Page 364 - Sustainability in the Process Industry Integration and Optimization
P. 364
Bibl iog r aph y 341
Tan, R. R., Cruz, D. E., 2004. Synthesis of robust water reuse networks for single
component retrofit problems using symmetric fuzzy linear programming.
Computers & Chemical Engineering, 28, 2547–2551.
Tan, R., Foo, D. C. Y., 2007. Pinch analysis approach to carbon-constrained energy
sector planning. Energy, 32(8), 1422–1429.
Ten Broeck, H., 1944. Economic selection of exchanger sizes. Industrial & Engineering
Chemistry Research, 36(1), 64–67.
Thevendiraraj, S., Klemeš, J., Paz, D., Aso, G., Cardenas, J., 2003. Water and
wastewater minimisation study of a citrus plant. Resources, Conservation and
Recycling, 37, 227–250.
Tick, J., Kovács, Z., Friedler, F., 2006. Synthesis of optimal workflow structure.
Journal of Universal Computer Science, 12, 1385–1392.
Timpe, C. H., Kallrath, J., 2000. Optimal planning in large multi-site production
networks. European Journal of Operational Research, 126, 422–435.
Tjoe, T. N., Linnhoff, B., 1986. Pinch technology retrofit: Setting targets for an
existing plant. Chemical Engineering, 93(8), 47–60.
Tokos, H., Novak Pintarič, Z., 2009. Synthesis of batch water network for a brewery
plant. Journal of Cleaner Production, 17(16), 1465–1479.
TOMLAB, 2010. MATLAB Optimization—TOMLAB. <http://tomopt.com/tomlab>
(accessed 13 January 2010).
Tovazshnyansky, L. L., Kapustenko, P. O., Khavin, G. L., Arsenyeva, O. P., 2004.
PHEs in industry. Kharkiv, Ukraine: NTU KhPI (in Russian).
Townsend, D. W., Linnhoff, B., 1983. Heat and power networks in process design.
Part II: Design procedure for equipment selection and process matching.
AIChE Journal, 29(5), 748–771.
Townsend, D. W., Linnhoff, B., 1984. Surface area targets for heat exchanger
networks. IChemE 11th Annual Research Meeting (Bath, U.K., April).
Triantafyllou, C., Smith R., 1992. The design and optimisation of fully thermally
coupled distillation columns. Chemical Engineering Research and Design, 70(A2),
118–132.
TRNSYS, 2009. A TRaNsient SYtems Simulation Program (University of Wisconsin,
Madison). <sel.me.wisc.edu/trnsys> (accessed 27 April 2009).
U.K. Government, 2007. Government Response to Kate Barker’s Review of Housing
Supply: The Supporting Analysis (Office of the Deputy Prime Minister).
<www.odpm.gov.uk> (accessed 15 March 2007).
Umeda, T., Harada, T., Shiroko, K. A., 1979. Thermodynamic approach to the
synthesis of heat integration systems in chemical processes. Computers &
Chemical Engineering, 3(1–4), 273–282.
UML, 2010. Object Management Group—UML. <www.uml.org> (accessed 18
January 2010).
Unitec New Zealand, 2009. <www.unitec.ac.nz> (accessed 13 June 2009).
Universität Karlsruhe, 2009. Institute for Industrial Production. <www.iip.kit.
edu/65.php> (accessed 18 June 2009).
Uryasev, S. (Ed.), 2000. Probabilistic constrained optimization: Methodology and
applications. Dordrecht: Kluwer.
U.S. Department of Housing and Urban Development, 2009. How to Identify
Primary Opportunities to Save Energy—Energy Saving Techniques. <www.
hud.gov/offices/cpd/affordablehousing/training/web/energy/techniques/
techniques.cfm> (accessed 5 August 2009).
U.S. DOE, 2007. U.S. Department of Energy, Industrial Assessment Centers, Energy
Efficiency and Renewable Energy. <www.iac.rutgers.edu/database> (accessed
30 September 2007).
Václavek, V., Novotná, A., Dedková, J., 2003. Pressure as a further parameter of
composite curves in energy process integration. Applied Thermal Engineering,
23(14), 1785–1795.
VALI III User Guide, 2003. Liege, Belgium: Belsim S.A.
van der Aalst, W. M. P., ter Hofstede, A. H. M. 2005. YAWL: Yet another workflow
language. Information Systems, 30, 245–275.
Varbanov, P., 2004. Optimisation and synthesis of process utility systems. PhD
thesis, UMIST, Manchester, U.K.