Modeling and in-depth analysis of the start-up of dividing-wall columns
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[1] Günter Wozny,et al. Analysis of the Start‐up Process for Reactive Distillation , 2003 .
[2] Sunwon Park,et al. Startup of distillation columns using profile position control based on a nonlinear wave model , 1999 .
[3] Kamalesh K. Sirkar,et al. Ternary gas mixture separation in two‐membrane permeators , 1987 .
[4] Georg Fieg,et al. Startup Operation of Middle-Vessel Batch Distillation Column: Modeling and Simulation , 2008 .
[5] Georg Fieg,et al. Experimental and Theoretical Studies of a Dividing-Wall Column Used for the Recovery of High-Purity Products , 2010 .
[6] Sigurd Skogestad,et al. Operation of Integrated Three-Product (Petlyuk) Distillation Columns , 1995 .
[7] Robert W. Field,et al. Distillation and Absorption , 1988 .
[8] Michel Cabassud,et al. Dynamic models for start-up operations of batch distillation columns with experimental validation , 2004, Comput. Chem. Eng..
[9] Pu Li,et al. Theoretical and experimental studies on startup strategies for a heat-integrated distillation column system , 2003 .
[10] Nicolás J. Scenna,et al. Start-up Operation of Reactive Columns with Multiple Steady States: The Ethylene Glycol Case , 2003 .
[11] Robin Smith,et al. Operation and Control of Dividing Wall Distillation Columns: Part 2: Simulation and Pilot Plant Studies Using Temperature Control , 1998 .
[12] Moses O. Tadé,et al. Dynamic Simulation of Startup in Ethyl tert-Butyl Ether Reactive Distillation with Input Multiplicity , 2000 .
[13] Günter Wozny,et al. Experimental and theoretical studies of the dynamics of startup and product switchover operations of distillation columns , 1993 .
[14] Nicolás J. Scenna,et al. Dynamic simulation of start-up procedures of reactive distillation columns , 1998 .
[15] Rodrigo Lopez-Negrete De La Fuente,et al. Optimal Start-Up and Product Transition Policies of a Reactive Distillation Column , 2007 .
[16] G. Fieg,et al. A new time-optimal strategy for column startup and product changeover , 1996 .
[17] F. Petlyuk. Thermodynamically Optimal Method for Separating Multicomponent Mixtures , 1965 .
[19] Sten Bay Jørgensen,et al. Dynamics and control during startup of heat integrated distillation column , 2000 .
[20] Günter Wozny,et al. Time optimal start-up strategies for reactive distillation columns , 2004 .
[21] Sigurd Skogestad,et al. Optimal operation of Petlyuk distillation: steady-state behavior , 1999 .
[22] Massimiliano Barolo,et al. On-line startup of a distillation column using generic model control , 1993 .
[23] Rafiqul Gani,et al. A generalized dynamic model for distillation columns—III. Study of startup operations , 1988 .
[24] M. Flender,et al. Classification of new product changeover strategy (NPS) for different application of distillation columns , 1996 .
[25] Cintia Marangoni,et al. Application of a new startup procedure using distributed heating along distillation column , 2009 .
[26] Luis Puigjaner,et al. Control and optimization of the divided wall column , 1999 .
[27] Z. Fidkowski,et al. Minimum energy requirements of thermally coupled distillation systems , 1987 .
[28] Georg Fieg,et al. Nonequilibrium stage modelling of dividing wall columns and experimental validation , 2010 .
[29] Georg Fieg. Design and Analysis of an Integral Startup System for Distillation Columns , 2005 .
[30] G. Kaibel,et al. Dividing wall columns: Fundamentals and recent advances , 2010 .
[31] M. Barolo. Nonlinear Model-Based Startup and Operation Control of a Distillation Column : An Experimental Study , 1994 .
[32] W. Geipel,et al. Fluid Dynamics of Packings for Gas‐Liquid Contactors , 2001 .
[33] Saibal Ganguly,et al. Startup of a distillation column using nonlinear analytical model predictive control , 1993 .
[34] G. Kaibel. Distillation columns with vertical partitions , 1987 .
[35] Ž. Olujić,et al. Equipment improvement trends in distillation , 2009 .
[36] Pu Li,et al. Optimisation and experimental verification of startup policies for distillation columns , 2004, Comput. Chem. Eng..
[37] Flávio Neves,et al. Startup of a distillation column using intelligent control techniques , 2005, Comput. Chem. Eng..
[38] G. Wozny,et al. A new strategy for product switchover and startup for a heat- and mass-integrated distillation system , 2001 .