nr |
titel |
auteur |
tijdschrift |
jaar |
jaarg. |
afl. |
pagina('s) |
type |
1 |
A case study in process engineering tool integration
|
Ballinger, Geoffrey H. |
|
|
19 |
S1 |
p. 759-764 |
artikel |
2 |
A discrete-event simulation approach for scheduling batch processes
|
Baudet, P. |
|
|
19 |
S1 |
p. 633-638 |
artikel |
3 |
A formal representation of process model equations
|
Bogusch, R |
|
|
19 |
S1 |
p. 211-216 |
artikel |
4 |
A framework for investigating schedule robustness under uncertainty
|
Mignon, D.J. |
|
|
19 |
S1 |
p. 615-620 |
artikel |
5 |
A general environment for steady state process simulation structure and main features.
|
Alliet, M. |
|
|
19 |
S1 |
p. 259-264 |
artikel |
6 |
Agent-based approach to a design support system for the synthesis of continuous chemical processes
|
Chonghun, Han |
|
|
19 |
S1 |
p. 63-69 |
artikel |
7 |
Aggregate modelling of multipurpose plant operation
|
Wilkinson, S.J. |
|
|
19 |
S1 |
p. 583-588 |
artikel |
8 |
A local optimization method for the design of reactive distillation
|
Pekkanen, Martti |
|
|
19 |
S1 |
p. 235-240 |
artikel |
9 |
A MINLP strategy for the debottlenecking problem in an ethane extraction plant
|
Diaz, S. |
|
|
19 |
S1 |
p. 175-180 |
artikel |
10 |
A modular approach to synthesis of cleaner processes
|
Flower, J.R. |
|
|
19 |
S1 |
p. 45-50 |
artikel |
11 |
Analysis of controlled technological systems using high level petri nets
|
Gerzson, M. |
|
|
19 |
S1 |
p. 531-536 |
artikel |
12 |
An approach to on-line optimization of chemical plants
|
Zhang, Zejun |
|
|
19 |
S1 |
p. 305-310 |
artikel |
13 |
A new design method for segmentally baffled heat exchangers
|
Reppich, M. |
|
|
19 |
S1 |
p. 137-142 |
artikel |
14 |
An extended cutting plane method for solving convex MINLP problems
|
Westerlund, Tapio |
|
|
19 |
S1 |
p. 131-136 |
artikel |
15 |
An integrated computer aided system for integrated design and control of chemical processes
|
Gong, Jianping |
|
|
19 |
S1 |
p. 489-494 |
artikel |
16 |
An object-oriented environment for queries and analysis of thermodynamic properties of compounds and mixtures
|
Uhlemann, Jens |
|
|
19 |
S1 |
p. 715-720 |
artikel |
17 |
Application of data-reconciliation and optimisation procedure to hydrogen plant
|
Bussani, G. |
|
|
19 |
S1 |
p. 299-304 |
artikel |
18 |
Application of Markov chains in deriving for predicting the dynamic behaviour of chemical engineering processes
|
Gutsche, R. |
|
|
19 |
S1 |
p. 729-734 |
artikel |
19 |
A process synthesis modelling framework based on mass/heat transfer module hyperstructure
|
Papalexandri, Katerina P. |
|
|
19 |
S1 |
p. 71-76 |
artikel |
20 |
A prototype KBS for recipe management in batch chemical processes
|
Wang, B.G. |
|
|
19 |
S1 |
p. 657-662 |
artikel |
21 |
A standard interface for use of thermodynamics in process simulation
|
Fieg, G. |
|
|
19 |
S1 |
p. 317-320 |
artikel |
22 |
A study of gross error detection and data reconciliation in process industries
|
Yang, Youqi |
|
|
19 |
S1 |
p. 217-222 |
artikel |
23 |
Author index
|
|
|
|
19 |
S1 |
p. V-VI |
artikel |
24 |
Automated synthesis of HENs using block decomposition and heuristic rules
|
Zhu, Xin X. |
|
|
19 |
S1 |
p. 155-160 |
artikel |
25 |
Automatic Differentiation applications to computer aided process engineering
|
Mischler, C. |
|
|
19 |
S1 |
p. 779-784 |
artikel |
26 |
AZEOPERT - A heuristic-numeric system for the prediction of azeotrope formation
|
Schembecker, Gerhard |
|
|
19 |
S1 |
p. 253-258 |
artikel |
27 |
Azeotropic batch distillation new problems and some solutions
|
Watsont, Stuart |
|
|
19 |
S1 |
p. 589-596 |
artikel |
28 |
Back-off calculations in optimising control: A dynamic approach
|
Bahri, P.A. |
|
|
19 |
S1 |
p. 699-708 |
artikel |
29 |
Bimap - a tool for computer aided modeling in chemical reaction engineering
|
Dieterich, E.E. |
|
|
19 |
S1 |
p. 773-778 |
artikel |
30 |
Biomass estimation and optimal control of the baker's yeast fermentation process
|
Beluhan, D. |
|
|
19 |
S1 |
p. 387-392 |
artikel |
31 |
Case-based reasoning system for mixing equipment selection
|
Kraslawski, A. |
|
|
19 |
S1 |
p. 821-826 |
artikel |
32 |
Chemical plant fault diagnosis through a hybrid symbolic- connectionist approach and comparison with neural networks
|
Özyurt, B. |
|
|
19 |
S1 |
p. 753-758 |
artikel |
33 |
Combined processes in multicomponent fluid systems: Simulation and design
|
Kenig, E.Ya. |
|
|
19 |
S1 |
p. 287-292 |
artikel |
34 |
Combined process synthesis and simulation system for feasibility studies
|
Hurme, Markku |
|
|
19 |
S1 |
p. 663-668 |
artikel |
35 |
Comparative analysis of various heat pump schemes applied to C4 splitters
|
Fonyo, Z. |
|
|
19 |
S1 |
p. 1-6 |
artikel |
36 |
Computer integrated management: An industrlal perspective on the future
|
Benson, Professor Roger S |
|
|
19 |
S1 |
p. 543-551 |
artikel |
37 |
Controllability analysis and modelling requirements: an industrial example
|
Walsh, Stephen |
|
|
19 |
S1 |
p. 369-374 |
artikel |
38 |
Controllability and operability of azeotropic heterogeneous distillation systems
|
Rovaglio, M. |
|
|
19 |
S1 |
p. 525-530 |
artikel |
39 |
Cost effective operator training
|
Stawarz, A.C. |
|
|
19 |
S1 |
p. 459-464 |
artikel |
40 |
Data reconciliation based on elemental balances applied to batch experiments
|
Fillon, M. |
|
|
19 |
S1 |
p. 293-298 |
artikel |
41 |
Dedication
|
Glavič, P. |
|
|
19 |
S1 |
p. xi |
artikel |
42 |
Design and control of batch reactors
|
Friedrich, M. |
|
|
19 |
S1 |
p. 357-368 |
artikel |
43 |
Design and operation of a batch distillation column with a middle vessel
|
Meski, George A. |
|
|
19 |
S1 |
p. 597-602 |
artikel |
44 |
Designing pressure relief equipment for a batch reactor
|
Brown-Brulant, D. |
|
|
19 |
S1 |
p. 537-542 |
artikel |
45 |
Design of a neural controller by inverse modelling
|
Dirion, J.L. |
|
|
19 |
S1 |
p. 797-802 |
artikel |
46 |
Design of multiproduct batch plants with uncertain demands
|
Ierapetritou, M.G. |
|
|
19 |
S1 |
p. 627-632 |
artikel |
47 |
Design of procedural controllers for chemical processes
|
Sanchez, A. |
|
|
19 |
S1 |
p. 381-386 |
artikel |
48 |
Design of reaction/separation networks using detailed models
|
Smith, E.M.B. |
|
|
19 |
S1 |
p. 83-88 |
artikel |
49 |
Development and application of problem specific “local” process simulators in cape
|
Jensen, Anne Krogh |
|
|
19 |
S1 |
p. 311-316 |
artikel |
50 |
Development of an advanced modelling environment
|
Maguire, P.Z. |
|
|
19 |
S1 |
p. 265-270 |
artikel |
51 |
Development of a process synthesizer in a modular environment
|
Reneaume, J.M. |
|
|
19 |
S1 |
p. 33-38 |
artikel |
52 |
Different operational policies for the batch extractive distillation
|
Lang, P. |
|
|
19 |
S1 |
p. 645-650 |
artikel |
53 |
Dispatching-like strategies using intermediate storage for the scheduling of batch chemical processes
|
Graells, M. |
|
|
19 |
S1 |
p. 621-626 |
artikel |
54 |
Dynamic model of a system with phase- and reaction equilibrium
|
Moe, H.I. |
|
|
19 |
S1 |
p. 513-518 |
artikel |
55 |
Dynamic process diagnosis via integrated neural networks
|
Tsai, Chii-Shang |
|
|
19 |
S1 |
p. 747-752 |
artikel |
56 |
Dynamic simulation of a distillation column with multiple liquid phases
|
Eckert, E. |
|
|
19 |
S1 |
p. 393-398 |
artikel |
57 |
Dynamic simulation of a NDBEPR activated sludge process
|
Ducato, R. |
|
|
19 |
S1 |
p. 441-446 |
artikel |
58 |
Dynamic simulation of a PVC suspension reactor
|
Dimian, A. |
|
|
19 |
S1 |
p. 427-432 |
artikel |
59 |
Effects of equipment failure uncertainty in batch production scheduling
|
Sanmartí, Eduard |
|
|
19 |
S1 |
p. 565-570 |
artikel |
60 |
Efficient simulation of periodic cycled reactor operation
|
Santiago Jr., W. |
|
|
19 |
S1 |
p. 483-488 |
artikel |
61 |
Eliciting expert knowledge; a study on connectionist approach for building a cognitive model of process design
|
Alha, M.K. |
|
|
19 |
S1 |
p. 809-814 |
artikel |
62 |
Energetic optimization of distillations in hybrid processes
|
Glanz, S. |
|
|
19 |
S1 |
p. 51-56 |
artikel |
63 |
Environmental considerations in batch production scheduling
|
Grau, Raimon |
|
|
19 |
S1 |
p. 651-656 |
artikel |
64 |
Evaluation of design flexibility in distillation columns using rigorous models
|
Hoch, Patricia M. |
|
|
19 |
S1 |
p. 669-674 |
artikel |
65 |
Evaluation of the dynamic behavior of an extractive distillation column for dehydration of aqueous ethanol mixtures
|
Maciel, M.R.Wolf |
|
|
19 |
S1 |
p. 405-408 |
artikel |
66 |
Flow of information through an artificial neural network
|
Guimarãaes, P.R.B. |
|
|
19 |
S1 |
p. 741-746 |
artikel |
67 |
Further developments in chemical plant cost estimating using fuzzy matching
|
Petley, G.J. |
|
|
19 |
S1 |
p. 675-680 |
artikel |
68 |
Generation and assessment of batch processes with ecological considerations
|
Linninger, Andreas A. |
|
|
19 |
S1 |
p. 7-13 |
artikel |
69 |
Incorporating on-line scheduling strategies in integrated batch production control
|
Huercio, A. |
|
|
19 |
S1 |
p. 609-614 |
artikel |
70 |
Industrial realization of time-optimal strategies for product changeover operations of coupled distillation columns
|
Kruse, Ch. |
|
|
19 |
S1 |
p. 603-608 |
artikel |
71 |
Integrated crude distillation design
|
Liebmann, K. |
|
|
19 |
S1 |
p. 119-124 |
artikel |
72 |
Integrated synthesis of a process and its fault-tolerant control system
|
Hangos, K.M. |
|
|
19 |
S1 |
p. 465-470 |
artikel |
73 |
Intelligent workstation for immediate decision helping in process supervision: A new paradigm ?
|
Mille, A |
|
|
19 |
S1 |
p. 815-820 |
artikel |
74 |
Issues in solving large scale planning, design and scheduling problems in batch chemical plants
|
Subrahmanyam, Sriram |
|
|
19 |
S1 |
p. 577-582 |
artikel |
75 |
Keyword index
|
|
|
|
19 |
S1 |
p. I-IV |
artikel |
76 |
Life cycle assessment and linear programming environmental optimisation of product system-
|
Azapagic, A. |
|
|
19 |
S1 |
p. 229-234 |
artikel |
77 |
Mathematical modeling of liquid - liquid equlibria in aqueous polymer solution containing neutral proteinase and oxytetracycline using artificial neural network
|
Bogdan, S. |
|
|
19 |
S1 |
p. 791-796 |
artikel |
78 |
Minimizing the environmental impact of process Plants: A process systems methodology
|
Stefanis, S.K. |
|
|
19 |
S1 |
p. 39-44 |
artikel |
79 |
Minimum energy requirement of distillation processes
|
Offers, H. |
|
|
19 |
S1 |
p. 247-252 |
artikel |
80 |
Mixed-integer nonlinear programming techniques for process systems engineering
|
Grossmann, Ignacio E. |
|
|
19 |
S1 |
p. 189-204 |
artikel |
81 |
Model based control of a multipurpose batch reactor - an experimental study
|
Liu, Z.H. |
|
|
19 |
S1 |
p. 477-482 |
artikel |
82 |
Model identification of batch crystallization processes
|
Livk, I. |
|
|
19 |
S1 |
p. 241-246 |
artikel |
83 |
Modelling and simulation of the operation of an industrial batch plant using gPROMS
|
Winkel, M.L. |
|
|
19 |
S1 |
p. 571-576 |
artikel |
84 |
Modelling and sizing of gas-solid chilling machines
|
Hermes, H.D. |
|
|
19 |
S1 |
p. 333-338 |
artikel |
85 |
Modified Integral Procedure (MIP) as a reliable short-cut method in mechanistic based ODE kinetic model estimation : Non-isothermal and (semi-)batch process cases
|
Maria, Gheorghe |
|
|
19 |
S1 |
p. 709-714 |
artikel |
86 |
Monitoring and control of hydrometallurgical processes with self-organizing and adaptive neural net systems
|
Aldrich, C |
|
|
19 |
S1 |
p. 803-808 |
artikel |
87 |
Moving finite elements method applied to the solution of front reaction models: causticizing reaction
|
Duarte, B.P.M. |
|
|
19 |
S1 |
p. 421-426 |
artikel |
88 |
Multiple steady states in heterogeneous azeotropic distillation
|
Bekiaris, Nikolaos |
|
|
19 |
S1 |
p. 21-26 |
artikel |
89 |
Multiplicity in reactive distillation of MTBE
|
Hauan, S. |
|
|
19 |
S1 |
p. 327-332 |
artikel |
90 |
Nonideal distillation in automated synthesis
|
Matias, T.R.Senos |
|
|
19 |
S1 |
p. 57-62 |
artikel |
91 |
Nonlinear dynamics of isothermal CMSMPR crystallizers: A simulation study
|
Lakatos, Béla G. |
|
|
19 |
S1 |
p. 501-506 |
artikel |
92 |
Nonlinear model-based control of a binary distillation column
|
Trotta, Antonio |
|
|
19 |
S1 |
p. 519-524 |
artikel |
93 |
Numerical simulation of extraction columns using a drop population model
|
Kronberger, T. |
|
|
19 |
S1 |
p. 639-644 |
artikel |
94 |
Optimal control under environmental considerations application to a pharmaceutical synthesis reaction
|
Cezerac, J. |
|
|
19 |
S1 |
p. 415-420 |
artikel |
95 |
Optimal design of continuous sterilisation networks
|
Samsatli, N.J. |
|
|
19 |
S1 |
p. 95-100 |
artikel |
96 |
Optimal design of controllable heat-exchanger networks under multi-directional resiliency-target constraints
|
Konukman, Alp Er Ş. |
|
|
19 |
S1 |
p. 149-154 |
artikel |
97 |
Optimal operation of an ethylene plant at variable feed conditions
|
Eliceche, Ana M. |
|
|
19 |
S1 |
p. 223-228 |
artikel |
98 |
Optimisation of animal cell culture media using dynamic simulation
|
Sanderson, C.S. |
|
|
19 |
S1 |
p. 681-686 |
artikel |
99 |
Parametric study of separation network synthesis: Extreme properties of optimal structures
|
Kovacs, Z. |
|
|
19 |
S1 |
p. 107-112 |
artikel |
100 |
Performance of different regulators for plants with recycle
|
Scali, C. |
|
|
19 |
S1 |
p. 409-414 |
artikel |
101 |
Phenomenon driven process design methodology: Focus on reactive distillation
|
Tanskanen, Juha |
|
|
19 |
S1 |
p. 77-82 |
artikel |
102 |
Preface
|
Glavič, P. |
|
|
19 |
S1 |
p. xiii-xiv |
artikel |
103 |
Pressure analysis of the ethylene cold-end process
|
Castillo, Francisco J.L. |
|
|
19 |
S1 |
p. 89-94 |
artikel |
104 |
Pressure swing adsorption - optimization of a trace separation system
|
Kvamsdal, H.M. |
|
|
19 |
S1 |
p. 339-344 |
artikel |
105 |
Preventive maintenance policy optimization for multipurpose plant equipment
|
Dedopoulos, I.T. |
|
|
19 |
S1 |
p. 693-698 |
artikel |
106 |
Process dynamics and temperature control of fed-batch reactors
|
Szeifert, F. |
|
|
19 |
S1 |
p. 447-452 |
artikel |
107 |
Process modelling for design, commissioning and operational analysis
|
Goldfarb, Stewart |
|
|
19 |
S1 |
p. 433-439 |
artikel |
108 |
Programmed cooling control of a batch crystallizer
|
Vega, A. |
|
|
19 |
S1 |
p. 471-476 |
artikel |
109 |
Qualitative modelling of chemical processes - a weighted digraph (WDG) approach
|
Vianna, R.F. |
|
|
19 |
S1 |
p. 375-380 |
artikel |
110 |
Qualitative process modelling - a fuzzy signed directed graph method
|
Wang, X.Z. |
|
|
19 |
S1 |
p. 735-740 |
artikel |
111 |
Reinitialization of DAE's after discontinuities
|
Majer, C. |
|
|
19 |
S1 |
p. 507-512 |
artikel |
112 |
Risk assessment: an object oriented tool for the rapid evaluation of liquid spill potential and loss prevention
|
Struthers, A. |
|
|
19 |
S1 |
p. 453-458 |
artikel |
113 |
Safe design of industrial multitubular fixed bed reactors based on parametric sensitivity studies
|
Baptista, Cristina M.S.G. |
|
|
19 |
S1 |
p. 125-130 |
artikel |
114 |
Separation of azeotropic mixtures by batch distillation using an entrainer
|
Düssel, R. |
|
|
19 |
S1 |
p. 113-118 |
artikel |
115 |
Simulation and optimization of a set of catalytic reactors used for dehydrogenation of butene into butadiene
|
Borio, D.O. |
|
|
19 |
S1 |
p. 345-350 |
artikel |
116 |
Simulation model of wet flue gas desulphurization plant
|
Gerbec, M. |
|
|
19 |
S1 |
p. 283-286 |
artikel |
117 |
Simulation of tubular reactors packed with large-pore catalysts with spherical geometry
|
Quinta-Ferreira, Rosa M. |
|
|
19 |
S1 |
p. 351-356 |
artikel |
118 |
Simultaneous heat and mass transfer model for spray tower design: Application on VOCs removal
|
Meyer, M. |
|
|
19 |
S1 |
p. 277-282 |
artikel |
119 |
Simultaneous solution and MINLP synthesis of DAE process problems: PFR networks in overall processes.
|
Pahor, B. |
|
|
19 |
S1 |
p. 181-188 |
artikel |
120 |
Some new approaches for the control of a distillation column and their experimental evaluation on a pilot plant
|
Maiti, Sachi N. |
|
|
19 |
S1 |
p. 399-404 |
artikel |
121 |
Steady state process simulation on MIMD machines:Solving nonlinear equations
|
Paloschi, Jorge R. |
|
|
19 |
S1 |
p. 721-728 |
artikel |
122 |
Study on optimization of operation for multipurpose batch chemical plants with multiple production routes
|
Wang, Yiping |
|
|
19 |
S1 |
p. 101-106 |
artikel |
123 |
Synthesis and analysis of processes with electrolyte mixtures
|
Thomsen, Kaj |
|
|
19 |
S1 |
p. 27-32 |
artikel |
124 |
Synthesis and optimization of distillation sequences for the separation of azeotropic mixtures
|
Bauer, M.H. |
|
|
19 |
S1 |
p. 15-20 |
artikel |
125 |
Synthesis of batch reaction/distillation processes using detailed dynamic models
|
Charalambides, M.S. |
|
|
19 |
S1 |
p. 167-174 |
artikel |
126 |
Synthesis of reactor networks with multiple multicomponent feeds
|
Bikić, D. |
|
|
19 |
S1 |
p. 161-166 |
artikel |
127 |
The numerical simulation of non-linear separation columns by boundary-domain integral formulation
|
Žagar, I. |
|
|
19 |
S1 |
p. 785-790 |
artikel |
128 |
The placement of two-stream and multi-stream heat-exchangers in an existing network through path analysis
|
van Reisen, Jos L.B. |
|
|
19 |
S1 |
p. 143-148 |
artikel |
129 |
The pointer federal distributed data management system for integrating process engineering
|
Das, B.P. |
|
|
19 |
S1 |
p. 321-326 |
artikel |
130 |
The sequential linear quadratic programming algorithm for solving dynamic optimization problems - a review.
|
Støren, Sverre |
|
|
19 |
S1 |
p. 495-500 |
artikel |
131 |
The visbreaking process simulation: products amount and their properties prediction
|
Dente, M. |
|
|
19 |
S1 |
p. 205-210 |
artikel |
132 |
Towards the incorporation of flexibility, maintenance and safety in process design
|
Thomaidis, T.V. |
|
|
19 |
S1 |
p. 687-692 |
artikel |
133 |
Uncertainty in process design and operations
|
Pistikopoulos, E.N. |
|
|
19 |
S1 |
p. 553-563 |
artikel |
134 |
User interfaces for mathematical programming based multipurpose plant optimisation systems
|
Shah, N. |
|
|
19 |
S1 |
p. 765-772 |
artikel |
135 |
Using constraint propagation to a user to acquire data for a simulation program
|
Boudiba, M. |
|
|
19 |
S1 |
p. 271-276 |
artikel |