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| LEADER |
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220111s2022 xx o 000 0 eng d |
| 005 |
20220613175750.4 |
| 035 |
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|a (FlBoTFG)9780203746769
|
| 040 |
|
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|a OCoLC-P
|b eng
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|c OCoLC-P
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| 020 |
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|a 9780203746769
|q (electronic bk.)
|
| 020 |
|
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|a 0203746767
|q (electronic bk.)
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| 020 |
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|a 9781351430678
|q (electronic bk. : PDF)
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| 020 |
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|a 135143067X
|q (electronic bk. : PDF)
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| 020 |
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|a 9781351430654
|q (electronic bk. : Mobipocket)
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| 020 |
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|a 1351430653
|q (electronic bk. : Mobipocket)
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| 020 |
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|z 9782881248832
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| 020 |
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|a 9781351430661
|q (electronic bk. : EPUB)
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| 020 |
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|a 1351430661
|q (electronic bk. : EPUB)
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| 024 |
7 |
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|a 10.1201/9780203746769
|2 doi
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| 035 |
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|a (OCoLC)1291627943
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| 035 |
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|a (OCoLC-P)1291627943
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| 050 |
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4 |
|a TP157
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| 082 |
0 |
4 |
|a 660/.2995
|2 23
|
| 100 |
1 |
|
|a Elnashaie, S. S. E. H.,
|d 1947-
|
| 245 |
1 |
0 |
|a Modelling, simulation, and optimization of industrial fixed bed catalytic reactors /
|c S.S.E.H. Elnashaie and S.S. Elshishini.
|
| 250 |
|
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|a First edition.
|
| 264 |
|
1 |
|a [Place of publication not identified] :
|b Routledge,
|c 2022.
|
| 300 |
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|a 1 online resource (478 pages).
|
| 336 |
|
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|a text
|b txt
|2 rdacontent
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| 337 |
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|a computer
|b c
|2 rdamedia
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| 338 |
|
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|a online resource
|b cr
|2 rdacarrier
|
| 490 |
0 |
|
|a Topics in chemical engineering ;
|v v. 7
|
| 505 |
2 |
|
|a Ch. 1. Systems Theory and Principles for Developing Mathematical Models of Industrial Fixed Bed Catalytic Reactors -- Ch. 2. Chemisorption and Catalysis -- Ch. 3. Intrinsic Kinetics of Gas-Solid Catalytic Reactions -- Ch. 4. Practical Relevance of Bifurcation, Instability and Chaos in Catalytic Reactors -- Ch. 5. Effect of Diffusional Resistances. The Single Pellet Problem -- Ch. 6. The Overall Reactor Models -- Ch. 7. The Catalyst Deactivation Problem -- Appendix A Physico-Chemical Parameters for Industrial Steam Reformers -- Appendix B Numerical Techniques for the Solution of Equations Arising in the Modelling of Industrial Fixed Bed Catalytic Reactors -- Appendix C Application of the Collocation Method to the Catalyst Deactivation Problem -- Appendix D Maximum Principle for the Heterogeneous Model. (The Catalyst Deactivation Problem, Chapter 7).
|
| 520 |
|
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|a Mathematical modelling of gas-solid catalytic reactors in industry is still limited. By consolidating progress in the understanding of catalytic processes, this book applies fundamental advances to the development of models for design, simulation and optimization of industrial reactors.
|
| 588 |
|
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|a OCLC-licensed vendor bibliographic record.
|
| 650 |
|
0 |
|a Chemical reactors.
|
| 650 |
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0 |
|a Catalysis.
|
| 655 |
|
7 |
|a Electronic books.
|2 local
|
| 700 |
1 |
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|a Elshishini, S. S.,
|d 1946-
|
| 710 |
1 |
|
|a Taylor & Francis.
|
| 730 |
0 |
|
|a MATHnetBASE.
|
| 856 |
4 |
0 |
|u http://proxy.library.tamu.edu/login?url=https://www.taylorfrancis.com/books/9780203746769
|z Connect to the full text of this electronic book
|t 0
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|
| 952 |
f |
f |
|a Texas A&M University
|b College Station
|c Electronic Resources
|s www_evans
|d Available Online
|t 0
|e TP157
|h Library of Congress classification
|
| 998 |
f |
f |
|a TP157
|t 0
|l Available Online
|