Zobrazeno 1 - 10
of 29
pro vyhledávání: '"Prokopis Pladis"'
Autor:
Costas Kiparissides, Prokopis Pladis
Publikováno v:
The Canadian Journal of Chemical Engineering. 100:714-730
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2b0775f6def8ec82ab12f6f0895364b9
https://doi.org/10.1002/cjce.24262
https://doi.org/10.1002/cjce.24262
Autor:
Costas Kiparissides, Prokopis Pladis
Publikováno v:
Industrial & Engineering Chemistry Research. 58:13093-13111
A segregation–backmixing model is developed to simulate the dynamic operation of multifeed high-pressure low-density polyethylene (LDPE) autoclaves, calculate the specific initiator consumption (gr...
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::658ca9a93a865c92c032159c663081fa
https://doi.org/10.1021/acs.iecr.9b02517
https://doi.org/10.1021/acs.iecr.9b02517
Publikováno v:
Industrial & Engineering Chemistry Research. 53:7352-7364
In the present study a comprehensive model is employed to describe the dynamic behavior of an industrial scale reactor for the emulsion polymerization of vinylidene fluoride (VDF) under different initiator and chain transfer agent (CTA) addition poli
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1dffea68dcec87c67f5a811dc733cb2f
https://doi.org/10.1021/ie403548m
https://doi.org/10.1021/ie403548m
Publikováno v:
Macromolecular Reaction Engineering. 8:392-405
Summary A multi-phase, multi-zone mathematical model is developed to describe the dynamic operation of an industrial high-pressure flash separator for a ternary (Ethylene–Vinyl acetate–EVA) system. The proposed description of the high-pressure se
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::3c576ac3bc80f8c070f5e2d82abcfcaf
https://doi.org/10.1002/mren.201300169
https://doi.org/10.1002/mren.201300169
Publikováno v:
Macromolecular Reaction Engineering. 5:479-489
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8e7ff4bda3a10d35ca0b05b3385a2478
https://doi.org/10.1002/mren.201100025
https://doi.org/10.1002/mren.201100025
Publikováno v:
Chemical Engineering & Technology. 33:1754-1766
A generalized multiscale modeling framework is described for the digital simulation of a high-pressure low-density polyethylene (LDPE) tubular reactor. According to the proposed modeling approach, various models describing the complex physical and ch
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::896ecc896932ef1ee5cb6d7bfb7d04a3
https://doi.org/10.1002/ceat.201000325
https://doi.org/10.1002/ceat.201000325
Modeling and simulation of an industrial slurry-phase catalytic olefin polymerization reactor series
Autor:
P. Van-Grambezen, D. Mignon, Vassileios Kanellopoulos, Costas Kiparissides, V. Touloupides, Prokopis Pladis
Publikováno v:
Chemical Engineering Science. 65:3208-3222
In the present study, a comprehensive mathematical model is developed to simulate the dynamic behaviour of an industrial slurry-phase olefin catalytic polymerization loop reactor series. More specifically, the effects of various operating conditions
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::9308f7a9972a64afc5e56c5c4e631bc6
https://doi.org/10.1016/j.ces.2010.02.014
https://doi.org/10.1016/j.ces.2010.02.014
Publikováno v:
Macromolecular Reaction Engineering. 4:303-318
A new software has been developed for the simulation, design, parameter and state estimation, optimization, and control of specific polymerization processes aiming at increasing plant efficiency, improving product quality, and reducing the impact to
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0c9046bdf870114f877574128cc1185e
https://doi.org/10.1002/mren.200900053
https://doi.org/10.1002/mren.200900053
Publikováno v:
Macromolecular Theory and Simulations. 17:478-487
A model is developed to predict the viscoelastic behavior of polyolefins produced in catalytic polymerization reactors. The approach is based on the solution of different sub-models (e.g., a kinetic model, a single particle model, a macroscopic react
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::359171232eae4f6c81a0db998ee27546
https://doi.org/10.1002/mats.200800047
https://doi.org/10.1002/mats.200800047