nr |
titel |
auteur |
tijdschrift |
jaar |
jaarg. |
afl. |
pagina('s) |
type |
1 |
A comparative analysis of the trickle-bed and the monolithic reactor for three-phase hydrogenations
|
Edvinsson, R.K. |
|
1994 |
49 |
24P2 |
p. 5653-5666 14 p. |
artikel |
2 |
A computational snapshot of gas—liquid flow in baffled stirred reactors
|
Ranade, V.V. |
|
1994 |
49 |
24P2 |
p. 5175-5192 18 p. |
artikel |
3 |
A generalized mixing model for initial contacting of reactive fluids
|
Villermaux, Jacques |
|
1994 |
49 |
24P2 |
p. 5127-5140 14 p. |
artikel |
4 |
A lumped kinetic model for liquid-phase catalytic oxidation ofp-xylene to terephthalic acid
|
Cao, Giacomo |
|
1994 |
49 |
24P2 |
p. 5775-5788 14 p. |
artikel |
5 |
A method for assessing thermal stability of batch reactors by sensitivity calculation based on Lyapunov exponents: experimental verification
|
Strozzi, F. |
|
1994 |
49 |
24P2 |
p. 5549-5561 13 p. |
artikel |
6 |
A novel circulating cross-flow moving bed reactor system for gas—solids contacting
|
Wolff, E.H.P. |
|
1994 |
49 |
24P2 |
p. 5427-5438 12 p. |
artikel |
7 |
A novel hydrazine oxidation technique for the determination ofk L a in gas—liquid and gas—liquid—solid reactors
|
Lara Ma´rquez, Alejandro |
|
1994 |
49 |
24P2 |
p. 5667-5679 13 p. |
artikel |
8 |
A novel kinetic model discrimination method: eigenfunction distribution via forced concentration oscillation
|
Tan, Hui |
|
1994 |
49 |
24P2 |
p. 5563-5569 7 p. |
artikel |
9 |
A novel reverse flow strategy for ethylbenzene dehydrogenation in a packed-bed reactor
|
Snyder, Jon D. |
|
1994 |
49 |
24P2 |
p. 5585-5601 17 p. |
artikel |
10 |
Application of a new exergy analysis method to a flow reversal SO2 convertor
|
Sorin, M. |
|
1994 |
49 |
24P2 |
p. 5603-5613 11 p. |
artikel |
11 |
A unified approach to the scale-up of gas—solid fluidized bed and gas—liquid bubble column reactors
|
Ellenberger, J. |
|
1994 |
49 |
24P2 |
p. 5391-5411 21 p. |
artikel |
12 |
Author index
|
|
|
1994 |
49 |
24P2 |
p. I-II nvt p. |
artikel |
13 |
Autocatalytic continuous reactions in a stirred tank: I. Multiplicity of steady states
|
Aris, Rutherford |
|
1994 |
49 |
24P2 |
p. 5307-5313 7 p. |
artikel |
14 |
Catalytic honeycomb reactors with electrical heating
|
Pinkas, Pavel |
|
1994 |
49 |
24P2 |
p. 5347-5358 12 p. |
artikel |
15 |
Catalytic oxidation ofn-propanol in a multiphase upflow reactor: surface tension effects
|
Mazzarino, I. |
|
1994 |
49 |
24P2 |
p. 5699-5707 9 p. |
artikel |
16 |
Chemical reactions under ultrasound: discrimination of chemical and physical effects
|
Contamine, F. |
|
1994 |
49 |
24P2 |
p. 5865-5873 9 p. |
artikel |
17 |
Circulating reaction zones in a packed-bed loop reactor
|
Lauschke, Go¨tz |
|
1994 |
49 |
24P2 |
p. 5359-5375 17 p. |
artikel |
18 |
Combined reaction and separation in pressure swing processes
|
Alpay, E. |
|
1994 |
49 |
24P2 |
p. 5845-5864 20 p. |
artikel |
19 |
Computer generated reaction networks: on-the-fly calculation of species properties using computational quantum chemistry
|
Broadbelt, Linda J. |
|
1994 |
49 |
24P2 |
p. 4991-5010 20 p. |
artikel |
20 |
Contribution of different turbulent scales to mixing and reaction between unpremixed reactants
|
Valerio, S. |
|
1994 |
49 |
24P2 |
p. 5159-5174 16 p. |
artikel |
21 |
Control of the ignited steady state in autothermal fixed-bed reactors for catalytic combustion
|
Nieken, Ulrich |
|
1994 |
49 |
24P2 |
p. 5507-5518 12 p. |
artikel |
22 |
Drop size distributions in high holdup fraction dispersion systems: effect of the degree of hydrolysis of PVA stabilizer
|
Chatzi, E.G. |
|
1994 |
49 |
24P2 |
p. 5039-5052 14 p. |
artikel |
23 |
Effect of scale on liquid recirculation in bubble columns
|
Kumar, Sailesh B. |
|
1994 |
49 |
24P2 |
p. 5637-5652 16 p. |
artikel |
24 |
Effects of Macromixing on the oregonator model of the belousov — zhabotinsky reaction in a stirred reactor
|
Hsu, T.J. |
|
1994 |
49 |
24P2 |
p. 5291-5305 15 p. |
artikel |
25 |
Emulsion copolymerization in continuous loop reactors
|
Abad, Carlos |
|
1994 |
49 |
24P2 |
p. 5025-5037 13 p. |
artikel |
26 |
Emulsion polymerization in various reactor types: recipes with high monomer contents
|
Mayer, M.J.J. |
|
1994 |
49 |
24P2 |
p. 4971-4980 10 p. |
artikel |
27 |
Fixed bed reactor design for gas phase chain reactions catalysed by solids: the oxidative coupling of methane
|
Hoebink, J.H.B.J. |
|
1994 |
49 |
24P2 |
p. 5453-5463 11 p. |
artikel |
28 |
Flow maldistributions and hot spots in down-flow packed bed reactors
|
Nguyen, Duyen |
|
1994 |
49 |
24P2 |
p. 5489-5505 17 p. |
artikel |
29 |
Gas—liquid flow in bubble columns and loop reactors: Part I. Detailed modelling and numerical simulation
|
Sokolichin, A. |
|
1994 |
49 |
24P2 |
p. 5735-5746 12 p. |
artikel |
30 |
Gas—liquid flow in bubble columns and loop reactors: Part II. Comparison of detailed experiments and flow simulations
|
Becker, S. |
|
1994 |
49 |
24P2 |
p. 5747-5762 16 p. |
artikel |
31 |
Heat transfer and the continuous production of hydroxypropyl starch in a static mixer reactor
|
Lammers, Gerard |
|
1994 |
49 |
24P2 |
p. 5097-5107 11 p. |
artikel |
32 |
Hydrodynamic modelling of circulating fluidised beds
|
Niewland, J.J. |
|
1994 |
49 |
24P2 |
p. 5803-5811 9 p. |
artikel |
33 |
Investigations of periodically operated trickle-bed reactors
|
Lange, R. |
|
1994 |
49 |
24P2 |
p. 5615-5621 7 p. |
artikel |
34 |
Kinetics of melt polymerization of maleic acid phthalic acids with propylene glycol
|
Salmi, T. |
|
1994 |
49 |
24P2 |
p. 5053-5070 18 p. |
artikel |
35 |
Kinetics of nitrate reduction in monolith reactor
|
Wa¨rn«, J. |
|
1994 |
49 |
24P2 |
p. 5763-5773 11 p. |
artikel |
36 |
Mass transfer in tubular reactors equipped with static mixers
|
Turunen, I. |
|
1994 |
49 |
24P2 |
p. 5257-5269 13 p. |
artikel |
37 |
Mechanisms of structure formation during combustion synthesis of materials
|
Rogachev, A.S. |
|
1994 |
49 |
24P2 |
p. 4949-4958 10 p. |
artikel |
38 |
Methanol to olefins—prediction of the performance of a circulating fluidized-bed reactor on the basis of kinetic experiments in a fixed-bed reactor
|
Schoenfelder, Hendrik |
|
1994 |
49 |
24P2 |
p. 5377-5390 14 p. |
artikel |
39 |
Methodologies for the design of reactors using structured catalysts: Modelling and experimental study of diffusion and reaction in structured catalysts
|
McGreavy, C. |
|
1994 |
49 |
24P2 |
p. 5413-5425 13 p. |
artikel |
40 |
Micromixing and memory in chemical reactors
|
Guida, Vincenzo |
|
1994 |
49 |
24P2 |
p. 5215-5228 14 p. |
artikel |
41 |
Mixing, reaction and precipitation: an interplay in continuous crystallizers
|
Tavare, N.S. |
|
1994 |
49 |
24P2 |
p. 5193-5201 9 p. |
artikel |
42 |
Modeling of a multistage high-pressure ethylene polymerization reactor
|
Gu Kwag, Byung |
|
1994 |
49 |
24P2 |
p. 4959-4969 11 p. |
artikel |
43 |
Modeling of light scattering in photochemical reactors
|
Alfano, Orlando M. |
|
1994 |
49 |
24P2 |
p. 5327-5346 20 p. |
artikel |
44 |
Modelling the increased gas capacity of self-inducing impellers
|
Forrester, S.E. |
|
1994 |
49 |
24P2 |
p. 5709-5718 10 p. |
artikel |
45 |
On-line optimization of a high-pressure low-density polyethylene tubular reactor
|
Kiparissides, C. |
|
1994 |
49 |
24P2 |
p. 5011-5024 14 p. |
artikel |
46 |
Operating and hydrodynamic characteristics of a cocurrent downflow bubble column reactor
|
Lu, Xiao-Xiong |
|
1994 |
49 |
24P2 |
p. 5719-5733 15 p. |
artikel |
47 |
Optimal operation strategies to control the molecular weight distribution of polymer products
|
Maschio, G. |
|
1994 |
49 |
24P2 |
p. 5071-5086 16 p. |
artikel |
48 |
Particle-aided chemical vapor deposition (PACVD) of silicon carbide composites
|
Zhao, G.Y. |
|
1994 |
49 |
24P2 |
p. 4917-4938 22 p. |
artikel |
49 |
Patterns due to convection—diffusion—reaction interaction in a fixed-bed catalytic reactor
|
Sheintuch, Moshe |
|
1994 |
49 |
24P2 |
p. 5315-5326 12 p. |
artikel |
50 |
PDF simulation of a turbulent series—parallel reaction in an axisymmetric reactor
|
Tsai, Kuochen |
|
1994 |
49 |
24P2 |
p. 5141-5158 18 p. |
artikel |
51 |
Pressure drop and liquid holdup in high pressure trickle-bed reactors
|
Al-Dahhan, Muthanna H. |
|
1994 |
49 |
24P2 |
p. 5681-5698 18 p. |
artikel |
52 |
Pyrolysis of biomass in the rotating cone reactor: modelling and experimental justification
|
Wagenaar, B.M. |
|
1994 |
49 |
24P2 |
p. 5109-5126 18 p. |
artikel |
53 |
Rate of solids and gas transfer via an orifice between partially and completely fluidized beds
|
Korbee, R. |
|
1994 |
49 |
24P2 |
p. 5819-5832 14 p. |
artikel |
54 |
Reaction kinetics for the hydrolysis of tributyrin using an immobilized bacterial lipase
|
Warmuth, W. |
|
1994 |
49 |
24P2 |
p. 5087-5095 9 p. |
artikel |
55 |
Reactive mixing in a tubular jet reactor: a comparison of PDF simulations with experimental data
|
Pipino, Massimo |
|
1994 |
49 |
24P2 |
p. 5229-5241 13 p. |
artikel |
56 |
Reactor modeling and scale-up of a multiphase reaction—extraction system: metallothermic reduction of rare earth oxides
|
Cho, Byong K. |
|
1994 |
49 |
24P2 |
p. 5439-5452 14 p. |
artikel |
57 |
Runaway in packed bed reactors operating with periodic flow reversal
|
Purwono, S. |
|
1994 |
49 |
24P2 |
p. 5473-5487 15 p. |
artikel |
58 |
Simultaneous shift reaction and carbon dioxide separation for the direct production of hydrogen
|
Han, Chun |
|
1994 |
49 |
24P2 |
p. 5875-5883 9 p. |
artikel |
59 |
Start-up and safeguarding of an industrial adiabatic tubular reactor
|
Verwijs, J.W. |
|
1994 |
49 |
24P2 |
p. 5519-5532 14 p. |
artikel |
60 |
Stochastic analysis of the local velocity gradient in a trickle-bed reactor
|
Latifi, M.A. |
|
1994 |
49 |
24P2 |
p. 5281-5289 9 p. |
artikel |
61 |
Studies of transport of asphaltenes through porous membranes: statistical structural models and continuum hydrodynamic theories
|
Ravi-Kumar, V.S. |
|
1994 |
49 |
24P2 |
p. 5789-5801 13 p. |
artikel |
62 |
Styrene maleic anhydride copolymerization in a recycle tubular reactor: reactor stability and product quality
|
Belkhiria, Sahbi |
|
1994 |
49 |
24P2 |
p. 4981-4990 10 p. |
artikel |
63 |
Synthesis and evaluation of titania powders for photodestruction of phenol
|
Fotou, George P. |
|
1994 |
49 |
24P2 |
p. 4939-4948 10 p. |
artikel |
64 |
The fluidized bed membrane reactor system: a pilot scale experimental study
|
Adris, A.M. |
|
1994 |
49 |
24P2 |
p. 5833-5843 11 p. |
artikel |
65 |
The origin of fine drops in batch gas-agitated liquid—liquid systems
|
Shahrokhi, H. |
|
1994 |
49 |
24P2 |
p. 5203-5213 11 p. |
artikel |
66 |
The production of vapor grown carbon fibers from a mixture of benzene, toluene and xylene using the liquid pulse injection technique
|
Mukai, S.R. |
|
1994 |
49 |
24P2 |
p. 4909-4916 8 p. |
artikel |
67 |
The simulated moving bed chemical reactor
|
Haynes, Thomas N. |
|
1994 |
49 |
24P2 |
p. 5465-5472 8 p. |
artikel |
68 |
The use of large scale computer assisted tomography for the study of hydrodynamics in trickling filters
|
Toye, D. |
|
1994 |
49 |
24P2 |
p. 5271-5280 10 p. |
artikel |
69 |
Transient flow structure in the entrance region of a bubble column using particle image velocimetry
|
Reese, J. |
|
1994 |
49 |
24P2 |
p. 5623-5636 14 p. |
artikel |
70 |
Two phase cluster model in riser reactors: impact of radial density distribution on yields
|
Fligner, M. |
|
1994 |
49 |
24P2 |
p. 5813-5818 6 p. |
artikel |
71 |
Uncertainty issues in the modeling and optimization of batch reactors with tendency models
|
Fotopoulos, Jake |
|
1994 |
49 |
24P2 |
p. 5533-5547 15 p. |
artikel |
72 |
Visualization of the concentration profiles in the entrance section of a fixed bed catalytic reactor—premixing of two gaseous components
|
Mewes, D. |
|
1994 |
49 |
24P2 |
p. 5243-5255 13 p. |
artikel |
73 |
Wrong-way behavior in packed-bed reactors with “large-pore” catalysts
|
Almeida-Costa, Cristina A. |
|
1994 |
49 |
24P2 |
p. 5571-5583 13 p. |
artikel |