Industri Dimetyleter Kelas b

7/23/2019 Industri Dimetyleter Kelas b

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0 0.01 0.02 0.03

0

20000

40000

60000

80000

100000

f(x) = 406264.09x + 34515.54

R² = 0.14

f(x) = 862549.86x + 66970.2

R² = 0.44

f(x) =

R² = 0

plate & frame 1

Linear (plate & frame 1)

plate & frame 2


plate & frame 3


v(m3)

v/t(s/m3)

0 0.010.010.020.020.03

0

10000

20000

30000

40000

50000

60000

70000

f(x) = 388121.08x + 27623.82R² = 0.32

f(x) = 337598.42x + 50177.05

R² = 0.22

f(x) =

R² = 0

plate & frame 1


plate & frame 2


plate & frame 3


v(m3)

v/t(s/m3)



0 0.01 0.01 0.02 0.02 0.03

0

20000

40000

60000

80000

f(x) = 217492.32x + 19615.56

R² = 0.16

f(x) = 259938.26x + 50033.44

R² = 0.08

f(x) =

R² = 0

plate & frame 1 Linear (plate & frame 1)



v(m3)

v/t(s/m3)



0 1 2 3 4

0

20

40

60

80

100

120

f(x) = 1.09x + 97.51

R² = 0.22

f(x) = 10.31x + 110.28

R² = 0.85

f(x) = 9.64x + 109.45

R² = 0.79 !"n#entra#i 1$

Linear (!"n#entra#i 1$)

!"n#entra#i 1.5$

Linear (!"n#entra#i

1.5$)

!"n#entra#i 2$

Linear (!"n#entra#i 2$)

jumlah plate

efsiensi CaCO3 (%)

0 1 2 3

0

20

40

60

80

100

120

f(x) = 17.78x + 56.64

R² = 0.72

f(x) = 2.94x + 98.93

R² = 1

f(x) = 0.67x + 96.33

R² = 0.85

plate & frame 1Linear (plate & frame 1)

plate& frame 2

Linear (plate& frame 2)

plate & frame 3


konsentrasi (%)

efsiensi CaCO3 (%)



0 1 2 3 40.00%+00

1.00%+13

2.00%+13

3.00%+13

4.00%+13

5.00%+13

6.00%+137.00%+13

8.00%+13

f(x) = 7737300000000x + 24482496666666.7

R² = 0.89

f(x) = 36126425000000x + 100651123333333

R² = 0.79

f(x) = 164945000000x + 5522666666666.67

R² = 0

!"naentra#i 1 $

Linear (!"naentra#i 1

$)

!"n#entra#i 1.5 $

Linear (!"n#entra#i

1.5 $)

!"n#entra#i 2 $

Linear (!"n#entra#i 2

$)

Jumlah Plate

Rm (m-1)

0.8 1 1.21.41.61.8 2 2.20.00%+00

1.00%+13

2.00%+13

3.00%+13

4.00%+135.00%+13

6.00%+13

7.00%+13

8.00%+13

f(x) = 1375930000000x + 5453255000000

R² = 0.85

f(x) = 3586610000000x + 12727401666666.7

R² = 0.94

f(x) = 14428560000000x + 10879040000000

R² = 0.04

plate 1Linear (plate 1)

plate 2

Linear (plate 2)

plate 3

Linear (plate 3)

konsentrasi (%)

Rm (m-1)



0.5 1 1.5 2 2.5 3 3.50

20

40

60

80

100

120

f(x) = 5.54x + 79.87

R² = 0.3

f(x) = 7.82x + 79.8

R² = 1

f(x) = 8.75x + 81.31R² = 0.93"n#entra#i 1 $ Linear ("n#entra#i 1 $)

"n#entra#i 1.5 $ Linear ("n#entra#i 1.5 $)

"n#entra#i 2 $ Linear ("n#entra#i 2 $)

Jumlah Plate

efsiensi HO (%)

0.5 1 1.5 2 2.50

20

40

60

80

100

120

f(x) = 11.09x + 74.33

R² = 0.3

f(x) = 4.84x + 90.34

R² = 0.74f(x) = 11x + 102.93

R² = 0.98 plate 1Linear (plate 1)

plate 2

Linear (plate 2)

plate 3

Linear (plate 3)

konsentrasi (%)

efsiensi HO (%)



0.5 1 1.5 2 2.5

0

0.01

0.01

0.02

14

15

16

17

18

19

f(x) = 2.2x + 20.59

R² = 0.98f(x) = 0x + 0

R² = 0.95

plate !"rame 1

'a'3 0t Linear ('a'3 0t) *2 "t

Linear (*2 "t)

konsentrasi (%)

CaCO3 out (k#) HO out (k#)

0.8 1 1.21.41.61.8 2 2.2

0

0.01

0.02

0.03

18.5

19

19.5

20

20.5

f(x) = 0.97x + 18.07

R² = 0.74

f(x) = 0.03x 0.02

R² = 1

plate ! "rame

'a'3 "t Linear ('a'3 "t ) *2 "t

Linear (*2 "t)

konsentrasi (%)

CaCO3 out(k#) HO out( k#)



0.8 1 1.21.41.61.8 2 2.2

0

0.02

0.04

0.06

0.08

0

5

10

15

20

25

f(x) = 2.6x + 14.58

R² = 0.32

f(x) = 0.01x + 0.02

R² = 0.02

plate ! "rame 3

'a'3 "t Linear ('a'3 "t) *2 "t

Linear (*2 "t)

konsentrasi (%)

CaCO3 out(k#) HO out( k#)

0.8 1 1.2 1.4 1.6 1.8 2 2.25.00%+13

0.00%+00

5.00%+13

1.00%+14

1.50%+14

2.00%+14

2.50%+14

3.00%+14

3.50%+14

4.00%+14

4.50%+14

L,-% 1

L,-% 2

L,-%3

$O&'R&* (%)

+, ()



0.5 1 1.5 2 2.5 3 3.55.00%+13

0.00%+00

5.00%+13

1.00%+14

1.50%+14

2.00%+14

2.50%+14

3.00%+14

3.50%+14

4.00%+14

4.50%+14

/%-R,/ 1$

/%-R,/ 1.5$

/%-R,/ 2 $

Jumlah Plate

+, ( )

Industri Dimetyleter Kelas b

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