Please use this identifier to cite or link to this item: http://cmuir.cmu.ac.th/jspui/handle/6653943832/70497
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dc.contributor.authorPiyathida Panyoyaien_US
dc.contributor.authorSamerkhwan Tantikulen_US
dc.contributor.authorThanasit Wongsiriamnuayen_US
dc.contributor.authorTipapon Khamdaengen_US
dc.contributor.authorNakorn Tippayawongen_US
dc.contributor.authorNumpon Panyoyaien_US
dc.date.accessioned2020-10-14T08:31:55Z-
dc.date.available2020-10-14T08:31:55Z-
dc.date.issued2020-04-06en_US
dc.identifier.issn17551315en_US
dc.identifier.issn17551307en_US
dc.identifier.other2-s2.0-85083461097en_US
dc.identifier.other10.1088/1755-1315/463/1/012136en_US
dc.identifier.urihttps://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=85083461097&origin=inwarden_US
dc.identifier.urihttp://cmuir.cmu.ac.th/jspui/handle/6653943832/70497-
dc.description.abstract© 2020 Institute of Physics Publishing. All rights reserved. Waste heat from the combustion process that is left unused may cause pollution problems and adversely affect health. This waste heat should be recovered. In this research, the simulation and experimental data on heat transfer characteristics of the pipe coiled inside the re-burning kiln heat exchanger were studied. The main objective of this study was to compare heat transfer coefficients obtained from the simulation using water as the working fluid with those obtained experimentally from the re-burning kiln heat exchanger for the drying system. The re-burning kiln heat exchanger was of coil-pipe-type with an outside diameter of 38 mm. The coiled pipe set up on the re-burning kiln heat exchanger was 80 cm in width and 173 cm in height. The flow rate of the cold water used as a working fluid was varied from 10 to 20 LPM, while the surface temperature of the coil pipe was varied from 200±20°C to 400±20°C, respectively. Thermal conductivity and outlet temperature of the water were also measured as a function of the internal temperature and water flow rate. The experimental results were validated against the simulation. The results showed that when the flow rate of water inlet decreased from 20 LPM to 10 LPM, the temperature of the water outlet was increased from 52.4 °C to 76.3 °C respectively. An increase in the temperature of the water outlet because of increased the re-burning kiln heat exchanger temperature and reduced the mass flow rate of supply water. The obtained simulated heat transfer coefficient in the re-burning kiln heat exchanger was in agreement with the experimental results.en_US
dc.subjectEarth and Planetary Sciencesen_US
dc.subjectEnvironmental Scienceen_US
dc.titleComparison between simulations and experiment for heat transfer characteristics in the re-burning kiln heat exchangeren_US
dc.typeConference Proceedingen_US
article.title.sourcetitleIOP Conference Series: Earth and Environmental Scienceen_US
article.volume463en_US
article.stream.affiliationsMaejo Universityen_US
article.stream.affiliationsChiang Mai Universityen_US
Appears in Collections:CMUL: Journal Articles

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