1 |
Kister, H. Z., Haas, J. R., Hart, D. R. and Gill, D. R., Distillation design, McGraw-Hill, New York(1992).
|
2 |
Peters, M. S., Timmerhaus, K. D. and West, R. E., Plant design and economics for chemical engineers, 5th ed., McGraw-Hill, New York(2003).
|
3 |
Towler, G. and Sinnott, R., Chemical engineering design: principles, practice and economics of plant and process design, Elsevier(2012).
|
4 |
Seader, J. D., Henley, E. J. and Roper, D. K., Separation process principles, 3rd ed.(2011).
|
5 |
Luyben, W. L., Distillation design and control using Aspen simulation, John Wiley & Sons(2013).
|
6 |
Alfadala, H. E., Ahmad, B. M. and Warsame, A. F., A hierarchical approach to optimize LNG fractionation units, Computer Aided Chemical Engineering, Elsevier, 1279-1284(2005).
|
7 |
https://esupport.aspentech.com/S_Article?id=000047303
|
8 |
Turton, R., Bailie, R. C., Whiting, W. B. and Shaeiwitz, J. A., Analysis, synthesis and design of chemical processes, Pearson Education(2008).
|
9 |
Fenske, M., "Fractionation of Straight-run Pennsylvania Gasoline," Industrial & Engineering Chemistry 24, 482-485(1932).
DOI
|
10 |
Kirkbride, C. G., "Process Design Procedure for Multicomponent Fractionators," Petroleum Refiner 23, 321-336(1944).
|