Distribution in Catalytic Packed Bed Reactors: ortho-Xylene Oxidation Y Nie, PM Witt, A Agarwal, LT Biegler Industrial & Engineering Chemistry Research 52 (44), 15311-15320, 2013 | 38 | 2013 |
| Methane coupling to acetylene over Pt-coated monoliths at millisecond contact times KL Hohn, PM Witt, MB Davis, LD Schmidt Catalysis letters 54, 113-118, 1998 | 36 | 1998 |
| Reactor runaway due to statistically driven axial activity variations in graded catalyst beds EM Calverley, PM Witt, JD Sweeney Chemical engineering science 80, 393-401, 2012 | 19 | 2012 |
| Non-adiabatic multitubular fixed-bed catalytic reactor model coupled with shell-side coolant CFD model EJ Hukkanen, MJ Rangitsch, PM Witt Industrial & Engineering Chemistry Research 52 (44), 15437-15446, 2013 | 17 | 2013 |
| Horizontal reactive distillation for multicomponent chiral resolution PH Au‐Yeung, SM Resnick, PM Witt, TC Frank, FA Donate, LA Robbins AIChE Journal 59 (7), 2603-2620, 2013 | 17 | 2013 |
| Partial oxidation of butane at microsecond contact times DA Goetsch, PM Witt, LD Schmidt | 16 | 1996 |
| Reactor runaway due to statistically driven axial activity variations in graded catalyst beds: Loading from pre-measured single tube aliquots EM Calverley, PM Witt, JD Sweeney Chemical engineering science 90, 170-178, 2013 | 12 | 2013 |
| Static and dynamic intensification of water–ethylene glycol separation using a dividing wall column L Yan, PM Witt, TF Edgar, M Baldea Industrial & Engineering Chemistry Research 60 (7), 3027-3037, 2021 | 11 | 2021 |
| Modeling mesoscale reactors for the production of fine chemicals PM Witt, S Somasi, I Khan, DW Blaylock, JA Newby, SV Ley Chemical Engineering Journal 278, 353-362, 2015 | 10 | 2015 |
| Kinetics of Direct Olefin Synthesis from Syngas over Mixed Beds of Zn–Zr Oxides and SAPO-34 JF DeWilde, CR Ho, J Conner, A Smith, AV Kirilin, A Malek, PM Witt Industrial & Engineering Chemistry Research 60 (39), 14166-14175, 2021 | 8 | 2021 |
| Parital oxidation of alkanes at short contact times DA Goetsch, PM Witt, LD Schmidt American Chemical Society, Washington, DC (United States), 1996 | 7 | 1996 |
| Fluidized‐bed reactor scale‐up: Reaction kinetics required. PM Witt, DA Hickman AIChE Journal 68 (9), 2022 | 4 | 2022 |
| Dynamic modeling to study reversible poisoning of a catalytic bed S Somasi, PM Witt, EM Calverley, DA Livingston, E Herceg Industrial & Engineering Chemistry Research 52 (44), 15330-15341, 2013 | 4 | 2013 |
