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dc.contributor.authorBudiyati, Eni
dc.contributor.authorMulyono, Panut
dc.contributor.authorPurwono, Suryo
dc.date.accessioned2015-05-18T03:57:08Z
dc.date.available2015-05-18T03:57:08Z
dc.date.issued2013-05-23
dc.identifier.citation[1] Eilittä, M., Bressani, R., Carew, L. B., Carsky, R. J., Flores, M., Gilbert, R., Huyck, L., St- Laurent, L., dan Szabo, N. J., 2000, “Mucuna pruriens asa a Food and Feed Crop: An Overview”, International Cover Crops Clearinghouse, 1, 18-45. [2] Brown, G. G., Foust, A. S., Katz, D. L., Schneidewind, R., White, R. R., dan Wood, W. P., 1950, “Unit Operations”, John Wiley and Sons, Inc., Tokyo. [3] Sediawan, W.B., Prasetya, A., 1997, “Pemodelan Matematis dan Penyelesaian Numeris dalam Teknik Kimia”, Penerbit Andi, Yogyakarta. [4] Smith, J.M., Van Ness, H.C., Abbott, M.M.,2001 “Introduction to Chemical Engineering Thermodynamics”, Sixth Ed., Mc. Graw Hill International Edition. [5] Tyoso, B.W., 1992, “Satuan Operasi pada Proses Pangan II”, Pusat Antar Universitas – Pangan dan Gizi UGM, Yogyakarta. [6] Landbo, A. K., dan Meyer, A. S., 2001, “Enzyme- Assisted Extraction of Antioxidative Phenols from Black Currant Juice Press Residues (Ribes ningrum)”, Journal of Agricultural and Food Chemistry, 49, 3169-3177. [7] Pinelo, M., Del Fabbro, P., Manzocco, L., Núñez, M. J., dan Nicoli, M. C., 2005, “Optimization of Continuous Phenol Extraction from Vitis Vinivera Byproducts”, Food Chemistry, 92, 109-117. [8] Treybal, R. E., 1981, “Mass Transfer Operation”, 3rd ed., McGraw_Hill Book Company, Ltd., Tokyo. [9] Mazza, G., dan Miniati, E., 1993, “Anthocyanins in Fruits, Vegetables, and Grains”, CRC Press Inc., Boca Raton, FL. [10] Fogler, H. S., 1999, “Element of Chemical Reaction Engineering”, 3rd ed., Prentice-Hall, Inc., New Jersey. [11] Owen, Sonia, 2006, “Material Safety Data Sheet”, Spectrum Chemical, New Jersey.in_ID
dc.identifier.issn2088-9828
dc.identifier.urihttp://hdl.handle.net/11617/5975
dc.description.abstractThe objective of this research was to extract L-Dopa from Mucuna pruriens’s seed in a batch stirred tank by use water as solvent. Beside it, this research also evaluates the impact of temperature and stirring speed to concentration of extracted L-Dopa. Three stages have been carried out, namely preparation of raw material, extraction experiment, and L-Dopa analysis. In the preparation of material, the particles were cleaned, size reducted, screen, and dried until the water content is 8.8%. The extraction process takes place in a batch stirred tank, which placed inside a waterbath. In the extraction experiment, variation of temperature (32, 37, 42, and 47oC) and stirring speed (250, 350, 470, dan 750 rpm). The L-Dopa concentration measured using HPLC at certain time (5, 10, 20, 30, 40, 50, and 50 minutes). The results showed that the L-Dopa can be extracted use water from Mucuna pruriens’s seed well. The L-Dopa concentration increased by increasing temperature at the constants diameter particles (d), stirring speed (N) and ratio of Solid-Liquid (S/L). The highest concentration 1659.12 ppm at 47oC. Increasing N at the constants values of d, T, and S/L, also increased the concentration of L-Dopa.in_ID
dc.language.isoidin_ID
dc.publisherUniversitas Muhammadiyah Surakartain_ID
dc.subjectbatch stirred tankin_ID
dc.subjectextractionin_ID
dc.subjectL-Dopain_ID
dc.subjectMucuna pruriens’s seedin_ID
dc.titlePengaruh Suhu dan Kecepatan Putaran Pengaduk pada Ekstraksi L-Dopa dari Biji Kara Benguk pada Tangki Berpengadukin_ID
dc.typeArticlein_ID


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