By Thomas Dietrich
Chapter 1 impression of Microtechnologies on Chemical Processing (pages 3–28): Jean F. Jenck
Chapter 2 Microreactors constituted of metal fabrics (pages 31–46): Frank N. Herbstritt
Chapter three Microreactors made from Insulating fabrics and Semiconductors (pages 47–64): Norbert Schwesinger and Andreas Freitag
Chapter four Micromixers (pages 65–86): Joelle Aubln and Catherine Xuereb
Chapter five Microchannel warmth Exchangers and Reactors (pages 87–129): Mark George Kirby and Svend Rumbold
Chapter 6 Separation devices (pages 131–163): Asterios Gavrlllldls and John Edward Andrew Shaw
Chapter 7 Calculations and Simulations (pages 165–184): Dieter Bothe
Chapter eight Dosage gear (pages 187–197): Aslf Karlm and Wolfgang Loth
Chapter nine Micromachined Sensors for Microreactors (pages 199–244): Jan Dziuban
Chapter 10 Automating Microprocess platforms (pages 245–264): Thomas Muller?Heinzerling
Chapter eleven ideas for Lab?Scale improvement (pages 267–283): Dirk Krischneck
Chapter 12 Microreaction structures for schooling (pages 285–298): Marcel A. Liauw and Dlna E. Treu
Chapter thirteen Microreaction structures for Large?Scale construction (pages 299–323): Anna Lee Y. Tonkovich and Eric A. Daymo
Chapter 14 strategy Intensification (pages 325–347): Michael Matlosz, Iaurent Falk and Jean?Marc Commenge
Chapter 15 Standardization in Microprocess Engineering (pages 349–357): Alexis Bazzanella
Chapter sixteen Polymerization in Microfluidic Reactors (pages 361–383): Eugenia Kumacheva, Hong Zhang and Zhihong Nie
Chapter 17 Photoreactions (pages 385–402): Teijiro Ichimura, Yoshihisa Matsushita, Kosaku Sakeda and Tadashi Suzuki
Chapter 18 Intensification of Catalytic strategy by way of Micro?Structured Reactors (pages 403–430): Lioubov Kiwi?Minsker and Albert Renken
Chapter 19 Microstructured Immobilized Enzyme Reactors for Biocatalysis (pages 431–447): Malene S. Thomsen and Bernd Nidetzky
Chapter 20 Multiphase Reactions (pages 449–474): J. G. E. Han Gardeniers
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Additional info for Microchemical Engineering in Practice
Jashuck and J. F. Jenck, AIChE Process Development Symposium, Palm Springs, CA, June 12, 2006. 10. D. Hendershot, CEP, 2000. 1 1. Image courtesy A. Stankiewicz, TU Delft, July 2003. 12. Image courtesy A. Green, BHR Group, Sept. 2005. 13. Image courtesy S. Fleet, BRITEST, March 2005. 14. Image courtesy Yole Development, Lyon, France. 15. Photos in Chemical & Engineering News, Dec. 18, 2006, p. 38. 16. 71st Annual Meeting SCE, Tokyo, Japan, March 28-29, 2006. hitachi. pdf. 17. com/siprocess. 18. Image courtesy A.
32 UOP hydrogen peroxide (copyright UOP LLC; all rights reserved). is the least capital-intensive (Fig. 31). Explosive conditions are also those that guarantee significantly lower variable costs (Fig. 32). 3 Fine Chemicals Lonza published the results of their detailed analysis of different type of reactions (Fig. 33). Type A are very fast and mixing-controlled; type B are rapid and kinetically controlled; type C are slow, but with a safety or quality issue. Of 86 reaction campaigns carried out at Lonza, 50% could benefit from a continuous process.
KOH (25 to 40%) is the most frequently used etching solution. Instead of KOH, one can also use CsOH, NaOH, and NH40H as inorganic etchants or ethylendiamine, hydrazine, and TMAH as organic solutions. Etching is performed at temperatures between 60 and 110°C. The etch behavior differs completely from that in acidic solutions. Instead of rounded shapes as seen in the previous chapter, one can achieve very sharp shapes and edges as well. 1 Wet chemical etching of Si in acidic solutions. Left: top view, right: cross section.
Microchemical Engineering in Practice by Thomas Dietrich