SECTION TEN-SPEAD MODELING FOR ORGANIC ACID AND ESTERS VAPOR PRESSURE 10.1 Background 10.2 Approaches in SPEAD Modeling 10.2.1. Pair Interaction Sites of Ethyl Lactate Oligomers and Acetals of Glycerols 10.2.2. Approach of Optimizing Secondary-OH and-COO-groups 10.2.3. Mathematical Methodology 10.2.4. The DBCONF routine algorithm 151 10.3. Results of Optimization of the 2 nd-OH and-COO-groups 10.4. Prediction of Psat for Ethyl lactate Oligomers 154 10.4.1. Effect of intramolecular H-bonds in Lactates 10.4.2. A common point for Ethyl Lactate Oligomers 156 10.5. Prediction of P sat for Acetals SECTION ELEVEN-REFERENCES 162 157 Original SOW covered by final report 161 SECTION ONE INTRODUCTION AND LITERATURE BACKGROUND ON ESTERIFICATION AND REACTIVE DISTILLATION 1.1. Introduction Organic esters are gaining increased importance in a number of industrial applications, primarily as solvents to replace petroleum-derived materials, and thus hold promise as a major class of bio-based commodity products. The application of reactive distillation to esterification holds great promise for efficient production, yet is relatively unexplored as a commercial process. The aim of the proposed project was to implement a full complement of scientific and technical tools ranging from fundamental thermodynamic data collection to detailed process economic and market analyses in order to demonstrate the viability of reactive distillation for esters production. The project was conducted by a multi-faceted team with combined expertise in scientific area necessary for the successful outcome of this project. Reactive distillation has gained substantial attention recently in the research and industrial communities, 1-2 because it offers clear advantages over traditional approaches for carrying out equilibrium-limited chemical reactions. Candidate reactions for reactive distillation are characterized by a substantial difference in volatility between reaction products, such that removal of one product by distillation drives the reaction to completion. Reactions are often catalyzed, either by solid catalysts packed within the distillation column or by addition of homogeneous catalysts (acids, bases, metal complexes, etc.) added to the column feed. Esterification of organic acids satisfies the above criterion for consideration as a reaction amenable to reactive distillation. In particular, the formation of alkyl esters, typically formed by reaction of simple alcohols such as methanol, ethanol, etc. with the acid, is attractive, as the ester and water produced as reaction products can usually be separated by distillation. Although this principle is well understood, reactive distillation has not been broadly exploited for esterification because of the typical complexity of the thermodynamics of these systems. An application of reactive distillation which has been demonstrated commercially is Tennessee Eastman's methyl acetate process 3. Upon its implementation; the single reactive distillation column replaced thirteen individual unit operations and ...