Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source

This article presents experimental performance of a batch-type longan dryer using a biomass burner with air flow reversal and also presents modeling of the longan dryer for drying of whole longan. The dryer essentially consists of a biomass burner and a drying bin with an arrangement for periodic ai...

Full description

Saved in:
Bibliographic Details
Main Authors: S. Janjai, N. Lamlert, B. Mahayothee, P. Sruamsiri, M. Precoppe, B. K. Bala, J. Muller
Format: Journal
Published: 2018
Subjects:
Online Access:https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=83155193378&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/49800
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Chiang Mai University
id th-cmuir.6653943832-49800
record_format dspace
spelling th-cmuir.6653943832-498002018-09-04T04:19:16Z Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source S. Janjai N. Lamlert B. Mahayothee P. Sruamsiri M. Precoppe B. K. Bala J. Muller Chemical Engineering Chemistry This article presents experimental performance of a batch-type longan dryer using a biomass burner with air flow reversal and also presents modeling of the longan dryer for drying of whole longan. The dryer essentially consists of a biomass burner and a drying bin with an arrangement for periodic air flow reversal. Three drying runs with loading capacity of 2,000, 1,500, and 1,000 kg of whole longan were carried out. There was no significant difference in temperatures in different positions (except inlet and outlet) inside the dryer (p<0.05) or moisture content inside the dryer (p<0.05). Whole longan was dried from an initial moisture content of 74% (wb) to a final moisture content of 14% (wb). The drying time of whole longan in the longan dryer was 60, 54, and 48 h for 2,000, 1,500, and 1,000 kg loading, respectively. The quality of dried product was also good in comparison to the high-quality product in markets. To simulate the performance of the longan dryer for drying of whole longan, a set of partial differential equations was developed and the equations were solved using the finite difference technique. The numerical solution was programmed in Compaq Visual FORTRAN version 6.5 (Compaq Computer Corp., TX). The simulated moisture contents agreed well with the experimental data. This model can be used to provide the design data and it is also essential for optimal dryer design. © 2011 Taylor & Francis Group, LLC. 2018-09-04T04:18:14Z 2018-09-04T04:18:14Z 2011-01-01 Journal 15322300 07373937 2-s2.0-83155193378 10.1080/07373937.2011.587925 https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=83155193378&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/49800
institution Chiang Mai University
building Chiang Mai University Library
country Thailand
collection CMU Intellectual Repository
topic Chemical Engineering
Chemistry
spellingShingle Chemical Engineering
Chemistry
S. Janjai
N. Lamlert
B. Mahayothee
P. Sruamsiri
M. Precoppe
B. K. Bala
J. Muller
Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
description This article presents experimental performance of a batch-type longan dryer using a biomass burner with air flow reversal and also presents modeling of the longan dryer for drying of whole longan. The dryer essentially consists of a biomass burner and a drying bin with an arrangement for periodic air flow reversal. Three drying runs with loading capacity of 2,000, 1,500, and 1,000 kg of whole longan were carried out. There was no significant difference in temperatures in different positions (except inlet and outlet) inside the dryer (p<0.05) or moisture content inside the dryer (p<0.05). Whole longan was dried from an initial moisture content of 74% (wb) to a final moisture content of 14% (wb). The drying time of whole longan in the longan dryer was 60, 54, and 48 h for 2,000, 1,500, and 1,000 kg loading, respectively. The quality of dried product was also good in comparison to the high-quality product in markets. To simulate the performance of the longan dryer for drying of whole longan, a set of partial differential equations was developed and the equations were solved using the finite difference technique. The numerical solution was programmed in Compaq Visual FORTRAN version 6.5 (Compaq Computer Corp., TX). The simulated moisture contents agreed well with the experimental data. This model can be used to provide the design data and it is also essential for optimal dryer design. © 2011 Taylor & Francis Group, LLC.
format Journal
author S. Janjai
N. Lamlert
B. Mahayothee
P. Sruamsiri
M. Precoppe
B. K. Bala
J. Muller
author_facet S. Janjai
N. Lamlert
B. Mahayothee
P. Sruamsiri
M. Precoppe
B. K. Bala
J. Muller
author_sort S. Janjai
title Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
title_short Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
title_full Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
title_fullStr Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
title_full_unstemmed Experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
title_sort experimental and simulated performances of a batch-type longan dryer with air flow reversal using biomass burner as a heat source
publishDate 2018
url https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=83155193378&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/49800
_version_ 1681423475250561024