Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature

Mireya Ruiz Amelio; Francisco Javier Altamirano García

doi:doi:10.11648/j.ijees.20170204.12

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Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature

Mireya Ruiz Amelio, Francisco Javier Altamirano García

Published in International Journal of Energy and Environmental Science (Volume 2, Issue 4)

Received: 29 June 2017 Accepted: 12 July 2017 Published: 11 August 2017

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Abstract

The objective of this study is to obtain, by means of a new design of the pipe which transports the hot air from the solar collector to the drying chamber, a uniform temperature inside the drying chamber so that the product to be dried deposited in all trays is evenly dehydrated. Outdoor drying experiments of agricultural products were carried out to test the thermal performance of a natural convection solar dyer constructed. Almost all the products were dehydrated in a single day. Since the quality of dried product depends significantly on the temperature of the drying process passive thermography -was used to monitor the product temperature during the drying process. The thermal images reveal that under climatological normal conditions the temperature gradient is 1-3°C among the apple slices placed in trays; the existing moisture in the surface of the specimens is homogeneously released and the maximal temperature attained by the product is less than 40°C when the irradiance is 1000 W/m² and the average temperature of the hot air in the drying cabinet is 55°C.

Published in	International Journal of Energy and Environmental Science (Volume 2, Issue 4)
DOI	10.11648/j.ijees.20170204.12
Page(s)	79-88
Creative Commons	This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.
Copyright	Copyright © The Author(s), 2024. Published by Science Publishing Group

Keywords

Indirect Type Solar Dryer, Solar Energy, Passive Thermography

References

[1]	Krokida, M. K., & Marinos-Kouris, D. “Rehydration kinetics of dehydrated products.” Journal of Food Engineering, Volume 57(1), pp 1–7. March 2003.
[2]	Tripaty, P. P. “Investigation into solar drying of potato: effect of simple geometry on drying kinetics and CO2 emissions mitigation.” J Food Sci Technol. Volume 52(3), pp 1383-1393. March 2015.
[3]	Gulcimen, F., Karakaya, H. and Durmus, A. “Drying of sweet basil with solar air collectors.” Renewable Energy. Volume 93, pp 77-86. August 2016.
[4]	Maskan, M. “Microwave/air and microwave finish drying of banana.” Journal of Food Engineering. Volume 44, issue 2, pp 71–78. May 2000.
[5]	Aguilera. J. M. “Drying and dried products under thE microscope.” Food Sci. Tech. Int. Volume: 9 issue: 3, pp. 137-143, June 2003.
[6]	Lin, T. M., Durance, T. D., & Scaman, C. H. “Characterization of vacuum microwave air and freeze dried carrot slices.” Food Research International. Volume 4, pp 111–117. March 1998.
[7]	Nindo, C., Sun, T., Wang, S. W., Tang, J. and Powers J. R. “Evaluation of drying technologies for retention of physical quality and antioxidants in asparagus. Leben Wissen Technol. Volume 36, pp 507-516. August 2003.
[8]	Beaudry, C., Raghava, G., Ratti, C and Rennie, T. “Effect of four drying methods on the quality of osmotically dehydrated cranberries.” Drying Technol Volume: 22, pp 521-539. February 2007.
[9]	Leon, A., Kumar, M., and Bhattacharya, S. “A comprehensive procedure for performance evaluation of solar food dryers.” Renewable and Sustainable Energy Reviews, Volume 6, issue 4, pp 367-393. August 2002.
[10]	Bezyma LA, Kutovoy V. A. “Vacuum drying and hybrid technologies” Stewart Post- harvest Review. Volume 4, pp 6-13, December 2005.
[11]	Kant, K., Shukla, A., Sharma, A., Kumar, A and Jain A. “Thermal energy storage based solar drying systems: A review.” Innovative Food Science and Emerging Technologies. Volume 34, pp 86-99. April 2016.
[12]	Gowen, A., Tiwari, B., Cullen, P., McDonnell, K. and O’Donnell, C. “Applications of thermal imaging in food quality and safety assessment.” Trends in Food Science & Technology. Volume 21, pp 190-200. April 2010.
[13]	Amon, F., Hamins, A., Bryner, N and Rowe, J. “Meaningful performance evaluation conditions for fire service thermal imaging cameras.” Fire Safety Journal. Volume 43. Issue: 8, pp. 541-550, November 2008.
[14]	Bagavathiappan, S., Lahiri B. B., Saravanan, T., Philip, J and Jayakumar, T. “Infrared thermography for condition monitoring. A review.” Infrared Physics & Technology. Volume 60, pp 35-55. September 2013.
[15]	Ridley, I. “Practical aspects of infrared remote thermometry. In Instrumentation and Sensors for the Food Industry” (E. Kress-Rogers and C. J. B. Brimelow, eds.) 187-212, CRC Press, Boca Raton, FL.
[16]	Lidhoo C. K. and Agrawal Y. C. “Hot-air oven drying characteristics of button mushroom-safe drying temperature.” Mush Res Vol. 15, pp 59-62. 2006.
[17]	Mayor, L., Sereno, A. M. “Modelling shrinkage during convective drying of food materials.” J Food Eng. Volume 61, pp 373-386. February 2004.
[18]	Sagar, V. R. “Recent advances in drying and dehydration of fruits and vegetables: a review.” J Food Sci Technol. Volume 47(1), pp 15-26. January 2010.

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APA Style

Mireya Ruiz Amelio, Francisco Javier Altamirano García. (2017). Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature. International Journal of Energy and Environmental Science, 2(4), 79-88. https://doi.org/10.11648/j.ijees.20170204.12

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ACS Style

Mireya Ruiz Amelio; Francisco Javier Altamirano García. Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature. Int. J. Energy Environ. Sci. 2017, 2(4), 79-88. doi: 10.11648/j.ijees.20170204.12

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AMA Style

Mireya Ruiz Amelio, Francisco Javier Altamirano García. Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature. Int J Energy Environ Sci. 2017;2(4):79-88. doi: 10.11648/j.ijees.20170204.12

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@article{10.11648/j.ijees.20170204.12,
  author = {Mireya Ruiz Amelio and Francisco Javier Altamirano García},
  title = {Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature},
  journal = {International Journal of Energy and Environmental Science},
  volume = {2},
  number = {4},
  pages = {79-88},
  doi = {10.11648/j.ijees.20170204.12},
  url = {https://doi.org/10.11648/j.ijees.20170204.12},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ijees.20170204.12},
  abstract = {The objective of this study is to obtain, by means of a new design of the pipe which transports the hot air from the solar collector to the drying chamber, a uniform temperature inside the drying chamber so that the product to be dried deposited in all trays is evenly dehydrated. Outdoor drying experiments of agricultural products were carried out to test the thermal performance of a natural convection solar dyer constructed. Almost all the products were dehydrated in a single day. Since the quality of dried product depends significantly on the temperature of the drying process passive thermography -was used to monitor the product temperature during the drying process. The thermal images reveal that under climatological normal conditions the temperature gradient is 1-3°C among the apple slices placed in trays; the existing moisture in the surface of the specimens is homogeneously released and the maximal temperature attained by the product is less than 40°C when the irradiance is 1000 W/m2 and the average temperature of the hot air in the drying cabinet is 55°C.},
 year = {2017}
}

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TY  - JOUR
T1  - Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature
AU  - Mireya Ruiz Amelio
AU  - Francisco Javier Altamirano García
Y1  - 2017/08/11
PY  - 2017
N1  - https://doi.org/10.11648/j.ijees.20170204.12
DO  - 10.11648/j.ijees.20170204.12
T2  - International Journal of Energy and Environmental Science
JF  - International Journal of Energy and Environmental Science
JO  - International Journal of Energy and Environmental Science
SP  - 79
EP  - 88
PB  - Science Publishing Group
SN  - 2578-9546
UR  - https://doi.org/10.11648/j.ijees.20170204.12
AB  - The objective of this study is to obtain, by means of a new design of the pipe which transports the hot air from the solar collector to the drying chamber, a uniform temperature inside the drying chamber so that the product to be dried deposited in all trays is evenly dehydrated. Outdoor drying experiments of agricultural products were carried out to test the thermal performance of a natural convection solar dyer constructed. Almost all the products were dehydrated in a single day. Since the quality of dried product depends significantly on the temperature of the drying process passive thermography -was used to monitor the product temperature during the drying process. The thermal images reveal that under climatological normal conditions the temperature gradient is 1-3°C among the apple slices placed in trays; the existing moisture in the surface of the specimens is homogeneously released and the maximal temperature attained by the product is less than 40°C when the irradiance is 1000 W/m2 and the average temperature of the hot air in the drying cabinet is 55°C.
VL  - 2
IS  - 4
ER  -

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Author Information

Mireya Ruiz Amelio

Department of Engineering of Process and Hydraulics, Universidad Autónoma Metropolitana, Mexico City, Mexico
Francisco Javier Altamirano García

Department of Engineering of Process and Hydraulics, Universidad Autónoma Metropolitana, Mexico City, Mexico

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APA Style

Mireya Ruiz Amelio, Francisco Javier Altamirano García. (2017). Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature. International Journal of Energy and Environmental Science, 2(4), 79-88. https://doi.org/10.11648/j.ijees.20170204.12

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ACS Style

Mireya Ruiz Amelio; Francisco Javier Altamirano García. Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature. Int. J. Energy Environ. Sci. 2017, 2(4), 79-88. doi: 10.11648/j.ijees.20170204.12

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AMA Style

Mireya Ruiz Amelio, Francisco Javier Altamirano García. Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature. Int J Energy Environ Sci. 2017;2(4):79-88. doi: 10.11648/j.ijees.20170204.12

Copy | Download

@article{10.11648/j.ijees.20170204.12,
  author = {Mireya Ruiz Amelio and Francisco Javier Altamirano García},
  title = {Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature},
  journal = {International Journal of Energy and Environmental Science},
  volume = {2},
  number = {4},
  pages = {79-88},
  doi = {10.11648/j.ijees.20170204.12},
  url = {https://doi.org/10.11648/j.ijees.20170204.12},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ijees.20170204.12},
  abstract = {The objective of this study is to obtain, by means of a new design of the pipe which transports the hot air from the solar collector to the drying chamber, a uniform temperature inside the drying chamber so that the product to be dried deposited in all trays is evenly dehydrated. Outdoor drying experiments of agricultural products were carried out to test the thermal performance of a natural convection solar dyer constructed. Almost all the products were dehydrated in a single day. Since the quality of dried product depends significantly on the temperature of the drying process passive thermography -was used to monitor the product temperature during the drying process. The thermal images reveal that under climatological normal conditions the temperature gradient is 1-3°C among the apple slices placed in trays; the existing moisture in the surface of the specimens is homogeneously released and the maximal temperature attained by the product is less than 40°C when the irradiance is 1000 W/m2 and the average temperature of the hot air in the drying cabinet is 55°C.},
 year = {2017}
}

Copy | Download

TY  - JOUR
T1  - Multiple Inlets of Hot Air to Drying Chamber of an Indirect Solar Dryer to Achieve Uniform Chamber Temperature
AU  - Mireya Ruiz Amelio
AU  - Francisco Javier Altamirano García
Y1  - 2017/08/11
PY  - 2017
N1  - https://doi.org/10.11648/j.ijees.20170204.12
DO  - 10.11648/j.ijees.20170204.12
T2  - International Journal of Energy and Environmental Science
JF  - International Journal of Energy and Environmental Science
JO  - International Journal of Energy and Environmental Science
SP  - 79
EP  - 88
PB  - Science Publishing Group
SN  - 2578-9546
UR  - https://doi.org/10.11648/j.ijees.20170204.12
AB  - The objective of this study is to obtain, by means of a new design of the pipe which transports the hot air from the solar collector to the drying chamber, a uniform temperature inside the drying chamber so that the product to be dried deposited in all trays is evenly dehydrated. Outdoor drying experiments of agricultural products were carried out to test the thermal performance of a natural convection solar dyer constructed. Almost all the products were dehydrated in a single day. Since the quality of dried product depends significantly on the temperature of the drying process passive thermography -was used to monitor the product temperature during the drying process. The thermal images reveal that under climatological normal conditions the temperature gradient is 1-3°C among the apple slices placed in trays; the existing moisture in the surface of the specimens is homogeneously released and the maximal temperature attained by the product is less than 40°C when the irradiance is 1000 W/m2 and the average temperature of the hot air in the drying cabinet is 55°C.
VL  - 2
IS  - 4
ER  -

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