Editorial pubs.acs.org/IECR
Jaime Cerdá Festschrift Preface: In Honor of Professor Jaime Cerdá His scientific and professional contributions in Process Systems Engineering are numerous and of great impact. These include planning and scheduling of batch and continuous processes, heat integration, synthesis of heat and power systems and distillation sequences, supply chain management, oil pipeline planning and scheduling, dynamic vehicle routing and pickup and delivery problems. After more than 30 years of strong dedication to R&D activities, Prof. Cerdá has authored more than 80 refereed publications, being the Argentine’s most recognized and highly cited scientist in the field of PSE. Furthermore, his former students or collaborators include Miguel Bagajewicz, Gabriela Henning, Miguel Isla, Aldo Vecchietti, Mariá Rosa Galli, Carlos Méndez, Rodolfo Dondo, Pablo Marchetti, Diego Cafaro, and Vanina Cafaro, all whom are active academic researchers in PSE. Professor Cerdá created and led, for more than 30 years, the INTEC Research Group on synthesis and optimization of industrial processes, which more recently became the Center for Advanced Process Systems Engineering (CAPSE, http:// www.intec.santafe-conicet.gov.ar/capse/). CAPSE currently has more than 15 researchers and Ph.D. students who have worked under his supervision. Professor Cerdá has given many seminars and courses abroad, holding positions as a Visiting Professor at Universidad de Valladolid (Spain), CarnegieMellon University (USA), Catholic University of the North (Chile), and Universidad de Barcelona (Spain). He has been a
We are very proud to present this Festschrift in honor of Professor Jaime Cerdá, in recognition to his outstanding research and academic career, as well as to his long-life contributions to the development of the Chemical and Process Systems Engineering (PSE) community in Argentina, and South America at large. Professor Cerdá has been a Full Professor at the Universidad Nacional del Litoral (UNL) in Santa Fe, and Superior Researcher at the Argentine National Scientific and Technical Research Council (CONICET) until his retirement in October 2012. Motivated by his passion for Process Systems Engineering, he still continues to be actively involved in research and other academic activities as a research fellow of CONICET. Professor Cerdá graduated with a B.S. degree in Chemical Engineering from Universidad Nacional del Litoral in 1967. He joined Universidad Nacional del Litoral (UNL) in 1968 as a Research Associate in the Institute of Technological Development for the Chemical Industry (INTEC). He was first appointed as a teaching assistant, and shortly thereafter was promoted to Assistant Professor. In 1976, he went to Pittsburgh, PA, where he worked under the direction of Professor Arthur Westerberg at Carnegie Mellon University in the area of process synthesis and heat integration. He received his M.S. degree in 1979 and his Ph.D. degree in 1980, both in Chemical Engineering. Next, he returned to UNL to teach undergraduate and graduate Chemical Engineering courses at the School of Chemical Engineering, and to supervise Ph.D. research projects at INTEC. Since 1990, Dr. Cerdá has been Full Professor at the Universidad Nacional del Litoral, and since 2007, he has been a CONICET Superior Resercher, the highest level of a CONICET fellow. © 2014 American Chemical Society
Special Issue: Jaime Cerdá Festschrift Received: October 1, 2014 Accepted: October 3, 2014 Published: November 5, 2014 16895
dx.doi.org/10.1021/ie503887k | Ind. Eng. Chem. Res. 2014, 53, 16895−16898
Industrial & Engineering Chemistry Research
■
LIST OF SELECTED PUBLICATIONS OF PROF. JAIME CERDÁ
member of the editorial board of Computers and Chemical Engineering, and Associate Editor of Brazilian Journal of Chemical Engineering. He has been actively involved in the organization of international conferences and meetings in Argentina and abroad, including the Second Pan-American workshop on Catalysis and Process Systems Engineering (Santa Fe, 1999), the Third Mercosur Congress on Process Systems Engineering (ENPROMER 2001, Santa Fe), and two meetings of the Pan American Advanced Studies Institute Program on Process Systems Engineering (PASI−PSE 2005, Iguazú, http://cepac.cheme.cmu.edu/pasi.htm; PASI−PSE 2008, Mar del Plata, http://cepac.cheme.cmu.edu/pasi2008/ index.htm). Professor Cerdá is the former Head of the Industrial Engineering Department in the School of Chemical Engineering at UNL (1999−2001/2004) and Vice Director of the Institute for the Technological Development of the Chemical Industry (INTEC) of Argentina (1988−1990). His teaching interests have included courses on Optimization, Production Management, and Process Design. He has also participated in several industrial projects, developing consulting activities on energy integration, debottlenecking of continuous processes, and planning and scheduling of manufacturing facilities for ́ major industrial firms, such as PASA Petroquimica Argentina, ́ ́ Yacimientos Petroliferos Fiscales (YPF), Petroquimica General Mosconi (PGM), ATANOR, PETROSUR, MONSANTO Argentina, ARCOR-Arroyito, ARCOR-Colonia Caroya, Establecimientos FRIAR S.A., and SOMISA. This special issue contains 27 papers. Many contributions are from researchers with whom Prof. Cerdá has collaborated, including his former Ph.D. students and researchers, who have greatly benefitted from his supervision, high standards, and novel ideas in PSE. We have attempted to have this special issue reflect some of the latest developments and research trends in PSE. The areas covered in the issue include, among others, planning and scheduling, supply chain management, vehicle routing problems, pipeline operation, energy, heat exchanger networks, process synthesis and design, separation processes, process optimization, and simulation. On behalf of all his colleagues and former students, it is an enormous privilege for us to dedicate this special issue of I&ECR in his honor. We wish Prof. Cerdá a happy retirement, good health, and many more years of prolific scientific contributions.
(1) Irazoqui, H. A.; Cerdá, J.; Cassano, A. E. Radiation profiles in an empty annular photoreactor with a source of finite spatial dimensions. AIChE J. 1973, 19, 460−469. (2) Cerdá, J.; Irazoqui, H. A.; Cassano, A. E. Radiation fields inside an elliptical photoreflector with source of finite spatial dimensions. AIChE J. 1973, 5, 963−968. (3) Irazoqui, H. A.; Cerdá, J.; Cassano, A. E. The radiation field for the point and line source approximations and the three-dimensional source models: Applications to photoreactions. Chem. Eng. J. 1976, 11, 27−37. (4) Cerdá, J.; Marchetti, J.; Cassano, A. E. Radiation efficiencies in elliptical photoreactors. Rev. Latinoam. Transferencia Calor Mater. 1977, 1, 33−63. (5) Cerdá, J.; Marchetti, J.; Cassano, A. E. The use of simple radiation models for the case of direct irradiation of photochemical reactors. Rev. Latinoam. Ing. Quim. Quim. Apl. 1978, 8, 15−25. (6) Cerdá, J.; Westerberg; A. W. Shortcut methods for complex distillation columns: Part IMinimum reflux. Ind. Eng. Chem. Process Des. Dev. 1981, 20, 546−557. (7) Cerdá, J.; Westerberg; A. W.; Mason, D.; Linnhoff, B. Minimum utility usage in heat exchanger network synthesis. A transportation problem. Chem. Eng. Sci. 1983, 38, 373− 387. (8) Cerdá, J.; Westerberg; A. W. Synthesizing heat exchanger networks having restricted stream/stream matches using transportation problem formulations. Chem. Eng. Sci. 1983, 38, 1723−1740. (9) Doldán, O. B.; Bagajewicz, M. J.; Cerdá, J. Optimal synthesis of heat and power generation and recovery systems. I. Optimal heating utility assignment. Rev. Latinoam. Transferencia Calor Mater. 1984, 8, 185−215. (10) Doldán, O. B.; Bagajewicz, M. J.; Cerdá, J. Optimal synthesis of heat and power generation and recovery systems. II. Maximum profitable heat recovery. Rev. Latinoam. Transferencia Calor Mater. 1985, 9, 21−48. (11) Doldán, O. B.; Bagajewicz, M. J.; Cerdá, J. Designing heat exchanger networks for existing chemical plants. Comput. Chem. Eng. 1985, 9, 483−498. (12) Isla, M. A.; Cerdá, J. Simultaneous synthesis of distillation trains and heat exchanger networks. Chem. Eng. Sci. 1987, 42, 2455−2463. (13) Isla, M. A.; Cerdá, J. A general algorithmic approach to the optimal synthesis of energy-efficient distillation train designs, Chem. Eng. Commun. 1987, 54, 353−379. (14) Isla, M. A.; Cerdá, J. A heuristic method for the synthesis of heat-integrated distillation systems. Chem. Eng. J. 1988, 38, 161−177. (15) Cerdá, J.; Vicente, M.; Gutiérrez, J.; Espulgas, S.; Mata, J. A new methodology for the optimal design and production schedule of multipurpose batch plants. Ind. Eng. Chem. Res. 1989, 28, 988−998. (16) Isla, M. A.; Irazoqui, H. A.; Cerdá, J. Optimizing sour water strippers through simulation. Hydrocarbon Process. 1989, 68, 65−66. (17) Cerdá, J.; Galli, M. R.; Camussi, N.; Isla, M. A. Synthesis of flexible heat exchanger networksI. Convex networks. Comput. Chem. Eng. 1990, 14, 197−211. (18) Cerdá, J.; Galli, M. R. Synthesis of flexible heat exchanger networks. II. Non-convex networks for large
Ignacio E. Grossmann* Carnegie Mellon University, Pittsburgh, Pennsylvania 15213, United States
Carlos A. Méndez*
■
Editorial
CAPSE/INTEC (UNL-CONICET), Santa Fe, Argentina
AUTHOR INFORMATION
Corresponding Authors
*E-mail:
[email protected]. *E-mail:
[email protected]. Notes
Views expressed in this editorial are those of the authors and not necessarily the views of the ACS. The authors declare no competing financial interest. 16896
dx.doi.org/10.1021/ie503887k | Ind. Eng. Chem. Res. 2014, 53, 16895−16898
Industrial & Engineering Chemistry Research
Editorial
continuous facilities. Comput. Chem. Eng. 2002, 26, 687− 695. (38) Méndez, C. A.; Cerdá, J. An MILP-based approach to the short-term scheduling of make-and-pack continuous production plants. OR Spectrum 2002, 24, 403−429. (39) Dondo, R.; Méndez, C. A.; Cerdá, J. An optimal approach to the multiple-depot heterogeneous vehicle routing problem with time window and capacity constraints. Lat. Am. Appl. Res. 2003, 33, 129−134. (40) Méndez, C. A.; Cerdá, J. A MILP continuous-time framework for short-term scheduling of multipurpose batch processes under different operation strategies. Optim. Eng. 2003, 4, 7−22. (41) Méndez, C. A.; Cerdá, J. Short-term scheduling of multistage batch processes subject to limited finite resources. In Computer-Aided Chemical Engineering, Vol. 15B; Chen, B., Westerberg, A. W., Eds.; Elsevier Science BV: Amsterdam, 2003; pp 984−989. (42) Méndez, C. A.; Cerdá, J. Dynamic scheduling in multiproduct batch plants. Comput. Chem. Eng. 2003, 27, 1247−1259. (43) Méndez, C. A.; Cerdá, J. An MILP-based approach to the short-term scheduling of make-and-pack continuous production plants. In Advanced Planning and Scheduling Solutions in Process Industry; Günther, H. O., van Beek, P., Eds.; Springer−Verlag: Berlin, Heidelberg, 2003; pp 295− 321. (44) Méndez, C. A.; Cerdá, J. An MILP framework for batch reactive scheduling with limited discrete resources. Comput. Chem. Eng. 2004, 28, 1059−1068. (45) Cafaro, D. C.; Cerdá, J. Optimal scheduling of multiproduct pipeline systems using a non-discrete MILP formulation. Comput. Chem. Eng. 2004, 28, 2053−2068. (46) Méndez, C. A.; Cerdá, J.; Grossmann, I.E.; Harjunkoski, I.; Fahl, M. State-of-the-art review of optimization methods for short-term scheduling of batch processes. Comput. Chem. Eng. 2006, 30, 913−946. (47) Dondo, R.; Cerdá, J. A Reactive MILP approach to the multidepot heterogeneous fleet vehicle routing problem with time windows, Int. Trans. Operational Res. 2006, 13, 441− 459. (48) Dondo, R.; Cerdá, J. A MILP framework for dynamic vehicle routing problems with time windows. Latin Am. Appl. Res. 2006, 36, 255−261. (49) Dondo, R.; Cerdá, J. A cluster-based optimization approach for the multi-depot heterogeneous fleet vehicle routing problem with time windows. Eur. J. Operational Res. 2007, 176, 1478−1507. (50) Méndez, C. A.; Cerdá, J. A precedence-based monolithic approach to lot-sizing and scheduling of multiproduct batch plants. Comput.-Aided Chem. Eng. 2007, 24, 679−684. (51) Cafaro, D. C.; Cerdá, J. Dynamic scheduling of multiproduct pipelines with multiple delivery due dates. Comput. Chem. Eng. 2008, 32, 728−753. (52) Dondo, R.; Méndez, C. A.; Cerdá, J. Optimal management of logistic activities in multi-site environments. Comput. Chem. Eng. 2008, 32, 2547−2569. (53) Cafaro, D. C.; Cerdá, J. Efficient tool for the scheduling of multiproduct pipelines and terminal operations. Ind. Eng. Chem. Res. 2008, 47, 9941−9956. (54) Marchetti, P. A.; Cerdá, J. A continuous-time tightened formulation for single-stage batch scheduling with
temperature variations. Comput. Chem. Eng. 1990, 14, 213− 225. (19) Cerdá, J.; Vicente, M.; Gutiérrez, J.; Espulgas, S.; Mata, J. Optimal production strategy and design of multiproduct batch plants. Ind. Eng. Chem. Res. 1990, 29, 590−600. (20) Galli, M. R.; Cerdá, J. Synthesis of flexible heat exchanger networks. III. Temperature and flowrate variations. Comput. Chem. Eng. 1991, 15, 7−24. (21) Benz, S.; Cerdá, J. Optimal Synthesis of Flexible HeatIntegrated Distillation Trains. Comput. Chem. Eng. 1992, 16, 753−776. (22) Henning, G. P.; Cerdá, J. An expert system for predictive and reactive scheduling of multiproduct batch plants. Lat. Am. Appl. Res. 1995, 25, 187−198. (23) Henning, G. P.; Cerdá, J. A knowledge-based approach to production scheduling for batch processes. Comput. Chem. Eng. 1996, 20, S1295−S1300. (24) Henning, G. P.; Cerdá, J.; Grossmann, I. E. A mixedinteger linear programming model for short-term scheduling of single-stage multiproduct batch plants with parallel lines. Ind. Eng. Chem. Res. 1997, 36, 1695−1707. (25) Galli, M. R.; Cerdá, J. Synthesis of structurallyconstrained heat exchanger networksI. Serial networks. Comput. Chem. Eng. 1998, 22, 819−839. (26) Galli, M. R.; Cerdá, J. Synthesis of structurallyconstrained heat exchanger networksII. Split networks. Comput. Chem. Eng. 1998, 22, 1017−1049. (27) Galli, M. R.; Cerdá, J. A user-controlled framework for the synthesis of heat exchanger networks involving nonisothermal mixers. Lat. Am. Appl. Res. 1998, 28, 57−62. (28) Galli, M. R.; Cerdá, J. A designer-controlled framework for the synthesis of heat exchanger networks involving nonisothermal mixers and multiple units over split streams. Comput. Chem. Eng. 1998, 22, S813−S816. (29) Galli, M. R.; Cerdá, J. A customized MILP approach to the synthesis of heat recovery networks reaching specified topology targets. Ind. Eng. Chem. Res. 1998, 37, 2479−2495. (30) Méndez, C. A.; Cerdá, J. Optimal scheduling of a resource-constrained multiproduct batch plant supplying intermediates to nearby end-product facilities. Comput. Chem. Eng. 2000, 24, 369−376. (31) Galli, M. R.; Cerdá, J. Synthesis of heat exchanger networks featuring a minimum number of constrained-size shells of 1-2 type. Appl. Therm. Eng. 2000, 20, 1443−1468. (32) Méndez, C. A.; Henning, G. P.; Cerdá, J. Optimal scheduling of batch plants satisfying multiple product orders with different due-dates. Comput. Chem. Eng. 2000, 24, 2223−2245. (33) Henning, G. P.; Cerdá, J. Knowledge-based predictive and reactive scheduling in industrial environments. Comput. Chem. Eng. 2000, 24, 2315−2338. (34) Méndez, C. A.; Henning, G. P.; Cerdá, J. An MILP continuous-time approach to short-term scheduling of resource-constrained multistage flowshop batch facilities. Comput. Chem. Eng. 2001, 25, 701−711. (35) Galli, M. R.; Cerdá, J. Retrofit of heat exchanger network with topology changes under designer control. Lat. Am. Appl. Res. 2001, 31, 247−254. (36) Méndez, C. A.; Henning, G. P.; Cerdá, J. Short-term scheduling of multiproduct batch plants under limited resource capacity. Lat. Am. Appl. Res. 2001, 31, 455−462. (37) Méndez, C. A.; Cerdá, J. An efficient MILP continuoustime formulation for short-term scheduling of multiproduct 16897
dx.doi.org/10.1021/ie503887k | Ind. Eng. Chem. Res. 2014, 53, 16895−16898
Industrial & Engineering Chemistry Research
Editorial
sequence-dependent changeovers. Ind. Eng. Chem. Res. 2009, 48, 483−498. (55) Marchetti, P. A.; Cerdá, J. A general resourceconstrained scheduling framework for multistage batch facilities with sequence-dependent changeovers. Comput. Chem. Eng. 2009, 33, 871−886. (56) Dondo, R.; Cerdá, J. A hybrid local improvement algorithm for large-scale multi-depot vehicle routing problems with time windows. Comput. Chem. Eng. 2009, 33, 513−530. (57) Marchetti, P. A.; Cerdá, J. An approximate mathematical framework for resource-constrained multistage batch scheduling, Chem. Eng. Sci. 2009, 64, 2733−2748. (58) Cafaro, D. C.; Cerdá, J. Short-term operational planning of multiple-source refined products pipelines. Comput.-Aided Chem. Eng. 2009, 26, 429−433. (59) Dondo, R.; Méndez, C. A.; Cerdá, J. The supply-chain pick-up and delivery problem with transshipments. Comput.Aided Chem. Eng. 2009, 26, 1009−1014. (60) Cafaro, D. C.; Cerdá, J. Optimal scheduling of refined products pipelines with multiple sources, Ind. Eng. Chem. Res. 2009, 48, 6675−6689. (61) Dondo, R.; Méndez, C. A.; Cerdá, J. Managing distribution in supply chain networks. Ind. Eng. Chem. Res. 2009, 48, 9961−9978. (62) Cafaro, D. C.; Cerdá, J. Operational scheduling of refined products pipeline networks with simultaneous batch injections. Comput. Chem. Eng. 2010, 34, 1687−1704. (63) Marchetti, P. A.; Méndez, C. A.; Cerdá, J. MILP monolithic formulations for lot-sizing and scheduling of single-stage batch facilities. Ind. Eng. Chem. Res. 2010, 49, 6482−6498. (64) Gleizes, M. F.; Herrero, G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. A discrete-event simulation tool for efficient operation of refined products pipelines. In Computer-Aided Chemical Engineering, Vol. 28; Pierucci, S., Buzzi Ferraris, G., Eds.; Elsevier Science BV: Amsterdam, 2010; pp 1697−1702. (65) Cafaro, D. C.; Cerdá, J. A rigorous mathematical formulation for the scheduling of tree-structure pipeline networks. Ind. Eng. Chem. Res. 2011, 50, 5064−5085. (66) Dondo, R.; Méndez, C. A.; Cerdá, J. The multi-echelon vehicle routing problem with cross docking in supply chain management. Comput. Chem. Eng. 2011, 35, 3002−3024. (67) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. Detailed scheduling of operations in singlesource refined products pipelines. Ind. Eng. Chem. Res. 2011, 50, 6240− 6259. (68) Gleizes, M. F.; Herrero, G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. Managing distribution in refined products pipelines using discrete-event simulation. Int. J. Inf. Syst. Supply Chain Manage. 2012, 5, 58−79. (69) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. New tools for the detailed scheduling of refined products pipelines. Comput.-Aided Chem. Eng. 2011, 29, 985−989. (70) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. Multiproduct operationsPart 1: Discrete-event simulation guides pipeline logistics. Oil Gas J. 2011, 109, 98−104. (71) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. Multiproduct operationsPart 2: New scheduling rule improves pipeline efficiency. Oil Gas J. 2011, 109, 136−139. (72) Cafaro, D. C.; Cerdá, J. Rigorous scheduling of meshstructure refined petroleum pipeline networks. Comput. Chem. Eng. 2012, 38, 185−203.
(73) Marchetti, P. A.; Méndez, C. A.; Cerdá, J. Simultaneous lot-sizing and scheduling of multistage batch processes handling multiple orders per product. Ind. Eng. Chem. Res. 2012, 51, 5762−5780. (74) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. Detailed scheduling of single-source pipelines with simultaneous deliveries to multiple offtake stations. Ind. Eng. Chem. Res. 2012, 51, 6145−6165. (75) Dondo, R.; Cerdá, J. A sweep-heuristic based formulation for the vehicle routing problem with cross docking. Comput. Chem. Eng. 2013, 48, 293−311. (76) Cafaro, D. C.; Cerdá, J. Rigorous formulation for the scheduling of reversible-flow multiproduct pipelines. Comput. Chem. Eng. 2014, 61, 59−76. (77) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. Detailed scheduling of oil products pipelines with parallel batch inputs at intermediate sources. Chem. Eng. Trans. 2014, 32, 1345−1350. (78) Dondo, R.; Cerdá, J. A monolithic approach to vehicle routing and operations scheduling of a cross-dock system with multiple dock doors. Comput. Chem. Eng. 2014, 63, 184−205. (79) Cafaro, V. G.; Cafaro, D. C.; Méndez, C. A.; Cerdá, J. MINLP model for the detailed scheduling of refined products pipelines with flow rate dependent pumping costs. Comput. Chem. Eng. 2014, DOI: 10.1016/j.compchemeng.2014.05.012.
16898
dx.doi.org/10.1021/ie503887k | Ind. Eng. Chem. Res. 2014, 53, 16895−16898
