Design and control of acetic acid dehydration system via heterogeneous azeotropic distillation using p-xylene as an entrainer

Abstract In the process of manufacturing terephthalic acid, very small amount of reactant p-xylene may enter into the feed stream of an acetic acid dehydration column. Traditionally, acetic esters were used as entrainers to separate acetic acid and water by heterogeneous azeotropic distillation (HAD). However, they can contaminate the process. In the study, the feasibility of using p-xylene as the entrainer is evaluated to eliminate the drawbacks of the HAD column using acetic esters as entrainers. An improved column is proposed for the separation of acetic acid and water in the presence of methyl acetate and tiny amount of p-xylene. Two configurations of the HAD column using p-xylene as the entrainer are designed by using different p-xylene purge strategies. The HAD column with a side stream to purge p-xylene accumulated in the column gives the most economical design. A temperature control strategy is proposed for this HAD column to maintain acetic acid compositions in both the aqueous phase of the decanter and the column bottom. The controlled stage temperatures are chosen by singular value decomposition and closed-loop analysis methods. Dynamic simulation results reveal that the proposed control strategy can maintain product purities in spite of feed flow and feed composition changes.

[2]  Charles F. Moore Selection of Controlled and Manipulated Variables , 1992 .

[3]  I. Chien,et al.  Design and Control of Acetic Acid Dehydration Column with p-Xylene or m-Xylene Feed Impurity. 1. Importance of Feed Tray Location on the Process Design , 2007 .

[4]  M. Rovaglio,et al.  The key role of entrainer inventory for operation and control of heterogeneous azeotropic distillation towers , 1993 .

[5]  Shaojun Li Influence of p-Xylene (PX) Accumulation on the Operation of Pure Terephthalic Acid (PTA) Solvent Dehydratic Distillation Column , 2009 .

[6]  I. Chien,et al.  Design and Control of an Acetic Acid Dehydration Column with p-Xylene or m-Xylene Feed Impurity. 2. Bifurcation Analysis and Control , 2008 .

[7]  J. B. Montón,et al.  Polyazeotropy in Associating Systems: The 2-Methylpropyl Ethanoate + Ethanoic Acid System , 1996 .

[8]  Shih‐Haur Shen,et al.  Use of relay‐feedback test for automatic tuning of multivariable systems , 1994 .

[9]  William L. Luyben,et al.  Derivation of transfer functions for highly nonlinear distillation columns , 1987 .

[10]  Shyan-Shu Shieh,et al.  Plant-wide design and control of acetic acid dehydration system via heterogeneous azeotropic distillation and divided wall distillation , 2008 .

[11]  John P. O'Connell,et al.  A Generalized Method for Predicting Second Virial Coefficients , 1975 .

[12]  Jun Hong Liu,et al.  Design and control of acetic acid dehydration system via heterogeneous azeotropic distillation , 2004 .

[13]  I. Chien,et al.  Influence of Feed Impurity on the Design and Operation of an Industrial Acetic Acid Dehydration Column , 2005 .

[14]  Francisco J. L. Castillo,et al.  Optimal design of complex azeotropic distillation columns , 2000 .