In the frame of globalization and sustainability, process intensification, a path to the future of chemical and process engineering (molecules into money)

Abstract In today's economy, chemical and process engineering must respond to the changing needs of the chemical processes and related industries in order to satisfy both the increasing market requirements for specific end-use properties of the product required by the customer, and the social, and the raw material and energy savings, and environmental constraints of the industrial-scale process. In such a context of globalization and sustainability and amongst several tracks, it is shown that process intensification is a path for the future of chemical and process engineering demands. Process intensification concerns the design of novel equipment based on scientific principles and new production methods and is obtained in using either multifunctional reactors, or new operating modes, or microengineering and microtechnology for both high throughput and formulation screening, and for chemical production. Thus process intensification leads to more or less complex technologies that replace large, expensive, energy-intensive equipment or processes with ones that are smaller, less costly, more efficient plants, minimizing environmental impact, increasing safety and improving remote control and automation, or that combine multiple operations into a single apparatus or into fewer devices. With the help of the multidisciplinary and multiscale approach of the chemical engineering applied from the scale of the microreaction technology up to the scale of multifunctional macroreactors or equipment, process intensification offers new opportunities for chemical engineering, e.g., in concurrent product/process or microprocess engineering which can offer strategic competitive advantage in speed to market, cost, and also production innovation. It is thus involved in the trend “molecules into money” which is based on the premise that chemical engineering drives today economy development and is fundamental to wealth creation.

[1]  B Allen,et al.  Design of a prototype miniature bioreactor for high throughput automated bioprocessing , 2003 .

[2]  Volker Hessel,et al.  Mixers with Microstructured Foils for Chemical Production Purposes , 2005 .

[3]  L. Papageorgiou,et al.  Customer Demand Forecasting via Support Vector Regression Analysis , 2005 .

[4]  Roshan Jeet Jee Jachuck Process Intensification for Responsive Processing , 2002 .

[5]  Jae W. Lee,et al.  Feasible Products in Batch Reactive Extractive Distillation , 2004 .

[6]  Claude de Bellefon,et al.  High-Throughput Screening of Molecular Catalysts Using Automated Liquid Handling, Injection, and Microdevices , 2002 .

[7]  K. Sundmacher,et al.  Reactive distillation : status and future directions , 2003 .

[8]  Lothar Spiegel,et al.  Distillation Columns with Structured Packings in the Next Decade , 2003 .

[9]  Alexandre C. Dimian,et al.  Fatty acid esterification by reactive distillation. Part 1: equilibrium-based design , 2003 .

[10]  Ka Ming Ng,et al.  Synthesis of crystallization–distillation hybrid separation processes , 1997 .

[11]  Raghunath V. Chaudhari,et al.  Selective hydrogenation of 1,5,9-cyclododecatriene in up- and down-flow fixed-bed reactors: experimental observations and modeling , 2001 .

[12]  Won Hi Hong,et al.  Recovery of Lactic Acid by Batch Distillation with Chemical Reactions Using Ion Exchange Resin , 1999 .

[13]  Ka Ming Ng,et al.  Synthesis of reactive crystallization processes , 1997 .

[14]  Cheng-Ching Yu,et al.  Control of different reactive distillation configurations , 2006 .

[15]  Asterios Gavriilidis,et al.  Technology and Applications of Microengineered Reactors , 2002 .

[16]  Faïçal Larachi,et al.  Theory of trickle-bed magnetohydrodynamics under magnetic-field gradients , 2003 .

[17]  M. Habulin,et al.  Hydrolases in supercritical CO2 and their use in a high-pressure membrane reactor , 2003, Bioprocess and biosystems engineering.

[18]  Andrew G. Livingston,et al.  Application of Organic Solvent Nanofiltration to Separation of Ionic Liquids and Products from Ionic Liquid Mediated Reactions , 2005 .

[19]  Asterios Gavriilidis,et al.  Catalyst Design: Optimal Distribution of Catalyst in Pellets, Reactors, and Membranes , 2005 .

[20]  Achim Hoffmann,et al.  Catalytic distillation in structured packings: Methyl acetate synthesis , 2001 .

[21]  Krishna D.P. Nigam,et al.  Process intensification in trickle-bed reactors , 2005 .

[22]  A. I. Stankiewicz,et al.  Process Intensification: Transforming Chemical Engineering , 2000 .

[23]  Rajamani Krishna,et al.  Modelling reactive distillation , 2000 .

[24]  K. Jensen Microreaction engineering * is small better? , 2001 .

[25]  Ravi Arora,et al.  Microchannel Technology Scale-up to Commercial Capacity , 2005 .

[26]  Faïçal Larachi,et al.  Mitigating fines plugging in high pressure/temperature hydrotreaters using an induced-pulsing trickle-bed filtration approach , 2005 .

[27]  Nathalie Tanchoux,et al.  Microreactors for Dynamic, High Throughput Screening of Fluid/Liquid Molecular Catalysis , 2000 .

[28]  Christian Guizard,et al.  Membrane technology and supercritical fluids: chemical engineering for coupled processes , 2002 .

[29]  Peter Lehner,et al.  Monoliths as multiphase reactors: A review , 2004 .

[30]  Thomas Bayer,et al.  IMPULSE – A New Approach to Process Design† , 2005 .

[31]  E. H. Stitt,et al.  Multifunctional Reactors? ‘Up to a Point Lord Copper’ , 2004 .

[32]  E. H. Stitt,et al.  Reactive distillation for toluene disproportionation: a technical and economic evaluation , 2002 .

[33]  Freek Kapteijn,et al.  Multiphase monolith reactors: Chemical reaction engineering of segmented flow in microchannels , 2005 .

[34]  M. van Sint Annaland,et al.  Development and modelling of membrane reactors , 2005 .

[35]  Enrico Drioli,et al.  Progress and New Perspectives on Integrated Membrane Operations for Sustainable Industrial Growth , 2001 .

[36]  Enrico Drioli,et al.  State of the Art and Recent Progresses in Membrane Contactors , 2005 .

[37]  J. C. Charpentier Four main objectives for the future of chemical and process engineering , 2003 .

[38]  Václav Tesař,et al.  Development of a Microfluidic Unit for Sequencing Fluid Samples for Composition Analysis , 2004 .

[39]  Stu Borman COMBINATORIAL CHEMISTRY: REDEFINING THE SCIENTIFIC METHODRecent concepts and advances in this dynamic field involve combinatorial animals, target-guided ligand assembly, fluorous mixtures, microencapsulation, and nanoelectrospray technology , 2000 .

[40]  P. L. Silveston,et al.  Periodic Operation of Three — Phase Catalytic Reactors , 2008 .

[41]  Tapio Salmi,et al.  Studies on The Ultrasonic Enhancement of The Catalytic Activity in The Hydrogenation of Citral , 2002 .

[42]  Marcel Liauw,et al.  Comparison of Microchannel and Fixed Bed Reactors for Selective Oxidation Reactions: Isoprene to Citraconic Anhydride , 2005 .

[43]  Gert Desmet,et al.  Performance limits of isothermal packed bed and perforated monolithic bed reactors operated under laminar flow conditions. Part II: performance comparison and design considerations , 2003 .

[44]  D. Paolucci-Jeanjean,et al.  Biomolecule Applications for Membrane-Based Phase Contacting Systems: Distribution, Separation and Reaction—A First State of the Art , 2005 .

[45]  D. C. Hendershot,et al.  Process minimization: Making plants safer , 2000 .

[46]  Muthanna H. Al-Dahhan,et al.  Modelling and simulation of the monolithic reactor for gas-liquid-solid reactions , 2005 .

[47]  Karl T. Chuang,et al.  Design of a Process for Production of Isopropyl Alcohol by Hydration of Propylene in a Catalytic Distillation Column , 2002 .

[48]  Achim Karl-Erich Heibel,et al.  Monolithic Catalysts for the Chemical Industry , 2004 .

[49]  Costas Tsouris,et al.  Process intensification - Has its time finally come? , 2003 .

[50]  F. Dautzenberg,et al.  Process intensification using multifunctional reactors , 2001 .

[51]  Gilbert Marcel Rios,et al.  Special Issue—Process Developments in Membrane Contactors and Reactors , 2005 .

[52]  Lester Kershenbaum Special Issue—ISMR3–CCRE18 , 2004 .