Modeling of batch reactions with in situ spectroscopic measurements and calorimetry
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R. R. Rhinehart | R. Russell Rhinehart | Paul J. Gemperline | Graeme Puxty | Marcel Maeder | M. Maeder | P. Gemperline | G. Puxty | Samir Alam | Shane Moore | S. Alam | S. Moore | R. Rhinehart
[1] Marcel Maeder,et al. Second-order globalisation for the determination of activation parameters in kinetics , 1994 .
[2] Sarah C. Rutan,et al. Multivariate curve resolution with non-linear fitting of kinetic profiles , 2001 .
[3] Zhongliang Zhu,et al. Iterative target transformation factor analysis for the resolution of kinetic–spectral data with an unknown kinetic model , 2002 .
[4] Erik Furusjö,et al. A method for the determination of reaction mechanisms and rate constants from two-way spectroscopic data , 1998 .
[5] Olof Svensson,et al. Estimation of kinetic parameters from non-isothermal batch experiments monitored by in situ vibrational spectroscopy , 2003 .
[6] L. G. Blackwood. Factor Analysis in Chemistry (2nd Ed.) , 1994 .
[7] Lionel Estel,et al. Kinetic parameter estimation of solvent-free reactions: application to esterification of acetic anhydride by methanol , 2002 .
[8] P. Bogaerts,et al. Stability parameter estimation at ambient temperature from studies at elevated temperatures. , 2001, Journal of pharmaceutical sciences.
[9] N. Philip. Adiabatic and isothermal compressibilities of liquids , 1939 .
[10] M. Friedrich,et al. Design and control of batch reactors: -An industrial viewpoint- , 1995 .
[11] A. Smilde,et al. Estimating rate constants and pure UV‐vis spectra of a two‐step reaction using trilinear models , 1999 .
[12] Graeme Puxty,et al. Calibration-free estimates of batch process yields and detection of process upsets using in situ spectroscopic measurements and nonisothermal kinetic models: 4-(dimethylamino)pyridine- catalyzed esterification of butanol. , 2004, Analytical chemistry.
[13] S. Pushpavanam,et al. Parametric Sensitivity, Runaway, and Safety in Batch Reactors: Experiments and Models , 1994 .
[14] M. Maeder,et al. Hard‐modelled trilinear decomposition (HTD) for an enhanced kinetic multicomponent analysis , 2002 .
[15] E. D. Heilshorn. Removing VOCs from contaminated water , 1991 .
[16] M. Maeder,et al. Nonlinear least-squares fitting of multivariate absorption data , 1990 .
[17] Marcel Maeder,et al. Analysis of non-isothermal kinetic measurements , 1997 .
[18] D. Marquardt. An Algorithm for Least-Squares Estimation of Nonlinear Parameters , 1963 .
[19] William H. Press,et al. Numerical recipes in C. The art of scientific computing , 1987 .
[20] Graeme Puxty,et al. Analyses of three-way data from equilibrium and kinetic investigations , 2003 .
[21] Renato Paludetto,et al. Batch and semibatch catalytic reactors (from theory to practice) , 1999 .
[22] A. Smilde,et al. Determination of Rate Constants in Second-Order Kinetics Using UV-Visible Spectroscopy , 2001 .
[23] L. Belfiore. Transport Phenomena for Chemical Reactor Design , 2003, Kirk-Othmer Encyclopedia of Chemical Technology.
[24] A. Smilde,et al. Rapid estimation of rate constants using on-line SW-NIR and trilinear models , 1998 .
[25] Paul J. Gemperline,et al. Characterizing batch reactions with in situ spectroscopic measurements, calorimetry and dynamic modeling , 2003 .
[26] Charles E. Miller,et al. Chemometrics for on‐line spectroscopy applications—theory and practice , 2000 .
[27] K. J. Molloy,et al. Hard modelling of spectroscopic measurements. Applications in non-ideal industrial reaction systems , 1999 .
[28] E. Roets,et al. Quantitative determination by high-performance liquid chromatography of acetylsalicylic acid and related substances in tablets. , 1987, Journal of chromatography.