Josh Kanter is from Barrington, Rhode Island. He received his B.S Degree
in chemical engineering from Lehigh University in 1996 and his M.S. Degree
in chemical engineering from the University of Pennsylvania in December,
1997. His research interests include the development of nonlinear
model-based controllers for processes with a non-minimum-phase, delay-free
part.
PRESENTATIONS
Soroush, M., W. D. Seider, and J. M. Kanter, “Model-based Control of Non-minimum-phase Nonlinear Processes,” AIChE 1999 Annual Meeting, Dallas, Texas, November, 1999.
Kanter, J. M., M. Soroush, and W. D. Seider, “Nonlinear Feedback Control of Multivariable Non-minimum-phase Processes,” AIChE 2000 Annual Meeting, Los Angeles, California, November, 2000.
Kanter, J. M., M. Soroush, and W. D. Seider, “Continuous-time Nonlinear
Control of Stable Non-minimum-phase
Processes,” IFAC 2000, Pisa, Italy, June, 2000.
Kanter, J. M., M. Soroush, and W. D. Seider, “Feedback Control of Stable,
Non-minimum-phase, Nonlinear Processes,” Chemical Process Control VI, Poster,
Tuscon, Arizona, January, 2001.
PUBLICATIONS
Kanter, J. M., M. Soroush, and W. D. Seider, "Continuous-time, Nonlinear Control of Stable Non-Minimum-Phase Processes," IFAC-ADCHEM, Pisa, Italy, 407-412 (2000).
Kanter, J. M., M. Soroush, and W. D. Seider, “Continuous-time, Nonlinear Feedback Control of Stable Processes,” Ind. Eng. Chem. Res., 40, 2069-2078 (2001).
Kanter, J. M., M. Soroush, and W. D. Seider. “Nonlinear Feedback Control of Stable Constrained Processes,” ACC Proceedings, in press. .
Kanter, J. M., M. Soroush, and W. D. Seider. “Feedback Control of Stable, Non-minimum-phase, Nonlinear Processes,” CPC 6 Proceedings, in press.
Kanter, J. M., M. Soroush, and W. D. Seider. “Nonlinear Feedback Control of Multivariable Non-minimum-phase Processes,” submitted to J. Process Control.
Kanter, J. M., M. Soroush, and W. D. Seider. “Nonlinear Feedback Control of Stable Constrained Processes,” submitted to Ind. Eng. Chem. Res.
Kanter, J. M., M. Soroush, and W. D. Seider. “Nonlinear Model-based
Control of Constrained, Non-minimum-phase Processes with Real-time Application
to a Four Tank System,” in preparation.