| Real-time optimization and nonlinear model predictive control of processes governed by differential-algebraic equations M Diehl, HG Bock, JP Schlöder, R Findeisen, Z Nagy, F Allgöwer Journal of Process Control 12 (4), 577-585, 2002 | 733 | 2002 |
| Nonlinear model predictive control: From theory to application F Allgower, R Findeisen, ZK Nagy Journal-Chinese Institute Of Chemical Engineers 35 (3), 299-316, 2004 | 368 | 2004 |
| Applying Kolb's experiential learning cycle for laboratory education M Abdulwahed, ZK Nagy Journal of engineering education 98 (3), 283-294, 2009 | 355 | 2009 |
| First-principles and direct design approaches for the control of pharmaceutical crystallization M Fujiwara, ZK Nagy, JW Chew, RD Braatz Journal of Process Control 15 (5), 493-504, 2005 | 339 | 2005 |
| Robust nonlinear model predictive control of batch processes ZK Nagy, RD Braatz AIChE Journal 49 (7), 1776-1786, 2003 | 302 | 2003 |
| Assessment of recent process analytical technology (PAT) trends: a multiauthor review LL Simon, H Pataki, G Marosi, F Meemken, K Hungerbühler, A Baiker, ... Organic Process Research & Development 19 (1), 3-62, 2015 | 252 | 2015 |
| Advances and new directions in crystallization control ZK Nagy, RD Braatz Annual review of chemical and biomolecular engineering 3, 55-75, 2012 | 241 | 2012 |
| Open-loop and closed-loop robust optimal control of batch processes using distributional and worst-case analysis ZK Nagy, RD Braatz Journal of process control 14 (4), 411-422, 2004 | 223 | 2004 |
| Recent advances in the monitoring, modelling and control of crystallization systems ZK Nagy, G Fevotte, H Kramer, LL Simon Chemical Engineering Research and Design 91 (10), 1903-1922, 2013 | 219 | 2013 |
| The impact of direct nucleation control on crystal size distribution in pharmaceutical crystallization processes MR Abu Bakar, ZK Nagy, AN Saleemi, CD Rielly Crystal Growth and Design 9 (3), 1378-1384, 2009 | 209 | 2009 |
| Distributional uncertainty analysis using power series and polynomial chaos expansions ZK Nagy, RD Braatz Journal of Process Control 17 (3), 229-240, 2007 | 176 | 2007 |
| Modelling and control of combined cooling and antisolvent crystallization processes ZK Nagy, M Fujiwara, RD Braatz Journal of Process Control 18 (9), 856-864, 2008 | 174 | 2008 |
| Comparative performance of concentration and temperature controlled batch crystallizations ZK Nagy, JW Chew, M Fujiwara, RD Braatz Journal of Process Control 18 (3-4), 399-407, 2008 | 174 | 2008 |
| Model based robust control approach for batch crystallization product design ZK Nagy Computers & Chemical Engineering 33 (10), 1685-1691, 2009 | 172 | 2009 |
| Model based control of a yeast fermentation bioreactor using optimally designed artificial neural networks ZK Nagy Chemical engineering journal 127 (1-3), 95-109, 2007 | 170 | 2007 |
| Modelling of mass transfer in gas–liquid stirred tanks agitated by Rushton turbine and CD-6 impeller: A scale-up study J Gimbun, CD Rielly, ZK Nagy Chemical Engineering Research and Design 87 (4), 437-451, 2009 | 135 | 2009 |
| Determination of the kinetic parameters for the crystallization of paracetamol from water using metastable zone width experiments ZK Nagy, M Fujiwara, XY Woo, RD Braatz Industrial & Engineering Chemistry Research 47 (4), 1245-1252, 2008 | 128 | 2008 |
| Model based control: case studies in process engineering PS Agachi, ZK Nagy, MV Cristea, Á Imre-Lucaci John Wiley & Sons, 2007 | 124 | 2007 |
| Evaluation study of an efficient output feedback nonlinear model predictive control for temperature tracking in an industrial batch reactor ZK Nagy, B Mahn, R Franke, F Allgöwer Control Engineering Practice 15 (7), 839-850, 2007 | 121* | 2007 |
| Worst-case and distributional robustness analysis of finite-time control trajectories for nonlinear distributed parameter systems ZK Nagy, RD Braatz IEEE Transactions on Control Systems Technology 11 (5), 694-704, 2003 | 114 | 2003 |
