Page 357 - Sustainability in the Process Industry Integration and Optimization
P. 357
334 Bibl iog r aph y
LINDO System, 2009. LINDO System Website. <www.lindo.com> (accessed 26
October 2009).
Linnhoff, B., Ahmad, S., 1990. Cost optimum heat exchanger networks—1. Minimum
energy and capital using simple models for capital cost. Computers & Chemical
Engineering, 14(7), 729–750.
Linnhoff, B., Akinradewo, C. G., 1998. Automated interface between dimulation
and integration, CHISA 1998 / 1st Conference PRES 1998, Plenary lecture A3.0
[818] Prague: Czech Society of Chemical Engineering.
Linnhoff, B., Dhole, V. R., 1992. Shaftwork targets for low temperature process
design. Chemical Engineering Science, 47(8), 2081–2091.
Linnhoff, B., Dhole, V. R., 1993. Targeting for CO emissions for total sites. Chemical
2
Engineering and Technology, 16(4), 252–259.
Linnhoff, B., Flower, J. R., 1978. Synthesis of heat exchanger networks: I. Systematic
generation of energy optimal networks. AIChE Journal, 24(4), 633–642.
Linnhoff, B., Hindmarsh, E., 1983. The pinch design method for heat exchanger
networks. Chemical Engineering Science, 38(5), 745–763.
Linnhoff, B., Mason, D. R., Wardle, I., 1979. Understanding Heat Exchanger
Networks. Computers & Chemical Engineering, 3(1–4), 295–302.
Linnhoff, B., Townsend, D. W., Boland, D., Hewitt, G. F., Thomas, B. E. A., Guy, A.
R., Marsland, R. H., 1982. A user guide on process integration for the efficient use
of energy. Rugby, U.K.: IChemE [revised edition published in 1994].
Linnhoff, B., Vredeveld, D. R., 1984. Pinch technology has come of age. Chemical
Engineering Progress, 80(7), 33–40.
Linnhoff March, 1998. Introduction to Pinch Technology. <www.linnhoffmarch.
com/pdfs/PinchIntro.pdf> (aaccessed 27 October 2009).
Linnhoff March, 2009. Introduction to Pinch Technology. <www.kbcat.com/Products-
and-Services/Software/Energy-Optimisation-Software-/SuperTarget/>
(accessed 11 January 2010).
Liu, F., Zhang, N., 2004. Strategy of purifier selection and integration in hydrogen
networks. Chemical Engineering Research and Design, 82(A10), 1315–1330.
Liu, J., Fan, L. T., Seib, P., Friedler, F., Bertok, B., 2004. Downstream process
synthesis for biochemical production of butanol, ethanol, and acetone from
grains: Generation of optimal and near-optimal flowsheets with conventional
operating units. Biotechnology Progress, 20, 1518–1527.
Liu, J., Fan, L. T., Seib, P. A., Friedler, F., Bertok, B., 2006. Holistic approach to process
retrofitting: Application to downstream process for biochemical production of
organics. Industrial & Engineering Chemistry Research, 45, 4200–4207.
Liu, Y., Yuan, X., Luo, Y., 2007. Synthesis of water utilization system using
concentration interval analysis method, II. Discontinuous process. Chinese
Journal of Chemical Engineering, 15(3), 369–375.
Luenberger D. G., Ye, Y., 2008. Linear and nonlinear programming, 3rd ed. New York:
Springer.
Macias-Corral, M., Samani, Z., Hanson, A., Smith, G., Funk, P., Yu, H., Longworth, J.,
2008. Anaerobic digestion of municipal solid waste and agricultural waste
and the effect of co-digestion with dairy cow manure. Bioresource Technology,
99(17), 8288–8293.
Majozi, T., 2005. An effective technique for wastewater minimisation in batch
processes. Journal of Cleaner Production, 13, 1374–1380.
Majozi, T., Brouckaert, C. J., Buckley, C. A., 2006. A graphical technique for waste-
water minimisation in batch processes. Journal of Environmental Management,
78, 317–329.
Majozi, T., Friedler, F. 2006. Maximization of throughput in a multipurpose batch
plant under fixed time horizon: S-graph approach. Industrial & Engineering
Chemistry Research, 45, 6713–6720.
Majozi, T., Zhu, X. X., 2001. A novel continuous time MILP formulation for
multipurpose batch plants. 1. Short-term scheduling. Industrial & Engineering
Chemistry Research, 40(25), 5935–5949.
Makwana, Y., 1998. Energy retrofit and debottlenecking of total sites. PhD thesis,
UMIST, Manchester, U.K.