Lampiran 1. Hasil analisis data pengaruh pencucian dan waktu modifikasi HMT terhadap profil gelatinisasi pati sagu dengan metode
GLM pada program SAS
a. Suhu awal gelatinisasi SAG
Source DF Type I SS Mean Square F Value Pr F pencucian 2 30.78857143 15.39428571 31.88 0.0003
waktu 2 8.72000000 4.36000000 9.03 0.0115 pencucianwaktu 2 25.22000000 12.61000000 26.12 0.0006
Source DF Type III SS Mean Square F Value Pr F pencucian 1 0.18750000 0.18750000 0.39 0.5529
waktu 2 8.72000000 4.36000000 9.03 0.0115 pencucianwaktu 2 25.22000000 12.61000000 26.12 0.0006
Duncan Grouping Mean N pencucian A 77.9000 6 DC
A A 77.6500 6 TD
B 73.5500 2 Kontrol Duncan Grouping Mean N waktu
A 78.9750 4 4 B 77.2750 4 8
B B 77.0750 4 16
C 73.5500 2 0 Duncan Grouping Mean N inter
A 79.1500 2 DC_8 A
A 79.1500 2 DC_4 A
A 78.8000 2 TD_4 A
A 78.7500 2 TD_16 B 75.4000 2 DC_16
B B 75.4000 2 TD_8
C 73.5500 2 Kontrol_
b. Viskositas puncak VP
Source DF Type I SS Mean Square F Value Pr F pencucian 2 54021.42857 27010.71429 657.65 .0001
waktu 2 9150.00000 4575.00000 111.39 .0001 pencucianwaktu 2 2450.00000 1225.00000 29.83 0.0004
Source DF Type III SS Mean Square F Value Pr F
93
pencucian 1 2268.750000 2268.750000 55.24 0.0001 waktu 2 9150.000000 4575.000000 111.39 .0001
pencucianwaktu 2 2450.000000 1225.000000 29.83 0.0004 Duncan Grouping Mean N pencucian
A 590.000 2 Kontrol B 430.000 6 DC
C 402.500 6 TD Duncan Grouping Mean N waktu
A 590.000 2 0 B 451.250 4 4
C 413.750 4 8 D 383.750 4 16
Duncan Grouping Mean N inter A 590.000 2 Kontrol_
B 465.000 2 DC_4 C 445.000 2 DC_8
C C 437.500 2 TD_4
D 387.500 2 TD_16 D
D 382.500 2 TD_8 D
D 380.000 2 DC_16
c. Viskositas pasta panas VPP
