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- 2011 Annual Meeting
- Process Development Division
- Simulation Tools for Chemical Product Design
- (409b) Lipid Processing Technology: Shifting From Waste Streams to High-Value Commercial by-Products
The aim of this work is to present the development of computer-aided methods and tools for the systematic design, analysis, and simulation of processes/products employing lipid technologies. This includes, the identification and classification of the most representative lipid chemical species found in the edible oil and biodiesel industries and their representation in terms of molecular structure and the buildup of appropriate models for estimating pure component properties needed for model-based design and analysis of edible oil and biodiesel processes. In addition, for the modeling of phase behavior of relevant lipid mixtures, a combined group-contribution and atom connectivity approach (Group-ContributionPlus (GCPlus)) that is able to extend the application range of property models has been developed. The main idea is the use of connectivity indices to describe the molecular fragmentation that relates properties which is the molecular interactions with the molecular structures.
For this purpose, a filled lipid-database (CAPEC_Lipids_Database) of collected experimental data from the open literature, confidential data from industry and generated data from validated predictive property models; as well as modeling tools for fast adoption-analysis of property prediction models to make it suitable for application with other computer-aided tools was developed. The CAPEC_Lipids_Database contains a total of 2603 data points collected for 12 pure component properties for a total of 243 lipid compounds. Among them 73 are triglycerides (C31-C63), 41 are diglycerides (C27-C43), 15 are monoglycerides (C11-C17), 29 are free fatty acids (C6:C24), 29 are methyl esters (C7-C25), 29 are ethyl esters (C8-C26), 4 are tocopherols (C27-C29), 4 are tocotrienols (C27-C29), 9 are terpenes (C30-C40), and 8 are sterols (C27-C53). For single value pure component properties and temperature dependent properties such as vapor pressure, enthalpy of vaporization, heat capacity, liquid viscosity, and surface tension GC-based models fine-tuned for the lipid chemicals were employed; in the case of the liquid density, the well-known modified Rackett equation and the Chemical Constituent Fragment approach were used. The regression of the adopted GC-based model parameters needed experimental data. PC-SAFT EoS was used to generate pseudo-experimental data when real data was not available. For the modeling of phase behavior of the relevant lipid mixtures, a master parameter table that contains all the needed binary interaction parameters fine tuned for lipid chemicals is made available. A user-added database (CAPEC_LIPIDS_x.x) that can be directly linked to PRO/II has been generated from the lipid-database. Through this database, PRO/II can be used to simulate and optimize edible oil process flowsheets.
Finally, the applicability of the developed methods and tools is shown through the analysis and simulation of the physical refining process of oils and fats. Within the traditional oleochemical industry this process is quite interesting because apart from obtaining the final oil product, it can now be employed to also produce (extract and refine) the high-value commercial by-products such as tocopherols and sterols.