1962: 1, kg/person 19 83: 1, kg/person Slide
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1 URL: : Slide 1
2 1962: 1, kg/person 19 83: 1, kg/person Slide
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5 : 11 : Food-Consumer Interaction Department 20 Slide 5 ( )
6 Slide 6 ( ) R&D
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9 A-K( K( ) A-K FD FD FD FD FD FD ( Slide 8 A-K
10 Refrigerator Thermocouple Internal condenser Slide 9 Heater Electric balance External condenser Pressure sensor Vacuum pump Indicator Data logger Indicator A/D converter C ontroller Chamber Press : Pa Condenser Temp : Slide 10 PC
11 Slide 12 (a) Slide 13 Surface Temperature Slide 11 Surface Temperature Contro l Quality Design: Scorch-Flavor Flavor-TasteT aste Difference in Drying Time Constan t Platen Temperature (Traditional metho d) Drying Time (b)
12 Slide 14 Slide 15 ( )
13 p p p ((Meth M ethodolo ogy f or con nsumer-oriented ed food d design n and produ uctio ction n) Slide 16 Total Engineering g for Consumer- oriented Technologies + + Slide 17
14 NaCl NaCl( ) NaCl NaCl NaCl NaCl NaCl( ) Slide 18
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15 Slide 20 [, ]] ( ) [ ] Slide 19 [ ]] [ ] [[ ] PC #4 (sweetness) Slide PC #1 (smoothness) PC #3 (fragrance) PC #2 (thickness) female students female office workers male office workers
16 To tal am ino acids To tal catechins Slide 24 Slide 22 Flowery flavor S weet flavor Roast f lavor Gre en flavor fe male stud ents Slide 23 fe male office w orker s m ale offi ce w orker s
17 TV TV Slide 25 TV Slide 26 ( CO CO (
18 Corporative Relationship among the Biodiesel Teams in the Biomass Energy Project Conducted by MAFF Microemulsification Methods Elucidation of Non -catalytic A lcoholysis R e ac tion M echanism Prof. Sagara s Lab, Un iv. of Tokyo D e ve lopm en t of E fficient Techn ologie s for R edu ction in V isc osity of O ils and Fats (N ational Food Re se ar ch Institut e) Non-catalytic Alcoholysis Method D evelopment of Pilot Plants for Production of BD F b y U se of N on-catalytic A lc oh olysis R eaction (Kajima Corp. L TD + A -IC S C orp.) Evalu at ion of Biodiese l Fuel Propert y Based on C ombustion Te st (Prof. Y amane s L ab., U niv. of Shiga P refec ture) Slide 27 Reactor for Non-cata lytic Alcoholysis Reac tion V egetable Oil M ethan ol Slide 28 Pump Heater Pump dehydration Column C ondenser Gas Phase Sample Reactor ( C) Liquid Phase Sample
19 ( : 40 L/d ) Slide 29 Demonstrational Plant Productivity 400L/day Slide 30 ( 400L/day) Estimation of Cost for BDF Production Yen/L Raw M aterial Waste Tr eatment Transportation P roduction C ost Labor Cost Equipme nt Yen/L Slide 31 BDF 0 Alkaline Catalyst Non-c atalytic Method Method Yen
20 BDF R&D Project Teams In Indonesia Indonesian Oil Palm Board (in process) (IPB) Prof. Armansyah H. Tambunan UNIVERSITIES North Sumatera University Soedirman University Indonesian Oil Palm Research Institute (IOPRI) GAPKI; Gabungan Pengusaha Kelapa Sawit BPPT; Badan Pengkajian dan Penerapan Teknologi Udayana University Institute of Technology in Bandung (ITB) Indonesian Oil Palm Society (IOPS/MAKSI) Ministry of Agriculture Ministry of Industry ( Ministry of Research and Technology ( Ministry of Energy ( Slide 32 BDF
21 Slide 33 Front view of 1500 L/day EC BPPT prototype biodiesel plant Front view of an 8 tones/day biodiesel pilot plant in Pekanbaru Riau Armansyah H. Tambunan Slide 34
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8 ( ) 8. 1 ( ) F F = F I (N I, T, V I ) + F II (N II, T, V II ) (8.1) F δf = δn I [ ( FI (N I ) N I 8. 1 111 ) T,V δn I [ ( FI N I ( ) F N T,V ( ) FII (N N I ) + N I ) ( ) FII T,V N II T,V T,V ] ] = 0
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