Year |
Citation |
Score |
2009 |
Betts CL, Karra S, Karim MN, Riggs JB. A Modified Extended Recursive Least-Squares Method for Closed-Loop Identification of FIR Models Industrial & Engineering Chemistry Research. 48: 6327-6338. DOI: 10.1021/Ie800922W |
0.404 |
|
2008 |
Dong H, Riggs JB. Detection of Unmeasured Disturbances in Model Predictive Control (MPC) Plant Test Data Industrial & Engineering Chemistry Research. 47: 332-343. DOI: 10.1021/Ie061623+ |
0.333 |
|
2007 |
and DDS, Riggs JB. The Inside-Out Approach to Refinery-Wide Optimization Industrial & Engineering Chemistry Research. 46: 4645-4653. DOI: 10.1021/Ie0608814 |
0.323 |
|
2007 |
Govindhakannan J, Riggs JB. On the Construction of a Continuous Concentration−Reactivity Function for the Continuum Lumping Approach Industrial & Engineering Chemistry Research. 46: 1653-1656. DOI: 10.1021/Ie0607191 |
0.633 |
|
2006 |
Enagandula S, Riggs JB. Distillation control configuration selection based on product variability prediction Control Engineering Practice. 14: 743-755. DOI: 10.1016/J.Conengprac.2005.03.011 |
0.342 |
|
2004 |
Slaback DD, Riggs JB. Time to Runaway in a Continuous Stirred Tank Reactor Industrial & Engineering Chemistry Research. 43: 3723-3730. DOI: 10.1021/Ie0306574 |
0.572 |
|
2004 |
Han I, Riggs JB, Chung C. Modeling and optimization of a fluidized catalytic cracking process under full and partial combustion modes Chemical Engineering and Processing. 43: 1063-1084. DOI: 10.1016/J.Cep.2003.10.007 |
0.328 |
|
2003 |
Gudekar KG, Riggs JB. Bifurcation and Stability Analysis of an Ethylene Oxide Reactor System Industrial & Engineering Chemistry Research. 42: 3285-3293. DOI: 10.1021/Ie020874P |
0.593 |
|
2002 |
Han I, Riggs JB, Chung C. Multivariable Control of a Fluidized Catalytic Cracking Process under Full and Partial Combustion Modes Journal of Chemical Engineering of Japan. 35: 830-839. DOI: 10.1252/Jcej.35.830 |
0.354 |
|
2002 |
Huang H, Riggs JB. Including Levels in MPC to Improve Distillation Control Industrial & Engineering Chemistry Research. 41: 4048-4053. DOI: 10.1021/Ie0005396 |
0.524 |
|
2002 |
Huang H, Riggs JB. Comparison of PI and MPC for control of a gas recovery unit Journal of Process Control. 12: 163-173. DOI: 10.1016/S0959-1524(01)00004-X |
0.553 |
|
2001 |
Han I, Chungz C, Riggs JB. Development of an optimization procedure for a fluidized catalytic cracking process Ifac Proceedings Volumes. 34: 523-528. DOI: 10.1016/S1474-6670(17)33877-6 |
0.325 |
|
2001 |
Duvall M, Riggs JB, Lee P. Multi-model decoupled Generic Model Control Control Engineering Practice. 9: 471-481. DOI: 10.1016/S0967-0661(01)00007-7 |
0.366 |
|
2000 |
Hurowitz SE, Bobkov aA, Riggs JB. pH Control Using Advanced Proportional−Integral Controls with the Dual-Injection In-Line Process Industrial & Engineering Chemistry Research. 39: 2418-2426. DOI: 10.1021/Ie980776X |
0.34 |
|
2000 |
Huang H, Riggs JB. On Applying MPC for 4x4 Distillation Control Ifac Proceedings Volumes. 33: 503-508. DOI: 10.1016/S1474-6670(17)38590-7 |
0.497 |
|
2000 |
Duvall PM, Riggs JB. On-line optimization of the Tennessee Eastman challenge problem Journal of Process Control. 10: 19-33. DOI: 10.1016/S0959-1524(99)00041-4 |
0.339 |
|
2000 |
Han I, Chung C, Riggs JB. Modeling of a fluidized catalytic cracking process Computers & Chemical Engineering. 24: 1681-1687. DOI: 10.1016/S0098-1354(00)00453-1 |
0.388 |
|
1998 |
Rangaratnam B, Riggs JB. A Novel Hammerstein Model Applied for High Purity Distillation Control Ifac Proceedings Volumes. 31: 467-470. DOI: 10.1016/S1474-6670(17)44970-6 |
0.395 |
|
1998 |
Anderson JJ, Riggs JB. A SISO Test Function for Evaluating the Effect of Steady-State and Dynamic Nonlinearity on Controller Performance Ifac Proceedings Volumes. 31: 165-168. DOI: 10.1016/S1474-6670(17)44923-8 |
0.373 |
|
1998 |
Ellis RC, Li X, Riggs JB. Modeling and Optimization of a Model IV Fluidized Catalytic Cracking Unit Aiche Journal. 44: 2068-2079. DOI: 10.1002/Aic.690440914 |
0.335 |
|
1997 |
Taskar U, Riggs JB. Modeling and optimization of a semiregenerative catalytic naphtha reformer Aiche Journal. 43: 740-753. DOI: 10.1002/Aic.690430319 |
0.412 |
|
1996 |
Flathouse SE, Riggs JB. Tuning GMC controllers using the ATV procedure Computers & Chemical Engineering. 20: 979-988. DOI: 10.1016/0098-1354(95)00213-8 |
0.348 |
|
1995 |
Gokhale V, Hurowitz S, Riggs JB. A Comparison of Advanced Distillation Control Techniques for a Propylene/Propane Splitter Industrial & Engineering Chemistry Research. 34: 4413-4419. DOI: 10.1021/Ie00039A033 |
0.373 |
|
1995 |
Gokhale V, Hurowitz SE, Riggs JB. A Dynamic Model of a Superfractionator: A Test Case for Comparing Distillation Control Techniques Ifac Proceedings Volumes. 28: 311-316. DOI: 10.1016/S1474-6670(17)47055-8 |
0.402 |
|
1995 |
Khandalekar PD, Riggs JB. Nonlinear process model based control and optimization of a model IV FCC unit Computers & Chemical Engineering. 19: 1153-1168. DOI: 10.1016/0098-1354(94)00110-3 |
0.465 |
|
1995 |
Kanadibhotla RS, Riggs JB. Nonlinear model based control of a recycle reactor process Computers & Chemical Engineering. 19: 933-948. DOI: 10.1016/0098-1354(94)00088-6 |
0.431 |
|
1995 |
Riggs JB, Curtner K, Foslien W. Comparison of two advanced steam temperature controllers for coal-fired boilers Computers & Chemical Engineering. 19: 541-550. DOI: 10.1016/0098-1354(94)00070-0 |
0.389 |
|
1995 |
Chung C, Riggs JB. Dynamic simulation and nonlinear-model-based product quality control of a crude tower Aiche Journal. 41: 122-134. DOI: 10.1002/Aic.690410112 |
0.402 |
|
1994 |
Gokhale V, Munsif H, Riggs JB. Comparison of Advanced Distillation Control Techniques Ifac Proceedings Volumes. 27: 351-356. DOI: 10.1016/S1474-6670(17)48176-6 |
0.363 |
|
1994 |
Riggs JB, Beauford MH, Watts JC. Model-based control using mechanistic, nonlinear models Isa Transactions. 33: 141-146. DOI: 10.1016/0019-0578(94)90045-0 |
0.394 |
|
1993 |
Mahuli SK, Rhinehart RR, Riggs JB. pH Control using a statistical technique for continuous on-line model adaptation Computers and Chemical Engineering. 17: 309-317. DOI: 10.1016/0098-1354(93)80023-G |
0.321 |
|
1993 |
Mahuli SK, Rhinehart RR, Riggs JB. Nonlinear model-based in-line control of wastewater pH: A laboratory study Isa Transactions. 32: 241-245. DOI: 10.1016/0019-0578(93)90024-Q |
0.365 |
|
1992 |
Ramchandran B, Riggs JB, Heichelheim HR. Nonlinear plant-wide control: application to a supercritical fluid extraction process Industrial & Engineering Chemistry Research. 31: 290-300. DOI: 10.1021/Ie00001A040 |
0.381 |
|
1992 |
Ramchandran B, Riggs JB, Heichelheim HR, Seibert AF, Fair JR. Dynamic simulation of a supercritical fluid extraction process Industrial & Engineering Chemistry Research. 31: 281-290. DOI: 10.1021/Ie00001A039 |
0.328 |
|
1992 |
Mahuli SK, Russell Rhinehart R, Riggs JB. Experimental demonstration of non-linear model-based in-line control of pH Journal of Process Control. 2: 145-153. DOI: 10.1016/0959-1524(92)85004-G |
0.341 |
|
1991 |
Rhinehart RR, Riggs JB. Two simple methods for on-line incremental model parameterization Computers and Chemical Engineering. 15: 181-189. DOI: 10.1016/0098-1354(91)85004-E |
0.318 |
|
1990 |
Riggs JB. Nonlinear process model based control of a propylene sidestream draw column Industrial & Engineering Chemistry Research. 29: 2221-2226. DOI: 10.1021/Ie00107A006 |
0.417 |
|
1990 |
Williams GL, Rhinehart RR, Riggs JB. In-line process-model-based control of wastewater pH using dual base injection Industrial & Engineering Chemistry Research. 29: 1254-1259. DOI: 10.1021/Ie00103A026 |
0.338 |
|
1990 |
Riggs JB, Rhinehart RR. Comparison between two nonlinear process-model based controllers Computers and Chemical Engineering. 14: 1075-1081. DOI: 10.1016/0098-1354(90)85004-T |
0.376 |
|
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