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ORCIDWilliam L. Luyben
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2020 – today
- 2024
[j22]William L. Luyben:
Dynamic simulation and control of dual-evaporator compression refrigeration systems. Comput. Chem. Eng. 185: 108661 (2024)- 2023
- [j21]William L. Luyben:
Reality versus simulation-implementation of heat exchangers with phase changes. Comput. Chem. Eng. 175: 108284 (2023) - 2021
- [j20]Shawn Henry, Jonas Baltrusaitis
, William L. Luyben:
Dynamic simulation and control of a combustion turbine process for biogas derived methane. Comput. Chem. Eng. 144: 107121 (2021) - [j19]William L. Luyben:
Importance of pressure-selection in pressure-swing distillation. Comput. Chem. Eng. 149: 107279 (2021) - 2020
- [j18]William L. Luyben:
Design and control of distillation columns with inert venting. Comput. Chem. Eng. 134: 106725 (2020) - [j17]William L. Luyben:
Importance of heat-transfer area in the controllability of openloop unstable reactors. Comput. Chem. Eng. 135: 106715 (2020)
2010 – 2019
- 2019
- [j16]William L. Luyben:
High-pressure versus low-pressure auxiliary condensers in distillation vapor recompression. Comput. Chem. Eng. 125: 427-433 (2019) - [j15]William L. Luyben:
Refrigerant selection for different cryogenic temperatures. Comput. Chem. Eng. 126: 241-248 (2019) - [j14]William L. Luyben:
Simplified plantwide control structure for the diethyl oxalate process. Comput. Chem. Eng. 126: 451-464 (2019) - 2018
- [j13]William L. Luyben:
Control of Heat-Integrated Extractive Distillation Processes. Comput. Chem. Eng. 111 (2018) - [j12]William L. Luyben:
Comparison of flowsheets for THF/water separation using pressure-swing distillation. Comput. Chem. Eng. 115: 407-411 (2018) - [j11]William L. Luyben:
Effect of feed composition on cryogenic distillation precooling configurations. Comput. Chem. Eng. 118: 261-267 (2018) - 2017
- [j10]William L. Luyben:
Estimating refrigeration costs at cryogenic temperatures. Comput. Chem. Eng. 103: 144-150 (2017) - [j9]William L. Luyben:
Improving the conventional reactor/separation/recycle DME process. Comput. Chem. Eng. 106: 17-22 (2017) - 2016
- [j8]William L. Luyben:
Economic trade-offs in acrylic acid reactor design. Comput. Chem. Eng. 93: 118-127 (2016) - 2014
- [j7]William L. Luyben:
Heat exchanger simulations involving phase changes. Comput. Chem. Eng. 67: 133-136 (2014) - 2013
- [j6]William L. Luyben:
Comparison of extractive distillation and pressure-swing distillation for acetone/chloroform separation. Comput. Chem. Eng. 50: 1-7 (2013) - 2012
- [j5]William L. Luyben:
Catalyst dilution to improve dynamic controllability of cooled tubular reactors. Comput. Chem. Eng. 37: 184-190 (2012) - [j4]William L. Luyben:
Use of dynamic simulation for reactor safety analysis. Comput. Chem. Eng. 40: 97-109 (2012) - [j3]William L. Luyben:
Rigorous dynamic models for distillation safety analysis. Comput. Chem. Eng. 40: 110-116 (2012)
2000 – 2009
- 2008
- [j2]Devrim B. Kaymak, William L. Luyben:
Quantitative comparison of dynamic controllability between a reactive distillation column and a conventional multi-unit process. Comput. Chem. Eng. 32(7): 1456-1470 (2008) - 2003
- [j1]Kwo-Liang Wu, Cheng-Ching Yu, William L. Luyben, Sigurd Skogestad:
Reactor/separator processes with recycles-2. Design for composition control. Comput. Chem. Eng. 27(3): 401-421 (2003)
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