Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids
A modified bubble coalescence model including rheological conditions and shear forces in non-Newtonian fluids is evaluated using CFD (Computational Fluid Dynamics). Euler's model, along with population balance equations, was used to simulate bubble size distribution. Simultaneously, different b...
- Autores:
-
Niño, Lilibeth
Peñuela Vásquez, Mariana
Gelves, German
- Tipo de recurso:
- Article of journal
- Fecha de publicación:
- 2021
- Institución:
- Universidad Francisco de Paula Santander
- Repositorio:
- Repositorio Digital UFPS
- Idioma:
- eng
- OAI Identifier:
- oai:repositorio.ufps.edu.co:ufps/6534
- Acceso en línea:
- https://repositorio.ufps.edu.co/handle/ufps/6534
- Palabra clave:
- Break up
Coalescence
Coulaloglou
Non-Newtonian fluids
- Rights
- openAccess
- License
- Copyright ©2006-2022 by: School of Engineering. Taylor’s University
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Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| title |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| spellingShingle |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids Break up Coalescence Coulaloglou Non-Newtonian fluids |
| title_short |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| title_full |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| title_fullStr |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| title_full_unstemmed |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| title_sort |
Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids |
| dc.creator.fl_str_mv |
Niño, Lilibeth Peñuela Vásquez, Mariana Gelves, German |
| dc.contributor.author.none.fl_str_mv |
Niño, Lilibeth Peñuela Vásquez, Mariana Gelves, German |
| dc.contributor.corporatename.spa.fl_str_mv |
Journal of Engineering Science and Technology |
| dc.subject.proposal.eng.fl_str_mv |
Break up Coalescence Coulaloglou Non-Newtonian fluids |
| topic |
Break up Coalescence Coulaloglou Non-Newtonian fluids |
| description |
A modified bubble coalescence model including rheological conditions and shear forces in non-Newtonian fluids is evaluated using CFD (Computational Fluid Dynamics). Euler's model, along with population balance equations, was used to simulate bubble size distribution. Simultaneously, different bubble breakage and coalescence models were evaluated to investigate mass transfer and bubble diameter. A conventional aeration stirring system (Rushton turbine, ring sparger) was used and the results were validated by determining the experimental mass transfer coefficient. A 10-liter bioreactor operated under different operating conditions commonly used for non-Newtonian rheology was used. Xanthan Gum 0.25% was used to resemble the rheological conditions developed during fungal culture. CFD results were contrasted with tested data obtained from ������ measurements at different stirring speeds using the concordance d-index. A reasonable prediction was obtained comparing the modified model Luo-New to the most used conventional models Luo-Luo and Laakkonen-Luo. Therefore, model Luo-New shows the highest d values at 400-700 rpm with values of 0.83, 0.95, 0.98 and 0.69. By contrast, the model Luo-Luo showed less inaccurate values with levels lower than 0.62 in almost all comparisons. The latter concludes numerically that the inclusion of viscosity effects and shear on a bubble coalescence model improves the degree of prediction related to oxygen transfer. The latter being a critical factor in the design and testing of stirring and aeration devices. |
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2021 |
| dc.date.issued.none.fl_str_mv |
2021-08 |
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2022-11-18T14:04:21Z |
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2022-11-18T14:04:21Z |
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Artículo de revista |
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http://purl.org/coar/resource_type/c_2df8fbb1 |
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http://purl.org/coar/version/c_970fb48d4fbd8a85 |
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http://purl.org/coar/resource_type/c_6501 |
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Text |
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info:eu-repo/semantics/article |
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http://purl.org/redcol/resource_type/ART |
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https://repositorio.ufps.edu.co/handle/ufps/6534 |
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https://repositorio.ufps.edu.co/handle/ufps/6534 |
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eng |
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eng |
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Journal of Engineering Science and Technology. Vol.16 N°.4. (2021) |
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Vol.16 No.4.(2021) |
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3198 |
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4 |
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3185 |
| dc.relation.citationvolume.spa.fl_str_mv |
16 |
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NIÑO, L., PEÑUELA, M., & GELVES, G. (2021). Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids. Journal of Engineering Science and Technology, 16(4), 3185-3198. |
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Journal of Engineering Science and Technology |
| dc.rights.eng.fl_str_mv |
Copyright ©2006-2022 by: School of Engineering. Taylor’s University |
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http://purl.org/coar/access_right/c_abf2 |
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https://creativecommons.org/licenses/by/4.0/ |
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info:eu-repo/semantics/openAccess |
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Copyright ©2006-2022 by: School of Engineering. Taylor’s University https://creativecommons.org/licenses/by/4.0/ http://purl.org/coar/access_right/c_abf2 |
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openAccess |
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14 páginas |
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application/pdf |
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Journal of Engineering Science and Technology |
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Malasia |
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https://jestec.taylors.edu.my/Vol%2016%20Issue%204%20August%202021/16_4_30.pdf |
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Niño, Lilibethfe424d07e145b419adb1d1597b49fd4f600Peñuela Vásquez, Mariana088289d4c3609f816116c1f50a6151ec600Gelves, German7446587450ae5fc4984fae3331a66538600Journal of Engineering Science and Technology2022-11-18T14:04:21Z2022-11-18T14:04:21Z2021-08https://repositorio.ufps.edu.co/handle/ufps/6534A modified bubble coalescence model including rheological conditions and shear forces in non-Newtonian fluids is evaluated using CFD (Computational Fluid Dynamics). Euler's model, along with population balance equations, was used to simulate bubble size distribution. Simultaneously, different bubble breakage and coalescence models were evaluated to investigate mass transfer and bubble diameter. A conventional aeration stirring system (Rushton turbine, ring sparger) was used and the results were validated by determining the experimental mass transfer coefficient. A 10-liter bioreactor operated under different operating conditions commonly used for non-Newtonian rheology was used. Xanthan Gum 0.25% was used to resemble the rheological conditions developed during fungal culture. CFD results were contrasted with tested data obtained from ������ measurements at different stirring speeds using the concordance d-index. A reasonable prediction was obtained comparing the modified model Luo-New to the most used conventional models Luo-Luo and Laakkonen-Luo. Therefore, model Luo-New shows the highest d values at 400-700 rpm with values of 0.83, 0.95, 0.98 and 0.69. By contrast, the model Luo-Luo showed less inaccurate values with levels lower than 0.62 in almost all comparisons. The latter concludes numerically that the inclusion of viscosity effects and shear on a bubble coalescence model improves the degree of prediction related to oxygen transfer. The latter being a critical factor in the design and testing of stirring and aeration devices.14 páginasapplication/pdfengJournal of Engineering Science and TechnologyMalasiaJournal of Engineering Science and Technology. Vol.16 N°.4. (2021)Vol.16 No.4.(2021)31984318516NIÑO, L., PEÑUELA, M., & GELVES, G. (2021). Bubble coalescence model effect on oxygen mass transfer using non-newtonian fluids. Journal of Engineering Science and Technology, 16(4), 3185-3198.Journal of Engineering Science and TechnologyCopyright ©2006-2022 by: School of Engineering. Taylor’s Universityhttps://creativecommons.org/licenses/by/4.0/info:eu-repo/semantics/openAccesshttp://purl.org/coar/access_right/c_abf2https://jestec.taylors.edu.my/Vol%2016%20Issue%204%20August%202021/16_4_30.pdfBubble coalescence model effect on oxygen mass transfer using non-newtonian fluidsArtículo de revistahttp://purl.org/coar/resource_type/c_6501http://purl.org/coar/resource_type/c_2df8fbb1Textinfo:eu-repo/semantics/articlehttp://purl.org/redcol/resource_type/ARTinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/version/c_970fb48d4fbd8a85Break upCoalescenceCoulaloglouNon-Newtonian fluidsLehr, F.; Millies, M.; and Mewes, D. (2004). Bubble-size distributions and flow fields in bubble columns. American Institute of Chemical Engineering, 48(11), 2426-2443.Karimi, A.; Golbabaei, F.; Mehrnia, M.R.; Neghab, M.; Mohammad, K.; Nikpey, A.; and Pourmand, M.R. (2013). Oxygen mass transfer in a stirred tank bioreactor using different impeller configurations for environmental purposes. Iranian Journal of Environmental Health Science and Engineering, 10(1), 1-6.Amaral, P.F.F.; Freire, M.G.; Rocha-Leão, M.H.M.; Marrucho, I.M.; Coutinho, J.A.P.; and Coelho, M.A.Z. (2008). Optimization of oxygen mass transfer in a multiphase bioreactor with perfluorodecalin as a second liquid phase. Biotechnology and Bioengineering, 99(3), 588-598.Nino, L.; Gelves, R.; Ali, H.; Solsvik, J.; and Jakobsen, H. (2020). Applicability of a modified breakage and coalescence model based on the complete turbulence spectrum concept for CFD simulation of gas-liquid mass transfer in a stirred tank reactor. Chemical Engineering Science, 211, 52-72.Alopaeus, V.; Koskinen, J.; and Keskinen, K.I. (1999) Simulation of the population balances for liquid-liquid systems in a nonideal stirred tank. Part 1 description and qualitative validation of the model. Chemical Engineering Science, 54(24), 5887-5899.Moilanen, P. (2009). Modeling gas-liquid flow and local mass transfer in stirred tanks. Doctoral dissertation, Helsinki University of Technology.Jenne, M.; and Reuss, M. (1999). A critical assessment on the use of k-ε turbulence models for simulation of the turbulent liquid flow induced by Rushton turbine in baffled stirred-tank reactors. Chemical Engineering Science, 54(17), 3921-3941.Luo, J.Y.; Issa, R.I.; and Gosman, A.D. (1994). Prediction of impeller induced flows in mixing vessels using multiple frames of reference. Proceedings of the 8th European Conference on Mixing. Cambridge, United Kingdom, 549-556.Micale, G.; Brucato, A.; Grisafi, F.; and Ciofalo,M. (1999). Prediction of flow fields in a dual-impeller stirred vessel. American Institute of Chemical Engineering, 45(3), 445-464.Tabor, G.; Gosman, A.D.; and Issa, R.I. (1996). Numerical simulation of the flow in a mixing vessel stirred by a Rushton turbine. Institute of Chemical Engineering, 32, 352-356.Rutherford, K.; Lee, K.C.; Mahmoudi, S.M.S.; and Yianneskis, M. (1996) Hydrodynamic characteristics of dual Rushton impeller stirred vessels. American Institute of Chemical Engineering, 42(2), 332-346.Bakker, A.; and Akker, H.E.A.V.D. (1994). A computational model for the gas-liquid flow in stirred reactors. Chemical Engineering Research and Design, 72(A4), 573-582.Kerdouss, F.; Bannari, A.; Proulx, P.; Bannari, R.; Skrga, M.; and Labrecque, Y. (2008). Two-phase mass transfer coefficient prediction in a stirred vessel with a CFD model. Computers and Chemical Engineering, 32(8), 1943-1955.Kerdouss, F.; Kiss, L.; Proulx, P.; Bilodeau, J.-F.; and Dupuis, C. (2005). 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World Journal of Microbiological Biotechnology, 23(5), 615-623.Gabelle J.-C.; Jourdier, E.; Licht, R.B.; Chaabane, F.B.; Henaut, I.; Morchain, J.; and Augier, F. (2012). Impact of rheology on the mass transfer coefficient during the growth phase of Trichoderma reesei in stirred bioreactors. Chemical Engineering Science, 75, 408-417.Willmott, C.J.; Steven, G.A.; Davis, R.E.; Feddema, J.J.; Klink, K.M.; Legates, D.R.; O'Donnell, J.; and Rowe, C.M. (1985). Statistics for the evaluation and comparison of models. Journal of Geophysical Research, 90(5), 8995-9005.Gelves, R.; Dietrich, A.; and Takors, R. (2014). Modeling of gas-liquid mass transfer in a stirred tank bioreactor agitated by a Rushton turbine or a new pitched blade impeller. Bioprocess and Biosystems Engineering, 37(3), 365-375.Nino, L.; Peñuela, M.; and Gelves, G.R. (2018). Gas-liquid hydrodynamics simulation using CFD in a helical ribbon impeller applied for non-newtonian fluids. International Journal of Applied Engineering Research, 13(11), 9353-9359.Politano, M.S.; Carrica, P.M.; and Balino, J.L. (2003). About bubble breakup models to predict bubble size distributions inhomogeneous flows. Chemical Engineering Communications, 190(3), 299-321.Han, M.; Sha, Z.; Laari, A.; and Koiranen, T. (2017). CFD-PBM coupled simulation of an airlift reactor with non-newtonian fluid. Oil & Gas Science and Technology, 72(5), 1-12.Hernandez, S.; Niño, L.; and Gelves, G. (2020). Simulating of Microbial Growth Scale Up in a Stirred Tank Bioreactor for Aerobic Processes using Computational Fluid Dynamics. Journal of Physics: Conference Series, 1655 1-6.Chisti, Y.; and Moo-Young, M. (1989). On the calculation of shear rate and apparent viscosity in airlift and bubble column bioreactors. Biotechnology and Bioengineering, 34(11), 1391-1392.Sanchez-Pérez, J.A.; Porcel, E.M.R.; López, J.L.C.; Sevilla, J.M.F.; and Chisti, Y. (2006). Shear rate in a stirred tank and bubble column bioreactors. Chemical Engineering Journal, 124(1-3), 1-5.Gelves, G. (2020). Simulating hydrodynamics in a Rushton turbine at different stirring velocities applied to non-Newtonian fluids. Proceedings of the 6th International Week of Science, Technology and Innovation. San José de Cúcuta, Colombia, 1-7.López, L.C.N.; Peñuela, M.; and Gelves, G. (2016). Improving of gas-liquid mass transfer in a stirred tank bioreactor: A CFD approach. International Journal of Applied Engineering. Research, 11(9), 6097-6108.Niño-López, L.C.; and Gelves-Zambrano, G.R. (2015). Simulating gas-liquid mass transfer in a spin filter bioreactor. Revista Facultad de Ingeniería, 1, 163-174.Niño-López, L.; Cárdenas, A.A.; and Zambrano, R.G. (2013). Evaluation of chemical pretreatments for enzymatic hydrolysis of lignocellulosic residues cassava (Manihot esculenta Crantz). Revista Facultad de Ingeniería, 69, 317-326.ORIGINAL16_4_30.pdf16_4_30.pdfapplication/pdf398698https://repositorio.ufps.edu.co/bitstream/ufps/6534/1/16_4_30.pdfb1e87d82e8ce173f95898f8205bb7a70MD51open accessLICENSElicense.txtlicense.txttext/plain; charset=utf-814828https://repositorio.ufps.edu.co/bitstream/ufps/6534/2/license.txt2f9959eaf5b71fae44bbf9ec84150c7aMD52open accessTEXT16_4_30.pdf.txt16_4_30.pdf.txtExtracted texttext/plain37761https://repositorio.ufps.edu.co/bitstream/ufps/6534/3/16_4_30.pdf.txtdbcc748f4bf513543a12c4b0a19d43ccMD53open accessTHUMBNAIL16_4_30.pdf.jpg16_4_30.pdf.jpgGenerated Thumbnailimage/jpeg8421https://repositorio.ufps.edu.co/bitstream/ufps/6534/4/16_4_30.pdf.jpgd98cec5af89ddeca0a1dd43852d1315cMD54open accessufps/6534oai:repositorio.ufps.edu.co:ufps/65342022-11-19 03:00:55.295An error occurred on the license name.|||https://creativecommons.org/licenses/by/4.0/open accessRepositorio Universidad Francisco de Paula 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 incorporada en las Obras Colectivas.

b.	Distribuir copias o fonogramas de las Obras, exhibirlas públicamente, ejecutarlas públicamente y/o ponerlas a disposición pública, incluyéndolas como incorporadas en Obras Colectivas, según corresponda.

c.	Distribuir copias de las Obras Derivadas que se generen, exhibirlas públicamente, ejecutarlas públicamente y/o ponerlas a disposición pública.
Los derechos mencionados anteriormente pueden ser ejercidos en todos los medios y formatos, actualmente conocidos o que se inventen en el futuro. Los derechos antes mencionados incluyen el derecho a realizar dichas modificaciones en la medida que sean técnicamente necesarias para ejercer los derechos en otro medio o formatos, pero de otra manera usted no está autorizado para realizar obras derivadas. Todos los derechos no otorgados expresamente por el Licenciante quedan por este medio reservados, incluyendo pero sin limitarse a aquellos que se mencionan en las secciones 4(d) y 4(e).

4. Restricciones.
La licencia otorgada en la anterior Sección 3 está expresamente sujeta y limitada por las siguientes restricciones:

a.	Usted puede distribuir, exhibir públicamente, ejecutar públicamente, o poner a disposición pública la Obra sólo bajo las condiciones de esta Licencia, y Usted debe incluir una copia de esta licencia o del Identificador Universal de Recursos de la misma con cada copia de la Obra que distribuya, exhiba públicamente, ejecute públicamente o ponga a disposición pública. No es posible ofrecer o imponer ninguna condición sobre la Obra que altere o limite las condiciones de esta Licencia o el ejercicio de los derechos de los destinatarios otorgados en este documento. No es posible sublicenciar la Obra. Usted debe mantener intactos todos los avisos que hagan referencia a esta Licencia y a la cláusula de limitación de garantías. Usted no puede distribuir, exhibir públicamente, ejecutar públicamente, o poner a disposición pública la Obra con alguna medida tecnológica que controle el acceso o la utilización de ella de una forma que sea inconsistente con las condiciones de esta Licencia. Lo anterior se aplica a la Obra incorporada a una Obra Colectiva, pero esto no exige que la Obra Colectiva aparte de la obra misma quede sujeta a las condiciones de esta Licencia. Si Usted crea una Obra Colectiva, previo aviso de cualquier Licenciante debe, en la medida de lo posible, eliminar de la Obra Colectiva cualquier referencia a dicho Licenciante o al Autor Original, según lo solicitado por el Licenciante y conforme lo exige la cláusula 4(c).

b.	Usted no puede ejercer ninguno de los derechos que le han sido otorgados en la Sección 3 precedente de modo que estén principalmente destinados o directamente dirigidos a conseguir un provecho comercial o una compensación monetaria privada. El intercambio de la Obra por otras obras protegidas por derechos de autor, ya sea a través de un sistema para compartir archivos digitales (digital file-sharing) o de cualquier otra manera no será considerado como estar destinado principalmente o dirigido directamente a conseguir un provecho comercial o una compensación monetaria privada, siempre que no se realice un pago mediante una compensación monetaria en relación con el intercambio de obras protegidas por el derecho de autor.

c.	Si usted distribuye, exhibe públicamente, ejecuta públicamente o ejecuta públicamente en forma digital la Obra o cualquier Obra Derivada u Obra Colectiva, Usted debe mantener intacta toda la información de derecho de autor de la Obra y proporcionar, de forma razonable según el medio o manera que Usted esté utilizando: (i) el nombre del Autor Original si está provisto (o seudónimo, si fuere aplicable), y/o (ii) el nombre de la parte o las partes que el Autor Original y/o el Licenciante hubieren designado para la atribución (v.g., un instituto patrocinador, editorial, publicación) en la información de los derechos de autor del Licenciante, términos de servicios o de otras formas razonables; el título de la Obra si está provisto; en la medida de lo razonablemente factible y, si está provisto, el Identificador Uniforme de Recursos (Uniform Resource Identifier) que el Licenciante especifica para ser asociado con la Obra, salvo que tal URI no se refiera a la nota sobre los derechos de autor o a la información sobre el licenciamiento de la Obra; y en el caso de una Obra Derivada, atribuir el crédito identificando el uso de la Obra en la Obra Derivada (v.g., "Traducción Francesa de la Obra del Autor Original," o "Guión Cinematográfico basado en la Obra original del Autor Original"). Tal crédito puede ser implementado de cualquier forma razonable; en el caso, sin embargo, de Obras Derivadas u Obras Colectivas, tal crédito aparecerá, como mínimo, donde aparece el crédito de cualquier otro autor comparable y de una manera, al menos, tan destacada como el crédito de otro autor comparable.

d.	Para evitar toda confusión, el Licenciante aclara que, cuando la obra es una composición musical:

i.	Regalías por interpretación y ejecución bajo licencias generales. El Licenciante se reserva el derecho exclusivo de autorizar la ejecución pública o la ejecución pública digital de la obra y de recolectar, sea individualmente o a través de una sociedad de gestión colectiva de derechos de autor y derechos conexos (por ejemplo, SAYCO), las regalías por la ejecución pública o por la ejecución pública digital de la obra (por ejemplo Webcast) licenciada bajo licencias generales, si la interpretación o ejecución de la obra está primordialmente orientada por o dirigida a la obtención de una ventaja comercial o una compensación monetaria privada.

ii.	Regalías por Fonogramas. El Licenciante se reserva el derecho exclusivo de recolectar, individualmente o a través de una sociedad de gestión colectiva de derechos de autor y derechos conexos (por ejemplo, los consagrados por la SAYCO), una agencia de derechos musicales o algún agente designado, las regalías por cualquier fonograma que Usted cree a partir de la obra (“versión cover”) y distribuya, en los términos del régimen de derechos de autor, si la creación o distribución de esa versión cover está primordialmente destinada o dirigida a obtener una ventaja comercial o una compensación monetaria privada.

e.	Gestión de Derechos de Autor sobre Interpretaciones y Ejecuciones Digitales (WebCasting). Para evitar toda confusión, el Licenciante aclara que, cuando la obra sea un fonograma, el Licenciante se reserva el derecho exclusivo de autorizar la ejecución pública digital de la obra (por ejemplo, webcast) y de recolectar, individualmente o a través de una sociedad de gestión colectiva de derechos de autor y derechos conexos (por ejemplo, ACINPRO), las regalías por la ejecución pública digital de la obra (por ejemplo, webcast), sujeta a las disposiciones aplicables del régimen de Derecho de Autor, si esta ejecución pública digital está primordialmente dirigida a obtener una ventaja comercial o una compensación monetaria privada.

5. Representaciones, Garantías y Limitaciones de Responsabilidad.
A MENOS QUE LAS PARTES LO ACORDARAN DE OTRA FORMA POR ESCRITO, EL LICENCIANTE OFRECE LA OBRA (EN EL ESTADO EN EL QUE SE ENCUENTRA) “TAL CUAL”, SIN BRINDAR GARANTÍAS DE CLASE ALGUNA RESPECTO DE LA OBRA, YA SEA EXPRESA, IMPLÍCITA, LEGAL O CUALQUIERA OTRA, INCLUYENDO, SIN LIMITARSE A ELLAS, GARANTÍAS DE TITULARIDAD, COMERCIABILIDAD, ADAPTABILIDAD O ADECUACIÓN A PROPÓSITO DETERMINADO, AUSENCIA DE INFRACCIÓN, DE AUSENCIA DE DEFECTOS LATENTES O DE OTRO TIPO, O LA PRESENCIA O AUSENCIA DE ERRORES, SEAN O NO DESCUBRIBLES (PUEDAN O NO SER ESTOS DESCUBIERTOS). ALGUNAS JURISDICCIONES NO PERMITEN LA EXCLUSIÓN DE GARANTÍAS IMPLÍCITAS, EN CUYO CASO ESTA EXCLUSIÓN PUEDE NO APLICARSE A USTED.

6. Limitación de responsabilidad.
A MENOS QUE LO EXIJA EXPRESAMENTE LA LEY APLICABLE, EL LICENCIANTE NO SERÁ RESPONSABLE ANTE USTED POR DAÑO ALGUNO, SEA POR RESPONSABILIDAD EXTRACONTRACTUAL, PRECONTRACTUAL O CONTRACTUAL, OBJETIVA O SUBJETIVA, SE TRATE DE DAÑOS MORALES O PATRIMONIALES, DIRECTOS O INDIRECTOS, PREVISTOS O IMPREVISTOS PRODUCIDOS POR EL USO DE ESTA LICENCIA O DE LA OBRA, AUN CUANDO EL LICENCIANTE HAYA SIDO ADVERTIDO DE LA POSIBILIDAD DE DICHOS DAÑOS. ALGUNAS LEYES NO PERMITEN LA EXCLUSIÓN DE CIERTA RESPONSABILIDAD, EN CUYO CASO ESTA EXCLUSIÓN PUEDE NO APLICARSE A USTED.

7. Término.

a.	Esta Licencia y los derechos otorgados en virtud de ella terminarán automáticamente si Usted infringe alguna condición establecida en ella. Sin embargo, los individuos o entidades que han recibido Obras Derivadas o Colectivas de Usted de conformidad con esta Licencia, no verán terminadas sus licencias, siempre que estos individuos o entidades sigan cumpliendo íntegramente las condiciones de estas licencias. Las Secciones 1, 2, 5, 6, 7, y 8 subsistirán a cualquier terminación de esta Licencia.

b.	Sujeta a las condiciones y términos anteriores, la licencia otorgada aquí es perpetua (durante el período de vigencia de los derechos de autor de la obra). No obstante lo anterior, el Licenciante se reserva el derecho a publicar y/o estrenar la Obra bajo condiciones de licencia diferentes o a dejar de distribuirla en los términos de esta Licencia en cualquier momento; en el entendido, sin embargo, que esa elección no servirá para revocar esta licencia o que deba ser otorgada , bajo los términos de esta licencia), y esta licencia continuará en pleno vigor y efecto a menos que sea terminada como se expresa atrás. La Licencia revocada continuará siendo plenamente vigente y efectiva si no se le da término en las condiciones indicadas anteriormente.

8. Varios.

a.	Cada vez que Usted distribuya o ponga a disposición pública la Obra o una Obra Colectiva, el Licenciante ofrecerá al destinatario una licencia en los mismos términos y condiciones que la licencia otorgada a Usted bajo esta Licencia.

b.	Si alguna disposición de esta Licencia resulta invalidada o no exigible, según la legislación vigente, esto no afectará ni la validez ni la aplicabilidad del resto de condiciones de esta Licencia y, sin acción adicional por parte de los sujetos de este acuerdo, aquélla se entenderá reformada lo mínimo necesario para hacer que dicha disposición sea válida y exigible.

c.	Ningún término o disposición de esta Licencia se estimará renunciada y ninguna violación de ella será consentida a menos que esa renuncia o consentimiento sea otorgado por escrito y firmado por la parte que renuncie o consienta.

d.	Esta Licencia refleja el acuerdo pleno entre las partes respecto a la Obra aquí licenciada. No hay arreglos, acuerdos o declaraciones respecto a la Obra que no estén especificados en este documento. El Licenciante no se verá limitado por ninguna disposición adicional que pueda surgir en alguna comunicación emanada de Usted. Esta Licencia no puede ser modificada sin el consentimiento mutuo por escrito del Licenciante y Usted.
0000-0002-5453-2171088289d4c3609f816116c1f50a6151ec600 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