Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model
The present study aims to assess the vapour bubble absorption into the ammonia/lithium nitrate (NH3/LiNO3) solution by using an optimized CFD model. A detailed methodology to build up the CFD model is presented, as well as its validation using experimental data. The operating conditions set correspo...
- Autores:
-
Zapata, Andrés
Amaris, Carlos
Sagastume Gutierrez, Alexis
Rodríguez, Andrés
- Tipo de recurso:
- Article of investigation
- Fecha de publicación:
- 2022
- Institución:
- Corporación Universidad de la Costa
- Repositorio:
- REDICUC - Repositorio CUC
- Idioma:
- eng
- OAI Identifier:
- oai:repositorio.cuc.edu.co:11323/12889
- Acceso en línea:
- https://hdl.handle.net/11323/12889
https://repositorio.cuc.edu.co/
- Palabra clave:
- CFD model
Absorption chiller
Ammonia
Lithium nitrate
Bubble absorber
- Rights
- openAccess
- License
- Atribución 4.0 Internacional (CC BY 4.0)
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Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| title |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| spellingShingle |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model CFD model Absorption chiller Ammonia Lithium nitrate Bubble absorber |
| title_short |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| title_full |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| title_fullStr |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| title_full_unstemmed |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| title_sort |
Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD model |
| dc.creator.fl_str_mv |
Zapata, Andrés Amaris, Carlos Sagastume Gutierrez, Alexis Rodríguez, Andrés |
| dc.contributor.author.none.fl_str_mv |
Zapata, Andrés Amaris, Carlos Sagastume Gutierrez, Alexis Rodríguez, Andrés |
| dc.subject.proposal.eng.fl_str_mv |
CFD model Absorption chiller Ammonia Lithium nitrate Bubble absorber |
| topic |
CFD model Absorption chiller Ammonia Lithium nitrate Bubble absorber |
| description |
The present study aims to assess the vapour bubble absorption into the ammonia/lithium nitrate (NH3/LiNO3) solution by using an optimized CFD model. A detailed methodology to build up the CFD model is presented, as well as its validation using experimental data. The operating conditions set corresponds to an absorption chiller driven by low-temperature heat sources such as solar energy in warm environments. Results evidenced that the Volume of Fluid and Mixture models are adequate to be used in the CFD model to predict the absorption process in the bubble absorber assessed depending on the mesh density refinement. Moreover, the heat transfer coefficient from the solution side and the absorption mass flux are the variables needed for reliable validation of the model. Finally, the absorbed flux estimated from the CFD model ranged between 3.2×10−3 kg.m−2 .s−1 and 4.4×10−3 kg.m−2 .s−1 , while the solution side heat transfer coefficient varied between 457 W.m−2 .K−1 and 786 W.m−2 .K−1 , under the conditions considered. |
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2022 |
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2022 |
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2024-04-29T14:12:51Z |
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2024-04-29T14:12:51Z |
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Artículo de revista |
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Amaris, C., Zapata, A., Sagastume, A., & Rodríguez, A. (2022). VAPOUR ABSORPTION PROCESS IN AN NH3/LINO3 BUBBLE ABSORBER USING AN OPTIMIZED CFD MODEL. Frontiers in Heat and Mass Transfer (FHMT), 19. https://doi.org/10.5098/hmt.19.33 |
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2151-8629 |
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https://hdl.handle.net/11323/12889 |
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10.5098/hmt.19.33 |
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Corporación Universidad de la Costa |
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REDICUC – Repositorio CUC |
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https://repositorio.cuc.edu.co/ |
| identifier_str_mv |
Amaris, C., Zapata, A., Sagastume, A., & Rodríguez, A. (2022). VAPOUR ABSORPTION PROCESS IN AN NH3/LINO3 BUBBLE ABSORBER USING AN OPTIMIZED CFD MODEL. Frontiers in Heat and Mass Transfer (FHMT), 19. https://doi.org/10.5098/hmt.19.33 2151-8629 10.5098/hmt.19.33 Corporación Universidad de la Costa REDICUC – Repositorio CUC |
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https://hdl.handle.net/11323/12889 https://repositorio.cuc.edu.co/ |
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eng |
| language |
eng |
| dc.relation.ispartofjournal.spa.fl_str_mv |
Frontiers in Heat and Mass Transfer |
| dc.relation.references.spa.fl_str_mv |
Aggarwal, M. K., and Agarwal, R. S. (1986). Thermodynamic properties of lithium nitrate‐ammonia mixtures. Int. J. Energy Res. 10, 59 –68. https://doi.org/10.1002/er.4440100107 Amaris, C. (2013). Intensification of NH3 bubble absorption process using advanced surfaces and carbon nanotubes for NH3/LiNO3 absorption chillers. Available at: https://www.tdx.cat/handle/10803/128504 Amaris, C., Alvarez, M. E., Vallès, M., and Bourouis, M. (2020a). Performance assessment of an NH3/LiNO3 bubble plate absorber applying a semi -empirical model and artificial neural networks. Energies 13. https://doi.org/10.3390/en13174313 Amaris, C., and Bourouis, M. (2021). Boiling process assessment for absorption heat pumps: A review. Int. J. Heat Mass Transf. 179, 121723. https://doi.org/10.1016/j.ijheatmasstransfer.2021.121723 Amaris, C., Bourouis, M., Vallès, M., Salavera, D., and Coronas, A. (2015). Thermophysical properties and heat and mass transfer of new working fluids in plate heat exchangers for absorption refrigeration systems. Heat Transf. Eng. 36. https://doi.org/10.1080/01457632.2014.923983 Amaris, C., Miranda, B. C., and Balbis -Morejón, M. (2020b). Experimental thermal performance and modelling of a waste heat recovery unit in an energy cogeneration system. Therm. Sci. Eng. Prog. 20. https://doi.org/10.1016/j.tsep.2020.100684 Amaris, C., Rodriguez, A., Sagastume, A., and Bourouis, M. (2023). Performance Assessment of a Solar/Gas Driven NH3/LiNO3 Absorption Cooling System for Malls. Lect. Notes Mech. Eng., 311 –328. https://doi.org/10.1007/978-981-19-3467-4_19 Amaris, C., Vallès, M., and Bourouis, M. (2018). Vapour absorption enhancement using passive techniques for absorption cooling/heating technologies: A review. Appl. Energy 231, 826–853. https://doi.org/10.1016/j.apenergy.2018.09.071 Anand, S., Suresh, S., Dhanuskodi, R., and Santhosh Kumar, D. (2020). Comparison of cfd and empirical models for predicting wall temperature at supercritical conditions of water. Front. Heat Mass Transf. 14. https://doi.org/10.5098/hmt.14.8 ANSYS (2013). ANSYS Fluent Theory Guide. , ed. Ansys New York, USA https://doi.org/10.1016/0140-3664(87)90311- 2 Asfand, F., Stiriba, Y., and Bourouis, M. (2015). CFD simulation to investigate heat and mass transfer processes in a membrane -based absorber for water -LiBr absorption cooling systems. Energy. https://doi.org/10.1016/j.energy.2015.08.018 Asfand, F., Stiriba, Y., and Bourouis, M. (2016). Performance evaluation of membrane -based absorbers employing H2O/(LiBr + LiI+ LiNO3+ LiCl) andH2O/(LiNO3+ KNO3+ NaNO3) as working pairs in absorption coolingsystems. Energy. https://doi.org/10.1016/j.energy.2016.08.103 Ayou, D. S., Bruno, J. C., Saravanan, R., and Coronas, A. (2013). An overview of combined absorption power and cooling cycles. Renew. Sustain. Energy Rev. 21, 728 –748. https://doi.org/10.1016/j.rser.2012.12.068 Bhagat, R. D., and Deshmukh, S. J. (2022). Numerical analysis to predict the behavior of liquid vapor slug flow in vertically placed u -shaped closed capillary tube. Front. Heat Mass Transf. 19. https://doi.org/10.5098/hmt.19.14 Cerezo, J. (2006). Estudio del proceso de absorción con amoníaco -agua en intercambiadores de placas para equipos de refrigeración por absorción. Cuenca, Y., Salavera, D., Vernet, A., Teja, A. S., and Vallès, M. (2014). Thermal conductivity of ammonia + lithium nitrate and ammonia + lithium nitrate + water solutions over a wide range of concentrations and temperatures. Int. J. Refrig. 38, 333 –340. https://doi.org/10.1016/j.ijrefrig.2013.08.010 Elperin, T., and Fominykh, A. (2003). Four stages of the simultaneous mass and heat transfer during bubble formation and rise in a bubbly absorber. Chem. Eng. Sci. 58, 3555 –3564. https://doi.org/10.1016/S0009-2509(03)00192-1 Florides, G. A., Tassou, S. A., Kalogirou, S. A., and Wrobel, L. C. (2002). Review of solar and low energy cooling technologies for buildings. Renew. Sustain. Energy Rev. 6, 557 –572. https://doi.org/10.1016/S1364-0321(02)00016-3 Haltenberger, W. (1939). Enthalpy -Concentration Charts from Vapor Pressure Data. Ind. Eng. Chem. 31, 783 –786. https://doi.org/10.1021/ie50354a032 Hosseinnia, S. M., Naghashzadegan, M., and Kouhikamali, R. (2016). CFD simulation of adiabatic water vapor absorption in large drops of water -LiBr solution. Appl. Therm. Eng. 102, 17 –29. https://doi.org/10.1016/j.applthermaleng.2016.03.144 Hosseinnia, S. M., Naghashzadegan, M., and Kouhikamali, R. (2017). CFD simulation of water vapor absorption in laminar falling film solution of water -LiBr ─ Drop and jet modes. Appl. Therm. Eng. 115, 860 –873. https://doi.org/10.1016/j.applthermaleng.2017.01.022 Kang, Y. T., Akisawa, A., and Kashiwagi, T. (2000). Analytical investigation of two different absorption modes: falling film and bubble types. Int. J. Refrig. 23, 430 –443. https://doi.org/10.1016/S0140-7007(99)00075-4 Kang, Y. T., Kashiwagi, T., and Christensen, R. N. (1998). Ammonia - water bubble absorber with a plate heat exchanger. in ASHRAE Transactions, 1565 –1575. Karima, A., Djamel, S., Ali, N., and Houari, A. (2018). CFD investigations of thermal and dynamic behaviors in a tubular heat exchanger with butterfly baffles. Front. Heat Mass Transf. 10. https://doi.org/10.5098/hmt.10.27 Libotean, S., Martín, A., Salavera, D., Valles, M., Esteve, X., and Coronas, A. (2008). Densities, viscosities, and heat capacities of ammonia + lithium nitrate and ammonia + lithium nitrate + water solutions between (293.15 and 353.15) K. J. Chem. Eng. Data 53, 2383 –2388. https://doi.org/10.1021/je8003035 Libotean, S., Salavera, D., Valles, M., Esteve, X., and Coronas, A. (2007). Vapor -liquid equilibrium of ammonia + lithium nitrate + water and ammonia + lithium nitrate solutions from (293.15 to 353.15) K. J. Chem. Eng. Data 52, 1050 –1055. https://doi.org/10.1021/je7000045 Lima, A. A. S., Ochoa, A. A. V, Da Costa, J. A. P., and Henríquez, J. R. (2019). CFD simulation of heat and mass transfer in an absorber that uses the pair ammonia/water as a working fluid. Int. J. Refrig. 98, 514 –525. https://doi.org/10.1016/j.ijrefrig.2018.11.010 McNeely, L. A. (1979). Thermodynamic properties of aqueous solutions of lithium bromide. ASHRAE Trans. 85, 413 –434 . Mendoza, J., Rhenals, J., Avila, A., Martinez, A., De la Vega, T., and Durango, E. (2021). Heat absorption cooling with renewable energies: a case study with photovoltaic solar energy and biogas in Cordoba, Colombia. INGE CUC 17, 1 –10. https://doi.org/10.17981/ingecuc.17.2.2021.01 Merrill, T. L., and Perez -Blanco, H. (1997). Combined heat and mass transfer during bubble absorption in binary solutions. Int. J. Heat Mass Transf. 40, 589 –603. https://doi.org/10.1016/0017-9310(96)00118 - 4 Mirzaie, M., Talebizadeh, A. R., and Hashemipour, H. (2020). CFD simulation of benzene adsorption on pistachio activated carbon porous media. Front. Heat Mass Transf. 14, 1 –7. https://doi.org/10.5098/hmt.14.1 9 Oronel, C., Amaris, C., Vallès, M., and Bourouis, M. (2010). Experiments on the characteristics of saturated boiling heat transfer in a plate heat exchanger for ammonia/lithium nitrate and ammonia/(lithium nitratewater). in 2010 3rd International Conference on Thermal Issues in Emerging Technologies, Theory and Applications - Proceedings, ThETA3 2010, 217 –225. https://doi.org/10.1109/THETA.2010.5766401 Panda, S. K., and Mani, A. (2016). CFD heat and mass transfer studies in a R134a -DMF bubble absorber with swirl flow entry of R134a vapour. Int. Compress. Eng. Refrig. Air Cond. High Perform. Build. Conf., 1 –10. Rodríguez -Toscano, A., Amaris, C., Sagastume -Gutiérrez, A., and Bourouis, M. (2022). Technical, environmental, and economic evaluation of a solar/gas driven absorption chiller for shopping malls inthe Caribbean region of Colombia. Case Stud. Therm. Eng. 30, 101743. https://doi.org/10.1016/J.CSITE.2021.101743 Soheel, A. H., Jumaah, O. M., and Saleem, A. M. (2021). Simulation and investigation of nano -refrigerant fluid characteristics with the two -phase flow in microchannel. Front. Heat Mass Transf. 17. https://doi.org/10.5098/hmt.17.21 Suresh, M., and Mani, A. (2010). Heat and mass transfer studies on R134a bubble absorber in R134a/DMF solution based on phenomenological theory. Int. J. Heat Mass Transf. 53, 2813 –2825. https://doi.org/10.1016/j.ijheatmasstransfer.2010.02.016 Triché, D., Bonnot, S., Perier -Muzet, M., Boudéhenn, F., Demasles, H., and Caney, N. (2017). Experimental and numerical study of a falling film absorber in an ammonia -water absorption chiller. Int. J. Heat Mass Transf. 111, 374 –385. https://doi.org/10.1016/j.ijheatmasstransfer.2017.04.008 Turkyilmazoglu, M. (2019). Cooling of Particulate Solids and Fluid in a Moving Bed Heat Exchanger. J. Heat Transfer 141, 114501. https://doi.org/10.1115/1.4044590 Turkyilmazoglu, M. (2021). Heat absorption due to falling film with imposed uniform mass fraction at the wall. Int. J. Heat Mass Transf. 177, 121585. https://doi.org/10.1016/j.ijheatmasstransfer.2021.121585 Ullah, K. R., Saidur, R., Ping, H. W., Akikur, R. K., and Shuvo, N. H. (2013). A review of solar thermal refrigeration and cooling methods. Renew. Sustain. Energy Rev. 24, 499 –513. https://doi.org/10.1016/j.rser.2013.03.024 Versteeg, H. K., and Malalasekera, W. (1995). An introduction to computational fluid dynamics. The finite volume method. 1st ed. , ed. Longman Group Ltd New York. Wu, X., Xu, S., and Jiang, M. (2018). Development of bubble absorption refrigeration technology: A review. Renew. Sustain. Energy Rev. 82, 3468 –3482. https://doi.org/10.1016/J.RSER.2017.10.109 Zapata, A., Amaris, C., Sagastume, A., and Rodríguez, A. (2021). CFD modelling of the ammonia vapour absorption in a tubular bubble absorber with NH3/LiNO3. Case Stud. Therm. Eng. 27, 101311. https://doi.org/10.1016/J.CSITE.2021.101311 Zhou, R., Wang, M., Jin, Z., and Li, S. (2023). Modeling and experimental verification of the enhancement of TiO2 nanofluid on ammonia falling film absorption process. Int. J. Therm. Sci. 184, 107917. https://doi.org/10.1016/j.ijthermalsci.2022.107917 |
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© 1997-2024 TSP (Henderson, USA) unless otherwise stated |
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Atribución 4.0 Internacional (CC BY 4.0) |
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Atribución 4.0 Internacional (CC BY 4.0)© 1997-2024 TSP (Henderson, USA) unless otherwise statedhttps://creativecommons.org/licenses/by/4.0/info:eu-repo/semantics/openAccesshttp://purl.org/coar/access_right/c_abf2Zapata, AndrésAmaris, CarlosSagastume Gutierrez, AlexisRodríguez, Andrés2024-04-29T14:12:51Z2024-04-29T14:12:51Z2022Amaris, C., Zapata, A., Sagastume, A., & Rodríguez, A. (2022). VAPOUR ABSORPTION PROCESS IN AN NH3/LINO3 BUBBLE ABSORBER USING AN OPTIMIZED CFD MODEL. Frontiers in Heat and Mass Transfer (FHMT), 19. https://doi.org/10.5098/hmt.19.332151-8629https://hdl.handle.net/11323/1288910.5098/hmt.19.33Corporación Universidad de la CostaREDICUC – Repositorio CUChttps://repositorio.cuc.edu.co/The present study aims to assess the vapour bubble absorption into the ammonia/lithium nitrate (NH3/LiNO3) solution by using an optimized CFD model. A detailed methodology to build up the CFD model is presented, as well as its validation using experimental data. The operating conditions set corresponds to an absorption chiller driven by low-temperature heat sources such as solar energy in warm environments. Results evidenced that the Volume of Fluid and Mixture models are adequate to be used in the CFD model to predict the absorption process in the bubble absorber assessed depending on the mesh density refinement. Moreover, the heat transfer coefficient from the solution side and the absorption mass flux are the variables needed for reliable validation of the model. Finally, the absorbed flux estimated from the CFD model ranged between 3.2×10−3 kg.m−2 .s−1 and 4.4×10−3 kg.m−2 .s−1 , while the solution side heat transfer coefficient varied between 457 W.m−2 .K−1 and 786 W.m−2 .K−1 , under the conditions considered.9 páginasapplication/pdfengTech Science PressUnited Stateshttps://www.techscience.com/fhmt/v19n1/52424Vapour absorption process in an nh3/lino3 bubble absorber using an optimized CFD modelArtículo de revistahttp://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_970fb48d4fbd8a85Frontiers in Heat and Mass TransferAggarwal, M. K., and Agarwal, R. S. (1986). Thermodynamic properties of lithium nitrate‐ammonia mixtures. Int. J. Energy Res. 10, 59 –68. https://doi.org/10.1002/er.4440100107Amaris, C. (2013). Intensification of NH3 bubble absorption process using advanced surfaces and carbon nanotubes for NH3/LiNO3 absorption chillers. Available at: https://www.tdx.cat/handle/10803/128504Amaris, C., Alvarez, M. E., Vallès, M., and Bourouis, M. (2020a). Performance assessment of an NH3/LiNO3 bubble plate absorber applying a semi -empirical model and artificial neural networks. Energies 13. https://doi.org/10.3390/en13174313Amaris, C., and Bourouis, M. (2021). Boiling process assessment for absorption heat pumps: A review. Int. J. Heat Mass Transf. 179, 121723. https://doi.org/10.1016/j.ijheatmasstransfer.2021.121723Amaris, C., Bourouis, M., Vallès, M., Salavera, D., and Coronas, A. (2015). Thermophysical properties and heat and mass transfer of new working fluids in plate heat exchangers for absorption refrigeration systems. Heat Transf. Eng. 36. https://doi.org/10.1080/01457632.2014.923983Amaris, C., Miranda, B. C., and Balbis -Morejón, M. (2020b). Experimental thermal performance and modelling of a waste heat recovery unit in an energy cogeneration system. Therm. Sci. Eng. Prog. 20. https://doi.org/10.1016/j.tsep.2020.100684Amaris, C., Rodriguez, A., Sagastume, A., and Bourouis, M. (2023). Performance Assessment of a Solar/Gas Driven NH3/LiNO3 Absorption Cooling System for Malls. Lect. Notes Mech. Eng., 311 –328. https://doi.org/10.1007/978-981-19-3467-4_19Amaris, C., Vallès, M., and Bourouis, M. (2018). Vapour absorption enhancement using passive techniques for absorption cooling/heating technologies: A review. Appl. Energy 231, 826–853. https://doi.org/10.1016/j.apenergy.2018.09.071Anand, S., Suresh, S., Dhanuskodi, R., and Santhosh Kumar, D. (2020). Comparison of cfd and empirical models for predicting wall temperature at supercritical conditions of water. Front. Heat Mass Transf. 14. https://doi.org/10.5098/hmt.14.8ANSYS (2013). ANSYS Fluent Theory Guide. , ed. Ansys New York, USA https://doi.org/10.1016/0140-3664(87)90311- 2Asfand, F., Stiriba, Y., and Bourouis, M. (2015). CFD simulation to investigate heat and mass transfer processes in a membrane -based absorber for water -LiBr absorption cooling systems. Energy. https://doi.org/10.1016/j.energy.2015.08.018Asfand, F., Stiriba, Y., and Bourouis, M. (2016). Performance evaluation of membrane -based absorbers employing H2O/(LiBr + LiI+ LiNO3+ LiCl) andH2O/(LiNO3+ KNO3+ NaNO3) as working pairs in absorption coolingsystems. Energy. https://doi.org/10.1016/j.energy.2016.08.103Ayou, D. S., Bruno, J. C., Saravanan, R., and Coronas, A. (2013). An overview of combined absorption power and cooling cycles. Renew. Sustain. Energy Rev. 21, 728 –748. https://doi.org/10.1016/j.rser.2012.12.068Bhagat, R. D., and Deshmukh, S. J. (2022). Numerical analysis to predict the behavior of liquid vapor slug flow in vertically placed u -shaped closed capillary tube. Front. 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ada 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.
 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