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FPR-O1.2 D RYING P ROCESS OF M ICROENCAPSULATED R ED P ALM O IL Nur Wulandari Dede R. Adawiyah FPR-01.2 Gatot Pramuhadi Department of Food Science & Technology - Faculty of Agricultural Enginering & Technology SEAFAST Center


  1. FPR-O1.2 D RYING P ROCESS OF M ICROENCAPSULATED R ED P ALM O IL Nur Wulandari Dede R. Adawiyah FPR-01.2 Gatot Pramuhadi • Department of Food Science & Technology - Faculty of Agricultural Enginering & Technology • SEAFAST Center BOGOR AGRICULTURAL UNIVERSITY INDONESIA

  2. I NTRODUCTION Palm oil: potencial Utilization of palm oil source of carotene as food carotenes ingredient and food (mainly b - supplement carotene) 500 ppm Crude palm oil (CPO) Red palm oil (RPO)

  3. High carotene content of Sensitivity of Protection RPO: +250 carotene to O2, by microen- ppm light, heat capsulation process Microen- capsulated RPO

  4. I NTRODUCTION • RPO RPO • Microen- emulsion capsulation • Drying • Homo- materials genization MRPO Materials Suitable Boundary conditions: • High viscosity of RPO dryer • Suceptibility of b -caroten to high T

  5. O BJECTIVES • to determine the most suitable drying equipment for producing 1 MRPO • to study the drying parameters of the chosen drying equipment 2

  6. M ETHODS  RPO was produced in pilot plant scale of oil line production at SEAFAST Center.

  7. M ETHODS Material formulation Emulsification Drying of the emulsion Mikroencapsulated RPO

  8. M ETHODS  The drying experiments were conducted by using tray dryer, drum dryer, and spray dryer  The drying time and drying process performance were evaluated, and quality attributes of MRPO were measured.

  9. RESULTS: D RYING PERFORMANCE Parameter Spray Dryer Drum Dryer Tray Dryer T in 150 o C, T out 70 o C 3 rpm, T 95,5 o C T 50 o C M.C. (% d.b.) 3,94 4,85 6,01 Carotene 160 78 230 content (ppm) Carotene 55,70 31,52 74.76% Retention (%) Pengujian dilakukan dengan menggunakan jumlah Solubility (%) 88,6 86,64 90.71 sampel yang sama, sebanyak 112,5 g emulsi Colour (+b) 25,07 23,63 27,98 Batch Drying system Kontinyu Kontinyu (8 h/batch) Drying rate (g 0,5 kg/h 0,6 kg/h 0,24 kg/h emulsion/hour)

  10. M ICROENCAPSULATED RED PALM OIL  Spray dryer Drum dryer Tray dryer

  11. R ESULTS  The position of the tray and the thickness of the RPO emulsion layer affected the drying time, moisture content, and drying rate  The thickness of emulsion layer will determined drying time and drying rate to achieve the same moisture content  The recomended emulsion layer thickness with good drying process parameters for tray dryer was 1.5 mm

  12. C ONCLUSIONS  Tray dryer can be used for producing high quality of MRPO, regarding of b -carotene contents and recovery during drying process.  The process efficiency of tray dryer must be improved by using continuous drying system

  13. ACKNOWLEDGEMENT  RUSNAS Project from Ministry of Research and Technology, Republic of Indonesia  Southeast Asian Food and Agricultural Science and Technology Center – Bogor Agricultural University

  14. T HAN ANK Y OU OU wulandari_n@ipb.ac.id

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