Estimation and analysis of the influence of interfacial gradients in a fixed bed adiabatic catalytic reactor
The influence of the interfacial gradients on the performance of a fixed bed adiabatic catalytic reactor cannot generally be determined only at the reactor inlet conditions because the magnitude of the gradients vary along the reactor. A very simple method for the estimation from inlet conditions of...
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| Formato: | Capítulo de libro |
| Lenguaje: | Inglés |
| Publicado: |
1983
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| Acceso en línea: | Registro en Scopus DOI Handle Registro en la Biblioteca Digital |
| Aporte de: | Registro referencial: Solicitar el recurso aquí |
| LEADER | 04181caa a22005537a 4500 | ||
|---|---|---|---|
| 001 | PAPER-18332 | ||
| 003 | AR-BaUEN | ||
| 005 | 20230518204942.0 | ||
| 008 | 190411s1983 xx ||||fo|||| 00| 0 eng|d | ||
| 024 | 7 | |2 scopus |a 2-s2.0-0020845273 | |
| 040 | |a Scopus |b spa |c AR-BaUEN |d AR-BaUEN | ||
| 100 | 1 | |a Martinez, O.M. | |
| 245 | 1 | 0 | |a Estimation and analysis of the influence of interfacial gradients in a fixed bed adiabatic catalytic reactor |
| 260 | |c 1983 | ||
| 270 | 1 | 0 | |m Lemcoff, N.O.; Department of Chemical Engineering, University of Houston, Houston, TX 77004, United States |
| 506 | |2 openaire |e Política editorial | ||
| 504 | |a Bischoflf, K.B., (1965) AlChE J, 11, p. 351 | ||
| 504 | |a Carberry, J.J., (1966) Ind. Eng. Chem, 58, p. 40 | ||
| 504 | |a Froment, G.F., Bischoff, K.B., Chemical Reaction Analysis and Design (1979), J. Wiley, New York; Giger, G., Mutharasan, R., Coughanowr, D., (1980) Ind. Eng. Chem. Fund, 19, p. 389 | ||
| 504 | |a Gonzo, E.E., Gottifredi, J.C., Ildas. Jornadas Argentinas sobre Catálisis (1981), Salta, Argentina; Gottifredi, J.C., Gonzo, E.E., Quiroga, O.D., (1981) Chem. Eng. Sci, 36, pp. 705-713 | ||
| 504 | |a Hlavacek, V., Kubicek, M., (1970) Chem. Eng. Sci, 25, p. 1537 | ||
| 504 | |a Lee, J.C.M., Luss, D., (1969) Ind. Eng. Chem, Fund, 8, p. 597 | ||
| 504 | |a Liu, S.L., (1970) AlChE J, 16, p. 742 | ||
| 504 | |a Liu, S.L., Amundson, N.R., (1963) Ind. Eng. Chem. Fund, 2, p. 183 | ||
| 504 | |a Mc Greavy, C., Cresswell, D.L., (1969) Can. J. Chem. Eng, 47, p. 583 | ||
| 504 | |a Mears, D.E., (1971) J. Cat, 20, p. 127 | ||
| 504 | |a Mears, D.E., (1971) Ind. Eng. Chem. Proc. Des. Dev, 10, p. 541 | ||
| 504 | |a Mercer, M.C., Aris, R., (1971) Lat. Am. J. Chem. Eng. Appl. Chem, 2, p. 149 | ||
| 504 | |a Minhas, S., Carberry, J.J., (1969) Brit. Chem. Eng, 14, p. 799 | ||
| 504 | |a Paspek, S., Varma, A., (1980) Chem. Eng. Sci, 35, p. 33 | ||
| 504 | |a Sharma, C.S., Hughes, R., (1979) Chem. Eng. Sci, 34, p. 613 | ||
| 504 | |a Sinkule, J., Votruba, J., Hlavacek, V., Hofmann, H., (1976) Chem. Eng. Sci, 31, p. 23 | ||
| 504 | |a Votruba, J., Kubicek, M., Hlavacek, V., (1974) Chem. Eng. Sci, 29, p. 2333 | ||
| 520 | 3 | |a The influence of the interfacial gradients on the performance of a fixed bed adiabatic catalytic reactor cannot generally be determined only at the reactor inlet conditions because the magnitude of the gradients vary along the reactor. A very simple method for the estimation from inlet conditions of the maximum interfacial temperature gradient is developed. A very good agreement with values obtained from the numerical solution of the balance equations is found. An analysis of the relative importance of the interfacial concentration and temperature gradients is also carried out. A parameter Lm, that is a good measure of the influence of each one of these gradients in the reactor, is introduced. © 1983, Taylor & Francis Group, LLC. All rights reserved. |l eng | |
| 593 | |a Departamento de Ingenieria Quimica, Universidad Nacional de La Plata, 1 y 47, 1900 La Plata, Argentina | ||
| 593 | |a PINMATE, Departamento de Industrias, Universidad de Buenos Aires, Ciudad Universitaria, 1428 Buenos Aires, Argentina | ||
| 690 | 1 | 0 | |a CHEMICAL REACTIONS |
| 690 | 1 | 0 | |a MASS TRANSFER |
| 690 | 1 | 0 | |a MATHEMATICAL MODELS |
| 690 | 1 | 0 | |a CHEMICAL EQUIPMENT |
| 700 | 1 | |a Lemcoff, N.O. | |
| 773 | 0 | |d 1983 |g v. 23 |h pp. 363-378 |k n. 4-6 |p Chem. Eng. Commun. |x 00986445 |w (AR-BaUEN)CENRE-4150 |t Chemical Engineering Communications | |
| 856 | 4 | 1 | |u https://www.scopus.com/inward/record.uri?eid=2-s2.0-0020845273&doi=10.1080%2f00986448308940485&partnerID=40&md5=28e2bda689d455afd1a974d57045aa81 |y Registro en Scopus |
| 856 | 4 | 0 | |u https://doi.org/10.1080/00986448308940485 |y DOI |
| 856 | 4 | 0 | |u https://hdl.handle.net/20.500.12110/paper_00986445_v23_n4-6_p363_Martinez |y Handle |
| 856 | 4 | 0 | |u https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00986445_v23_n4-6_p363_Martinez |y Registro en la Biblioteca Digital |
| 961 | |a paper_00986445_v23_n4-6_p363_Martinez |b paper |c PE | ||
| 962 | |a info:eu-repo/semantics/article |a info:ar-repo/semantics/artículo |b info:eu-repo/semantics/publishedVersion | ||
| 999 | |c 79285 | ||