Data Praktikum Fluidisasi

Percobaan 1Penurunan Laju Alir

Q(L/s) p1(mmH20) p2(mmH20) Hb(cm) h0(cm)1.7 3 3.7 0.7 16 5.5 10.51.6 3 3.75 0.75 15.6 5.5 10.11.4 2.8 3.7 0.9 14.4 5.5 8.91.2 2.6 3.65 1.05 13 5.5 7.5

1 2.5 3.5 1 11.8 5.5 6.30.8 2.3 3.45 1.15 9.5 5.5 40.6 2.3 3.2 0.9 6.3 5.5 0.80.4 2.3 2.9 0.6 5.5 5.5 00.2 2.3 2.6 0.3 5.5 5.5 0

0.15 2.3 2.5 0.2 5.5 5.5 0

Kenaikan Laju AlirQ(L/s) p1(mmH20) p2(mmH20) Hb(cm) h0(cm)

0.15 2.3 2.6 0.3 5.5 5.5 00.2 2.3 2.65 0.35 5.5 5.5 00.4 2.3 3 0.7 5.5 5.5 00.6 2.3 3.3 1 5.5 5.5 00.8 2.3 3.45 1.15 8.6 5.5 3.1

1 2.4 3.6 1.2 9.8 5.5 4.31.2 2.6 3.7 1.1 12.2 5.5 6.71.4 2.7 3.75 1.05 14.5 5.5 91.6 2.9 3.8 0.9 15.4 5.5 9.91.7 3 3.75 0.75 17.2 5.5 11.7

DP(mmH20) DH(cm)

DP(mmH20) DH(cm)

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.80.1

1

10

f(x) = − 0.275495750708216 x + 1.24808781869688f(x) = 1.53694581280788 x − 0.0187192118226599penurunan laju alir

Linear (penurunan laju alir)kenaikan laju alir

Laju Alir (L/s)

ΔP (m

mH2

O)

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.80

5

10

15

20

25

30

-1

1.5

4

∆H vs U

∆P vs U

Laju Alir (L/s)

ΔH (c

m)

ΔP (m

mH2

O)

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.80

2

4

6

8

10

12

14

f(x) = 9.16949152542373 x − 4.2

f(x) = 10.65 x − 6.06

f(x) = 0

kenaikan laju alirLinear (kenaikan laju alir)penurunan laju alir

Laju Alir (L/s)

ΔH (c

m)

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.80

5

10

15

20

25

30

-1

1.5

4

∆H vs U

∆P vs U

Laju Alir (L/s)

ΔH (c

m)

ΔP (m

mH2

O)

1.7Percobaan Kedalaman heater T1 Kedalaman Termocouple Voltase Ampere

1 adidalam unggun 60

didalam unggun (67) 200 2.5b diatas unggun (58) 200 2.5

2 adiatas unggun 80




4 adiatas unggun 60




6 adiatas unggun 100





2 adiatas unggun 80




4 adiatas unggun 60






1Percobaan Kedalaman heater T1 Kedalaman Termocouple Voltase Ampere



2 adiatas unggun 80

didalam unggun (88) 200 2.5b diatas unggun 82 200 2.5


didalam unggun 98 200 2.5b diatas unggun 101 200 2.5

4 adiatas unggun 60









2 adiatas unggun 80




4 adiatas unggun 60









2 adiatas unggun 80




4 adiatas unggun 60






0Percobaan Kedalaman heater T1 Kedalaman Termocouple Voltase Ampere



2 adiatas unggun 80

didalam unggun (93 ) 200 2.5b diatas unggun (88 ) 200 2.5


didalam unggun ( 148 ) 200 2.5b diatas unggun (103 ) 200 2.5

4 adiatas unggun 60

didalam unggun (72 ) 200 2.5b diatas unggun( 78 ) 200 2.5


didalam unggun ( 79 ) 200 2.5b diatas unggun (94 ) 200 2.5


didalam unggun (122 ) 200 2.5

b diatas unggun 100 diatas unggun (96 ) 200 2.5

T2 T3 Hb36 37 16.4 0.234 35 17 0.837 34 17.5 0.7538 35 18 0.6537 34 17 0.738 34 16.7 0.733 34 16.6 0.6535 35 16.4 0.7537 35 16.7 0.7537 36 16.4 0.737 35 17.8 0.736 34 17.2 0.65

T2 T3 Hb39 33 15.3 0.9539 33 14.3 0.938 34 14.3 0.938 34 14.6 0.940 34 15 0.9541 33 15.3 1.137 34 14.3 0.940 33 14.5 0.939 33 14.8 0.938 33 15.2 0.941 34 15.3 1.141 34 14.6 1.1

T2 T3 Hb36 31 10.4 1.135 31 10.5 1.137 30 10.6 1.138 31 10.3 1.136 30 10.4 1.1536 30 10.7 1.136 33 10.2 1.0536 32 10.8 1.1537 31 11 1.138 30 10.5 1.136 31 10.8 135 30 9.9 1.1

DP

DP

DP

T2 T3 Hb50 30 8.9 1.248 29 8.6 1.249 30 8.5 1.148 29 8.8 1.137 30 8.8 1.1542 30 9 1.1545 29 8.7 1.1545 30 9 1.146 29 9 1.1542 30 9.1 1.148 30 8.7 1.142 30 9.2 1.1

T2 T3 Hb38 30 5.5 0.741 30 5.5 0.736 31 5.5 0.736 30 5.5 0.735 31 5.5 0.735 31 5.5 0.743 30 5.5 0.743 30 5.5 0.738 31 5.5 0.738 30 5.5 0.736 31 5.5 0.736 30 5.5 0.7

T2 T3 Hb32 31 5.5 0.231 31 5.5 0.1537 31 5.5 0.237 31 5.5 0.1538 31 5.5 0.1535 31 5.5 0.1536 31 5.5 0.1536 31 5.5 0.235 31 5.5 0.232 31 5.5 0.237 32 5.5 0.15

DP

DP

DP

35 31 5.5 0.2

Data Praktikum Fluidisasi

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