Page 345 - Sustainability in the Process Industry Integration and Optimization

322 Bibl iog r aph y

Alva-Argáez, A., Kokossis, A. C., Smith, R., 1998. Wastewater minimisation of
industrial systems using an integrated approach. Computers & Chemical
Engineering, 22, 741–744.
Alves, J., 1999. Analysis and design of refinery hydrogen distribution systems.
PhD thesis, UMIST, Manchester, U.K.
Alves, J. J., Towler, G. P., 2002. Analysis of refinery hydrogen distribution systems.
Industry and Engineering Chemistry Research, 41, 5759–5769.
Arellano-Garcia, H., Martini, W., Wendt, M., Li, P., Wozny, G., 2003. Chance
constrained batch distillation process optimization under uncertainty.
Foundations of Computer Aided Process Operations—FOCAPO (Coral Springs,
FL, 12–15 January).
Arellano-Garcia, H., Wozny, G., 2009. Chance constrained optimization of process
systems under uncertainty: I. Strict monotonicity. Computers & Chemical
Engineering, 33, 1568–1583.
Argonne National Laboratory, 2009a. Electricity Market Complex Adaptive
System (EMCAS). <www.dis.anl.gov/projects/emcas.html> (accessed 23
April 2009).
Argonne National Laboratory, 2009b. Energy and Power Evaluation Program
(ENPEP-BALANCE). <www.dis.anl.gov/projects/Enpepwin.html> (accessed
23 April 2009).
Argonne National Laboratory, 2009c. Generation and Transmission Maximization
(GTMax) Model. <www.dis.anl.gov/projects/Gtmax.html> (accessed 23 April
2009).
Asante, N. D. K., 1996. Automated and interactive retrofit design of practical heat
exchanger networks. PhD thesis, UMIST, Manchester, U.K.
Asante, N. D. K., Zhu, X. X., 1997. An automated and interactive approach for
heat exchanger network retrofit. Chemical Engineering Research and Design,
75(part A), 349–360.
Aspelund, A., Berstad, D. A., Gundersen, T., 2007. An extended pinch analysis and
design procedure utilizing pressure based exergy for subambient cooling.
Applied Thermal Engineering, 27, 2633–2649.
Aspelund, A., Gundersen, T., 2007. A new process synthesis methodology utilizing
pressure exergy in subambient processes. Computer Aided Chemical Engineering,
24, 1133–1138.
AspenTech, 2009a. Aspen Economic Evaluation. <www.aspentech.com/products/
aspen-economic-eval.cfm> (accessed 26 October 2009).
AspenTech, 2009b. Aspen Exchanger Design & Rating (EDR). <www.aspentech.
com/products/spen-edr.cfm> (accessed 26 October 2009).
AspenTech, 2009c. Aspen Plus. <www.aspentech.com/core/aspen-plus.cfm>
(accessed 26 October 2009).
AspenTech, 2009d. What Is Aspen ONE. <www.aspentech.com/v7/whatis.cfm>
(accessed 26 October 2009).
Avriel, M., Wilde, D. J., 1966. Optimality proof for the symmetric Fibonacci search
technique. Fibonacci Quarterly, 4, 265–269.
Bagajewicz, M., 2000. A review of recent design procedures for water networks
in refineries and process plants. Computers & Chemical Engineering, 24,
2093–2113.
Bagajewicz, M., Savelski, M., 2001. On the use of linear models for the design
of water utilization systems in process plants with a single contaminant.
Chemical Engineering Research and Design, 79(5), 600–610.
Balmorel [Danish Energy Research Program], 2009. <www.balmorel.com/>
(accessed 30 December 2009).
Bandyopadhyay, S., Ghanekar, M. D., Pillai, H. K., 2006. Process water management.
Industrial & Engineering Chemistry Research, 45, 5287–5297.
Banerjee, I., Ierapetritou, M. G., 2003. Parametric process synthesis for general
non-linear models. Computers & Chemical Engineering, 27, 1499–1512.
Barlow, R. E, Proschan, F., 1996. Mathematical theory of reliability. Society
for Industrial and Applied Mathematics, New York, USA, ISBN-13:
978-0898713695.