Industrial Requirements for Thermodynamics and Transport Properties

被引:224
作者
Hendriks, Eric [1 ]
Kontogeorgis, Georgios M. [2 ]
Dohrn, Ralf [3 ]
de Hemptinne, Jean-Charles [4 ]
Economou, Ioannis G. [5 ]
Zilnik, Ljudmila Fele [6 ]
Vesovic, Velisa [7 ]
机构
[1] Shell Global Solut, Shell Technol Ctr Amsterdam, NL-1031 HW Amsterdam, Netherlands
[2] Tech Univ Denmark, CERE, Dept Chem & Biochem Engn, DK-2800 Lyngby, Denmark
[3] Bayer Technol Serv GmbH, Proc Technol Kinet Properties & Modeling, D-51368 Leverkusen, Germany
[4] IFP, F-92852 Rueil Malmaison, France
[5] Petr Inst, Dept Chem Engn, Abu Dhabi, U Arab Emirates
[6] Natl Inst Chem, Dept Catalysis & React Engn, SI-1001 Ljubljana, Slovenia
[7] Univ London Imperial Coll Sci Technol & Med, Dept Earth Sci & Engn, London SW7 2AZ, England
关键词
SOLVENT SELECTION; QUANTUM-MECHANICS; PHASE-EQUILIBRIA; FLUID PROPERTIES; SOLUBILITY; PRODUCT; DESIGN; TECHNOLOGIES; PREDICTION; SIMULATION;
D O I
10.1021/ie101231b
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work reports the results of an investigation on industrial requirements for thermodynamic and transport properties carried out by the Working Party on Thermodynamic and Transport properties (http://www. wp-ttp.dk/) of the European Federation of Chemical Engineering, EFCE (http://www.efce.info/). A carefully designed questionnaire was sent to a number of key technical people in companies in the oil and gas, chemicals, and pharmaceutical/biotechnology sectors. Twenty-eight companies have provided answers which formed the basis for the analysis presented here. A number of previous reviews, specifically addressed to or written by industrial colleagues, are discussed initially. This provides the context of the survey and material with which the results of the survey can be compared. The results of the survey have been divided into the themes: data, models, systems, properties, education, and collaboration. The main results are as follows. There is (still) an acute need for accurate, reliable, and thermodynamically consistent experimental data. Quality is more important than quantity. Similarly, there is a great need for reliable predictive, rather than correlative, models covering a wide range of compositions, temperatures, and pressures and capable of predicting primary (phase equilibrium) and secondary (enthalpy, heat capacity, etc.) properties. It is clear that the ideal of a single model covering all requirements is not achievable, but there is a consensus that this ideal should still provide the direction for future development. The use of new methods, such as SAFT, is increasing, but they are not yet in position to replace traditional methods such as cubic equations of state (especially in oil and gas industry) and the UNIFAC group contribution approach. A common problem with novel methods is lack of standardization, reference data, and correct and transparent implementations, especially in commercially available simulation programs. The survey indicates a great variety of systems where further work is required. For instance, for electrolyte systems better models are needed, capable of describing all types of phase behavior and mixtures with other types of components. There is also a lack of data and methods for larger complex molecules. Compared with the previous reviews, complex mixtures containing carbon dioxide associated with a wide range of applications, such as capture, transport, and storage are becoming interesting to a number of survey participants. Despite the academic success of molecular simulation techniques, the survey does not indicate great interest in it or its future development. Algorithms appear to be a neglected area, but improvements are still needed especially for multiphase reactive systems (simultaneous chemical and physical equilibrium). Education in thermodynamics is perceived as key, for the future application of thermodynamics in the industry. A number of suggestions for improvement were made at all three levels (undergraduate, postgraduate, and professional development) indicating that the education is correctly perceived as an ongoing process.
引用
收藏
页码:11131 / 11141
页数:11
相关论文
共 58 条
[1]   Chemical product design - A new challenge of applied thermodynamics [J].
Abildskov, J ;
Kontogeorgis, GM .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2004, 82 (A11) :1505-1510
[2]  
Agarwal R, 2001, CHEM ENG PROG, V97, P64
[3]   Challenges in thermodynamics [J].
Arlt, W ;
Spuhl, O ;
Klamt, A .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (03) :221-238
[4]  
Bokis CP, 1999, CHEM ENG PROG, V95, P39
[5]   Phase equilibria for food product and process design [J].
Bruin, S .
FLUID PHASE EQUILIBRIA, 1999, 158 :657-671
[6]  
Carlson EC, 1996, CHEM ENG PROG, V92, P35
[7]   Applied thermodynamics for process modeling [J].
Chen, CC ;
Mathias, PM .
AICHE JOURNAL, 2002, 48 (02) :194-200
[8]   Correlation and prediction of drug molecule solubility in mixed solvent systems with the Nonrandom Two-Liquid Segment Activity Coefficient (NRTL-SAC) model [J].
Chen, Chau-Chyun ;
Crafts, Peter A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (13) :4816-4824
[9]  
Crafts P, 2007, CHEM PRODUCT DESIGN
[10]   A DATA-BASE STANDARD FOR THE EVALUATION OF VAPOR-LIQUID-EQUILIBRIUM MODELS [J].
DANNER, RP ;
GESS, MA .
FLUID PHASE EQUILIBRIA, 1990, 56 :285-301