Abstract:IntroductionT he process industries spend an estimated $500 billion annually worldwide in conceptual design, process engineering, detailed engineering, construction, startup, plant operations, and maintenance for chemical, refining, polymer and power plants. In order for chemical engineers to successfully execute these process and product studies, they perform process modeling and capture knowledge of the thermodynamic properties and phase behavior of the chemical systems they work with.Process modeling is a k… Show more
“…The major problem concerning the VLE measurements of aqueous alkanolamine-acid gas systems, in general, is that lack of consistency and regularity in the numerous published values. Excess Gibbs energy-based activity coefficient models provide a practical and rigorous thermodynamic framework to model thermodynamic properties of aqueous electrolyte systems, including aqueous alkanolamine systems for CO 2 capture (Chen & Mathias, 2002, Chen, 2006. Austgen et al (1991) and Posey (1996) applied the electrolyte NRTL model (Song & Chen, 2009;Chen & Evans, 1986;Chen et al, 1982) to correlate CO 2 solubility in aqueous MDEA solution and other aqueous alkanolamines.…”
Carbon dioxide (CO 2 ) capture by absorption with aqueous alkanolamines is considered as an important technology to reduce CO 2 emissions and to help alleviate global climate change. To understand more the thermodynamics of some of the CO 2 -Amines, the NRTL electrolyte model has been used to simulate the behaviour of carbon dioxide absorption by some amines. To determine NRTL interaction parameters of the model, VLE, heat capacity and excess enthalpy data have been used. In this study, carbon dioxide, water and Methyl DiEthanolAmine (MDEA) ternary system are used to calculate eNRTL (electrolyte Non-Ramdom Two Liquid) interaction parameters, and the system was modelled using VLE data available in the literature. Differential evolution algorithm (DE), an evolutionary computational technique, has been used to estimate NRTL parameters model to predict the VLE of CO 2 with MDEA. Differential Evolution algorithm (DE) have been used to compare it with annealing (SA) and deterministic technique like Levenberg-Marquardt (LM) using one set of experimental data for MDEA-H 2 O system. Its standard deviation is lower than those of SA and LM algorithms when used to regress the eNRTL binary interactions parameters for MDEA-H 2 O Keywords: Themodynamics of Electrolytes; CO 2 Capture; MDEA; Differential Evolution; NRTL.
IntroductionDifferential Evolution (DE) algorithm is a new heuristic approach mainly having three advantages; finding the true global minimum regardless of the initial parameter values, fast convergence, and using few control parameters. DE algorithm is a population based algorithm like genetic algorithms using similar operators; crossover, mutation and selection. However, the success of DE in solving a specific problem crucially depends on appropriately choosing trial vector generation strategies and their associated control parameter values. Employing a trial-and-error scheme to search for the most suitable strategy and its associated parameter settings requires high computational costs. Moreover, at different stages of evolution, different strategies coupled with different parameter settings may be required in order to achieve the best performance. The NRTL-electrolyte model has been used for CO 2 absorption by MDEA where DE has been applied to have a better optimisation of the model. Scalable simulation, design, and optimization of the CO 2 capture processes start with modeling of the thermodynamic properties, specifically vapor-liquid equilibrium (VLE) and chemical reaction equilibrium, as well as calorimetric properties. Accurate modeling of thermodynamic properties requires availability of reliable experimental data. For the rational gas treating processes
“…The major problem concerning the VLE measurements of aqueous alkanolamine-acid gas systems, in general, is that lack of consistency and regularity in the numerous published values. Excess Gibbs energy-based activity coefficient models provide a practical and rigorous thermodynamic framework to model thermodynamic properties of aqueous electrolyte systems, including aqueous alkanolamine systems for CO 2 capture (Chen & Mathias, 2002, Chen, 2006. Austgen et al (1991) and Posey (1996) applied the electrolyte NRTL model (Song & Chen, 2009;Chen & Evans, 1986;Chen et al, 1982) to correlate CO 2 solubility in aqueous MDEA solution and other aqueous alkanolamines.…”
Carbon dioxide (CO 2 ) capture by absorption with aqueous alkanolamines is considered as an important technology to reduce CO 2 emissions and to help alleviate global climate change. To understand more the thermodynamics of some of the CO 2 -Amines, the NRTL electrolyte model has been used to simulate the behaviour of carbon dioxide absorption by some amines. To determine NRTL interaction parameters of the model, VLE, heat capacity and excess enthalpy data have been used. In this study, carbon dioxide, water and Methyl DiEthanolAmine (MDEA) ternary system are used to calculate eNRTL (electrolyte Non-Ramdom Two Liquid) interaction parameters, and the system was modelled using VLE data available in the literature. Differential evolution algorithm (DE), an evolutionary computational technique, has been used to estimate NRTL parameters model to predict the VLE of CO 2 with MDEA. Differential Evolution algorithm (DE) have been used to compare it with annealing (SA) and deterministic technique like Levenberg-Marquardt (LM) using one set of experimental data for MDEA-H 2 O system. Its standard deviation is lower than those of SA and LM algorithms when used to regress the eNRTL binary interactions parameters for MDEA-H 2 O Keywords: Themodynamics of Electrolytes; CO 2 Capture; MDEA; Differential Evolution; NRTL.
IntroductionDifferential Evolution (DE) algorithm is a new heuristic approach mainly having three advantages; finding the true global minimum regardless of the initial parameter values, fast convergence, and using few control parameters. DE algorithm is a population based algorithm like genetic algorithms using similar operators; crossover, mutation and selection. However, the success of DE in solving a specific problem crucially depends on appropriately choosing trial vector generation strategies and their associated control parameter values. Employing a trial-and-error scheme to search for the most suitable strategy and its associated parameter settings requires high computational costs. Moreover, at different stages of evolution, different strategies coupled with different parameter settings may be required in order to achieve the best performance. The NRTL-electrolyte model has been used for CO 2 absorption by MDEA where DE has been applied to have a better optimisation of the model. Scalable simulation, design, and optimization of the CO 2 capture processes start with modeling of the thermodynamic properties, specifically vapor-liquid equilibrium (VLE) and chemical reaction equilibrium, as well as calorimetric properties. Accurate modeling of thermodynamic properties requires availability of reliable experimental data. For the rational gas treating processes
“…Simple thermodynamic models are preferred for industrial applications versus more sophisticated models with a high number of parameters, unless a clear advantage is evident [35]. For example, Chen and col. [39] correlated the LLE data of some quaternary systems using ternary and quaternary interaction parameters in an extension of the UNIQUAC model, which was not able to reproduce the quaternary systems only with binary data.…”
Section: Limitations Of Models and Commercial Regression Toolsmentioning
confidence: 99%
“…Advantages of global versus local correlations for separation equipment design calculations are evident, since parameters are valid for all the composition space. A model that provides an accurate description of the thermodynamic properties of a system, in the entire diagram, facilitates the plant design improvement strategies, the solution of problems and the process control [35].…”
Phase equilibrium data regression is an unavoidable task necessary to obtain the appropriate values for any model to be used in separation equipment design for chemical process simulation and optimization. The accuracy of this process depends on different factors such as the experimental data quality, the selected model and the calculation algorithm. The present paper summarizes the results and conclusions achieved in our research on the capabilities and limitations of the existing G E models and about strategies that can be included in the correlation algorithms to improve the convergence and avoid inconsistencies. The NRTL model has been selected as a representative local composition model. New capabilities of this model, but also several relevant limitations, have been identified and some examples of the application of a modified NRTL equation have been discussed. Furthermore, a regression algorithm has been developed that allows for the advisable simultaneous regression of all the condensed phase equilibrium regions that are present in ternary systems at constant T and P. It includes specific strategies designed to avoid some of the pitfalls frequently found in commercial regression tools for phase equilibrium calculations. Most of the proposed strategies are based on the geometrical interpretation of the lowest common tangent plane equilibrium criterion, which allows an unambiguous comprehension of the behavior of the mixtures. The paper aims to show all the work as a whole in order to reveal the necessary efforts that must be devoted to overcome the difficulties that still exist in the phase equilibrium data regression problem.
“…Traditional methods for physical property modeling are well understood (Chen and Mathias, 2002) and will not be considered in this paper. Instead, we will briefly consider recent and current developments in six areas that we believe will have a significant impact on the practice of physical property modeling over the next several years.…”
Section: Physical Property Modelingmentioning
confidence: 99%
“…It has impacted process modeling in a number of ways: 1) help elucidate fundamental physical and chemical interactions and support development of new theories and models, 2) complement experiments for data generation especially for systems that are not readily amenable to existing experimental procedures, and 3) provide an alternative approach to extend and improve on existing applied thermodynamic models (Chen and Mathias, 2002).…”
The use of advanced modeling and simulation tools for both design and operations has long since become routine in industry, and their development has been well documented at previous FOCAPD meetings. Nevertheless many long-existent needs and new requirements are not met, and both the enabling technologies and application of these tools continues to evolve. This paper provides an industrial perspective on the current state of modeling and simulation technology, with an emphasis on recent developments, emerging technologies, and new industrial applications that promise to have a significant impact on industrial practice and economic effectiveness, as well as gaps requiring further research. Three main subject areas are covered. The first is physical property modeling, the technology for representing the properties and phase behavior of material. The second is systems and architectures for modeling and simulation. The third is design environments that enable effective use of models.
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