Effect of Some Operating Parameters on the Reversing Continuous Countercurrent Extraction Process

Authors

  • Waigoon RITTIRUT School of Agricultural Technology, Walailak University, Nakhon Si Thammarat 80161
  • Chairat SIRIPATANA School of Engineering and Resources Management, Walailak University, Nakhon Si Thammarat, 80161

Keywords:

Garcinia fruit, Garcinia atroviridis, degree of inclination, yield, slope of extractor, percent forward progression, evaporation, concentration profile

Abstract

The effect of some operating parameters on the reversing continuous countercurrent extraction process including the degree of inclination of the extractor and the percent forward progression by a screw conveyor was reported. Garcinia fruit was selected as model solid while sucrose was used as soluble solid for the diffusion system. The results showed that the degree of inclination provided certain effect on concentration profile, however was still ambiguous. For experimental purpose, 5, 7 or 10° can be used. Nevertheless, the solid and liquid phase were not in contact at the end point of the extraction unit in the case of 7° and 10° where the specified draft was 1.6. Based on the highest yield, a slope of 10° should be chosen. For a percent forward progression range of 10 - 20 %, the concentration profiles for both liquid and solid phase were almost identical. However, the lowest 5 % percent forward progression led to highest concentration profile for the liquid phase.

Keywords:

Downloads

Download data is not yet available.

Metrics

Metrics Loading ...

References

HG Schwartzberg. Continuous counter current extraction in the food industry. Chem. Eng. Progress 1980; 76, 67-85.

C Iversion and HG Schwartzberg. Development in beet and sugar cane extraction. Food Technol. 1984; 38, 40-4.

DJ Casimir. Counter current extraction of soluble solids from foods. CSIRO. Food Res. Quar. 1983; 53, 38-43.

AJ Jones. A chronology of Australian bioscience, chemical and chemical engineering achievements: part I (1976-2006). Chem. Aust. 2007; 2, 7-17.

UPASI Tea Research Foundation. UPASI Annual report. Nirar Dam BPO, Valparai-642-127, Coimbatore Dist, INDEA, 2006, p. 16.

W Rittirut and C Siripatana. Drying characteristics of Garcinia atroviridis. Walailak J. Sci. & Tech. 2006; 3, 13-32.

W Rittirut and C Siripatana. Diffusion properties of garcinia fruit acids (Garcinia atrovirridis). Walailak J. Sci. & Tech. 2007; 4, 187-202.

W Rittirut. 2009, Modeling simulation of solid-liquid diffusion in continuous countercurrent extraction process, Ph.D. Thesis. Walailak University, Thailand.

YC Lee and HG Schwartzberg. Effect of Axial Dispersion During Solid-Liquid Extraction. In: WEL Spiess and H Schubert. (eds.). Engineering and Food volume III. Elsevier Science Publishers, London, 1990, p. 1-10.

C Siripatana. 1986. Mass transfer in a reversing countercurrent extractor. Master of Applied Science Thesis. The University of New South Wales, Australia.

FP Placho and JH Krasuk. Solid-liquid countercurrent extractors. Ind. & Eng. Chem. Proc. Des. Dev. 1970; 9, 419-33.

T Thummadetsak. 1996. Mass transfer in pineapple juice extractor. Master of Engineering Thesis (in Thai). Prince of Songkla University, Songkhla, Thailand.

HG Schwartzberg. Leaching organic materials, chapter 10. In: RW Rousseau (ed.). Handbook of Separation Process Technology. New York, John Wileys & Sons, Inc. 1987, p. 540-77.

Downloads

Published

2011-11-08

How to Cite

RITTIRUT, W., & SIRIPATANA, C. (2011). Effect of Some Operating Parameters on the Reversing Continuous Countercurrent Extraction Process. Walailak Journal of Science and Technology (WJST), 6(2), 203–215. Retrieved from https://wjst.wu.ac.th/index.php/wjst/article/view/60

Issue

Section

Research Article

Most read articles by the same author(s)