H1.1 9.30
Keynote lecture:
Better solutions for process sustainability through better insight in process energy integration.
*B. Kalitventzeff, F. Marechal1, H. Closon
(BELSIM s.a., Angleur, BE; 1LASSC, Liege, BE)
[1240]
H1.2 10.10
The sustainable process index (SPI) as a tool for strategic planing and optimisation of process industries.
*M. Narodoslawsky, C. Krotscheck1, M. Bachhiesl2
(Graz Univ. Technol., AT; 1Kornberg Inst., Feldbach, AT; 2Verbund-Umwelt, Klagenfurt, AT)
[1091]
H1.3 10.30
Mass and energy integration in the planning of an eco-industrial park.
Dingjiang Chen, *Yourun Li, Jingzhu Shen, Shanying Hu, Mingheng Li, Chong Chen
(Tsinghua Univ., Beijing, CN)
[309]
H1.4 10.50
Cooling crystallization applied to the "extract" of a chromatographic separation process (SMB) of beet raw juice.
*G. Vaccari, E. Tamburini, G. Sgualdino, M. Kearney1, V. Kochergin1, D. Costesso1
(Univ. Ferrara, IT; 1Amalgamated Res., Twin Falls ID, US)
[1157]
H1.5 11.10
Minimum energy consumption in sugar production by cooling crystallisation of concentrated raw juice.
*M. Grabowski, K. Urbaniec
(Warsaw Univ. Technol., Plock, PL)
[1161]
H1.6 11.30
Optimization of gas cleaning devices using nondominated sorting genetic algorithm.
R. Gopalan, S. K. Gupta, S. Viswanathan, *M. B. Ray
(Nat. Univ. Singapore, SG)
[307]
H1.7 11.50
Waste usage of coal cleaned plants for the manufacturing of thermal-insulated ceramic products.
*G. A. Statyukha1, V. I. Mikhajlov, L. P. Chernyavskaya, R. N. Kolesnikova
(Kiev Polytech. Inst., UA; 1Sci. Inst. Build. Mat., Kiev, UA)
[519]
H1.8 12.10
A statistical study on the activated sludge process of Tupras refinery in Izmit.
I. C. Onbilgin, *T. A. Ozbelge1, O. H. Ozbelge1
(Tupras Refinery, Izmit, TR; 1Middle East Tech. Univ., Ankara, TR)
[789]
H2.1 14.00
Keynote lecture:
Design of cooling systems.
R. Smith
(UMIST, Manchester, UK)
[1239]
H2.2 14.40
Direct heat integration of independent processes.
Jian Wen, *Xiao Feng, Guilian Liu, Li Wang, Zaoxiao Zhang, Jihua Chen1, Bin Wang1, Kai Wu1
(Xi'an Jiaotong Univ., CN; 1Lanzhou Pet. Proc. Chem. Complex, CN)
[195]
H2.3 14.55
Alternative energy-saving structures for distillation and hybrid separation processes.
*E. Rev, Z. Fonyo
(Tech. Univ., Budapest, HU)
[212]
H2.4 15.10
Effect of heat losses in energy integration.
*V. Vaclavek, V. Briza
(Inst. Chem. Technol., Praha, CZ)
[42]
H2.5 15.25
A new methodology for simultaneous optimization of capital and operating cost targets in heat exchanger network design.
*H. K. Shethna, J. M. Jezowski, F. J. L. Castillo
(Hyprotech Ltd., Calgary, CA)
[1101]
H2.6 15.40
Loop breaking in heat exchanger networks by mathematical programming.
*J. Jezowski, R. Bochenek, A. Jezowska
(Rzeszow Univ. Technol., PL)
[122]
H2.7 15.55
Studies on water use in beet sugar factories.
*K. Urbaniec, J. Wernik
(Warsaw Univ. Technol., Plock, PL)
[1160]
H2.8 16.10
Towards an efficient water management strategy: Vito's integrated approach.
*D. Baetens, R. A. Tainsh1
(Vito, Mol, BE; 1Linnhoff March Ltd., Northwich, UK)
[607]
H2.9 16.25
VOC emission- "end of pipe" and process integration approach.
*J. Vlasakova, V. Vaclavek
(Inst. Chem. Technol., Praha, CZ)
[43]
H3.1 9.30
Keynote lecture:
Understanding the limitations of modeling and simulation.
*M. Shacham, N. Brauner1
(Ben Gurion Univ. Negev, Beer Sheva, IL; 1Tel-Aviv Univ., IL)
[1323]
H3.2 10.00
Optimisation of the ammonia-hydrogensulfide circulation scrubbing process (AS-Process) using reverse osmosis membrane.
*O. Brettschneider, H. Thielert1, J. Mayer, G. Wozny
(Tech. Univ. Berlin, DE; 1THYSSEMKRUPP, Bochum, DE)
[1047]
H3.3 10.25
MINLP-Optimization of product recovery from rinsing waters.
*F. Beuster, B. Goers, A. Lehmann, G. Wozny
(Tech. Univ. Berlin, DE)
[1048]
H3.4 10.50
Heat exchanger network optimization with discontinuous exchanger cost function.
K. Y. Cheung, *C. W. Hui
(Hong Kong Univ. Sci. Technol., Hong Kong, CN)
[168]
H3.5 11.15
Optimization of industrial process water systems.
*A. Lassahn, G. Gruhn
(Tech. Univ. Hamburg-Harburg, DE)
[188]
H3.6 11.40
Multistream heat exchanger network synthesis.
*Lee Ming Pua, F. Zhu
(UMIST, Manchester, UK)
[1079]
H3.7 12.05
Enhancement prediction and extrapolation properties of hybrid neural network model.
C. Benqlilou, D. Ruiz, A. Espuna, *L. Puigjaner
(Univ. Polit. Catalunya, Barcelona, ES)
[1172]
H4.1 14.00
Keynote lecture:
Molecular modelling and plant-wide optimisation.
X. X. Zhu
(UMIST, Manchester, UK)
[1014]
H4.2 14.40
Process integration retrofit by structural analysis.
*M. Amidpour, D. Rashtchian
(Iranian R & D Cent. Chem. Ind., Tehran, IR)
[291]
H4.3 15.05
Applying column targeting technique for the separation section of ethylene process.
*M. A. Al-Otaibi, M. Soliman, A. Adris
(SABIC, Riyadh, SA)
[326]
H4.4 15.30
Considering range and precision of data in model reduction.
N. Brauner, *M. Shacham1
(Tel-Aviv Univ., IL; 1Ben Gurion Univ. Negev, Beer-Sheva, IL)
[1324]
H4.5 15.55
Synthesis and optimization of membrane networks.
R. Uppaluri, *A. C. Kokossis
(UMIST, Manchester, UK)
[1148]
H4.6 16.20
Match constraints in heat exchanger network syntheses.
M. Amidpour
(Iranian R & D Cent. Chem. Ind., Tehran, IR)
[290]
H5.1 9.30
Keynote lecture:
High performances reboilers applied to the oil and gas processing industries.
B. Thonon
(CEA-Grenoble, FR)
[269]
H5.2 10.10
Objective fuctions for optimization problems in the process industry.
G. A. Efthimeros, Z. G. Diamantis, D. I. Photeinos, *D. T. Tsahalis
(Univ. Patras, GR)
[12]
H5.3 10.35
Process integration analysis and retrofit of the crude oil distillation unit heat exchanger network in an oil refinery.
*D. Fernandez-Polanco, J. Klemes, V. Plesu1
(UMIST, Manchester, UK; 1Univ. Politehnica, Bucuresti, RO)
[1039]
H5.4 11.00
Rigorous MINLP model for ethanol dehydration system.
*Z. Szitkai, Z. Lelkes, E. Rev, Z. Fonyo
(Tech. Univ., Budapest, HU)
[211]
H5.5 11.25
Unit for thermal treatment of gas wastes.
*R. Stulir, V. Fabikovic, J. Oral1, P. Stehlik
(Tech. Univ. Brno, CZ; 1EVECO Brno, CZ)
[983]
H5.6 11.50
Estimation of energy saving potential of industrial sites with methods of process integration.
L. L. Tovazhnyansky, *P. A. Kapustenko, L. M. Uliev
(Kharkiv State Polytech. Univ., UA)
[189]
H6.1 14.00
Keynote lecture:
Different strategies to improve industrial heat exchange.
*V. V. Wadekar, P. Stehlik1
(HTFS, AEA Technol., Harwell, UK; 1Tech. Univ. Brno, CZ)
[982]
H6.2 14.40
Design and control of energy efficient multicomponent distillations.
M. Serra, M. Perrier1, A. Espuna, *L. Puigjaner
(Univ. Polit. Catalunya, Barcelona, ES; 1Ec. Polytech. Montreal, CA)
[55]
H6.3 15.00
Combinatorial framework for the algorithmic synthesis of azeotropic-distillation systems.
*B. Bertok, F. Friedler, G. Feng1, L. T. Fan1
(Univ. Veszprem, HU; 1Kansas State Univ., Manhattan KS, US)
[1203]
H6.4 15.20
Integration of fault diagnosis and reactive scheduling in batch chemical plants.
D. Ruiz, J. Canton, J. M. Nougues, A. Espuna, *L. Puigjaner
(Univ. Polit. Catalunya, Barcelona, ES)
[1394]
H6.5 15.40
Integrated synthesis of combined process and heat exchanger networks.
*A. B. Nagy, G. Biros, F. Friedler, L. T. Fan1
(Univ. Veszprem, HU; 1Kansas State Univ., Manhattan KS, US)
[1205]
H6.6 16.00
Optimisation and energy saving in the separation of a mixture containing n-pentane and i-pentane.
R. M. Dragomir, *V. Plesu, A. Platon1, G. Constantinescu2
(Univ. Politehnica, Bucuresti, RO; 1SNP-Petrom, Bucuresti, RO; 2SNP-Petrom, Brazi, RO)
[1218]
H6.7 16.20
End product quality control in batch reactors using automatic and statistical process control techniques.
B. Alakent, *M. C. Camurdan
(Bogazici Univ., Istanbul, TR)
[662]
H7.1 9.30
Keynote lecture:
Energy integration with inherent flexibility.
L. Tantimuratha, D. K. Antonopoulos, *A. C. Kokossis
(UMIST, Manchester, UK)
[1146]
H7.2 10.10
Flexibility analysis and steady-state optimizing control of a deep-cut turboexpander plant with flexible energy integration.
K. Uygun, A. E. S. Konukman1, *U. Akman
(Bogazici Univ., Istanbul, TR; 1Gebze Inst. Technol., Kocaeli, TR)
[552]
H7.3 10.35
Multiperiod synthesis of heat-exchanger networks with period-specific structural flexibilities through superstructure-based simultaneous MILP formulation.
*A. E. S. Konukman, U. Akman1
(Gebze Inst. Technol., Kocaeli, TR; 1Bogazici Univ., Istanbul, TR)
[578]
H7.4 11.00
Simultaneous MILP synthesis with flexibility targeting of minimum-utility heat-exchanger networks and minimum-cost flexible retrofit design.
*A. E. S. Konukman, M. C. Camurdan1, U. Akman1
(Gebze Inst. Technol., Kocaeli, TR; 1Bogazici Univ., Istanbul, TR)
[581]
H7.5 11.25
Energy-resource-saving optimal control of simple controllers.
Yu. L. Muromtsev, L. P. Orlova, *V. M. Tyutyunnik1
(Tambov State Tech. Univ., RU; 1Int. Inf. Nobel Centre, Tambov, RU)
[62]
H7.6 11.50
Development of an in-situ continuous monitoring system for pure water.
*D. J. Kukulka, R. E. Baier, J. C. Mollendorf
(State Univ. New York, Buffalo, NY, US)
[84]
H8.1 14.00
Keynote lecture:
A sequential framework for optimal synthesis of industrial size heat exchanger networks.
*T. Gundersen, A. Hashemi-Ahmady1, J. M. Zamora2, I. E. Grossmann3
(Norwegian Univ. Sci. Technol., Trondheim, NO; 1Statoil, Stavanger, NO; 2Univ. Aut. Metrop., Iztapalapa, MX; 3Carnegie Mellon Univ., Pittsburg, US)
[953]
H8.2 14.40
Keynote lecture:
The role of equilibrium thermodynamics in process synthesis.
*M. Sorin, B. Spinner1
(CANMET, Varennes Que, CA; 1CNRS, Perpignan, FR)
[154]
H8.3 15.10
Compact multifunctional heat exchangers.
B. Thonon
(CEA-Grenoble, FR)
[455]
H8.4 15.35
Heat-integrated distillation columns sequencing pitfalls.
P. Lenfeld
(UNIPETROL Kaucuk, Kralupy n/Vlt., CZ)
[6]
H8.5 16.00
Design and synthesis of distillation sequences for the separation of multicomponent azeotropic mixtures.
*S. K. Wasylkiewicz, F. J. L. Castillo
(AEA Technol. Eng. Software, Calgary, CA)
[1100]
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