Chung Lim Law

Prof. Dr. Chung Lim Law

orcid

Research Focus & Metrics

Academic Career Length

24Years (2003-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 December 2009 in Chemical Engineering Journal
Verified
Journal Article
Closed access
Yi Jing ChanYi Jing Chan
Yi Jing Chan
MCMei Fong Chong
Mei Fong Chong
CLChung Lim Law
Chung Lim Law
DHD.G. Hassell
D.G. Hassell

23 April 2010 in Food and Bioprocess Technology
Verified
Journal Article
Closed access
PDF file
AMArun S. Mujumdar
Arun S. Mujumdar
CLChung Lim Law
Chung Lim Law

1 May 2018 in Journal of Food Engineering
Verified
Journal Article
Closed access
JWJun Wang
Jun Wang
CLChung Lim Law
Chung Lim Law
PNPrabhat K. Nema
Prabhat K. Nema
JZJin-Hong Zhao
Jin-Hong Zhao
ZLZi-Liang Liu
Zi-Liang Liu
Hong-Wei XiaoHong-Wei Xiao
Hong-Wei Xiao

1 January 2009 in Journal of Food Engineering
Verified
Journal Article
Closed access
Ching Lik HiiChing Lik Hii
Ching Lik Hii
CLChung Lim Law
Chung Lim Law
MCM. Cloke
M. Cloke

12 February 2014 in Drying Technology
Verified
Journal Article
Closed access
Hong-Wei XiaoHong-Wei Xiao
Hong-Wei Xiao
CLChung Lim Law
Chung Lim Law
DSDa-Wen Sun
Da-Wen Sun
ZGZhen-Jiang Gao
Zhen-Jiang Gao
The color change kinetics of American ginseng (Panax quinquefolium) slices were investigated in an air impingement dryer under different drying temperatures (35, 45, 55, and 65°C) using the CIE Lab color parameters (L*, a*, b*) as the assessment indicators. Results illustrated that all three color parameters (L*, a*, b*) increased with drying time. The L* value decreased with increasing drying temperature. However, a* and b* values increased with the increase in drying temperature. Furthermore, at the initial drying stage the change rate of L* increased significantly, while towards the end of drying it reduced significantly. As regards a*, it slowly changed at the initial and final drying stages rather than in the intermediate drying stage. In the case of b*, it increased with increasing drying time and drying temperature during the whole process. The zero-order, first-order, and fractional conversion models were fitted to the experimental data, and the model's parameters were determined using linear regression analysis. By comparing the fitting of kinetic models to the experimental data, the most suitable model was selected to describe the color change kinetics. An Arrhenius equation was used to calculate the activation energy for color change kinetics and it was found that the values were 33.87–38.55, 56.48, and 74.03 kJ/mol for L*, a*, and b*, respectively. The findings of this work contribute to a better understanding of ginseng color changes kinetics during drying, and the established change kinetics models are a good tool for predicting, evaluating, and controlling of color change of American ginseng during its drying process.

24 February 2010 in Food and Bioprocess Technology
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Journal Article
Closed access
PDF file
Fabiano André Narciso FernandesFabiano André Narciso Fernandes
Fabiano André Narciso Fernandes
Sueli RodriguesSueli Rodrigues
Sueli Rodrigues
CLChung Lim Law
Chung Lim Law
AMArun S. Mujumdar
Arun S. Mujumdar