PMT Equilibrium Data

7/23/2019 PMT Equilibrium Data

http://slidepdf.com/reader/full/pmt-equilibrium-data 1/23

A Aseton B Chloroform

liquid vapor temp pressure

A A C mmHg

0 0 61.3 760

11.08 6.5 62.8

13.75 10 63.121.08 17.6 63.8

26.6 23.7 6.

7.71 51.7 63.!

57.5 6.8 62.8

66.33 75.05 61.6

73.88 82.35 60.

7!.55 86.88 5!.

85.! !1.65 58.3

!1.5 !5.22 57.5

100 100 56.2

K

% mol aseto

Temperatur



0 20 0 60 80 100 1200

20

0

60

80

100

120

setimbangan Aseton-Chlorofrm

Column B

Column A

% mol aseton (liquid)

n (vapor)

0 20 0 60 80 100 120

52

556

58

60

62

6

66

Sistem Aseton-Chloroform

#iquid

$apor

Komposisi aseton (%mol)

(ᵒC)



A Aseton B %thanol


A A C mmHg

0 0 78.3 760

5 15.5 75.

10 26.2 7315 3.8 71

20 1.7 6!

25 7.8 67.3

30 52. 65.!

35 56.6 6.7

0 60.5 63.6

50 67. 61.8

60 73.! 60.

70 80.2 5!.1

80 86.5 58!0 !2.! 57

100 100 56.1

% mol aseto

Temperatur



0 20 0 60 80 100 1200

20

0

60

80

100

120

esetimbangan aseton-ethanol

Column B

Column A


n (vapor)

0 20 0 60 80 100 120

Sistem Aseton-Ethanol

#iquid

$apor


(ᵒC)



A Aseton B &ater


A A C mmHg

5 62 7 760

8.2 72 68.!

12.5 77.1 65.822 80 62.!

.5 83.1 62.7

66 86.6 58.3

76 88.8 57.8

86.5 !3 57.3

!3 !6 56.7

% mol asetoTemperatur



0 10 20 30 0 50 60 70 80 !0 100

0

20

0

60

80

100

120

Kesetimbangan Aseton- ater

Column B


n (vapor)

0 20 0 60 80 100 120

Sistem Aseton-!ater

#iquid

$apor


(ᵒC)



A 'hloroform B (en)ene


A A C mmHg

0 0 80.6 760

8 10 7!.8

15 20 7!22 30 78.2

2! 0 77.3

36 50 76.

60 75.3

5 70 7

66 80 71.!

7! !0 68.!

100 100 61.

Kes

% mol #hlor

Temperatur



0 20 0 60 80 100 1200

20

0

60

80

100

120

timbangan Chloroform - ben"ene

Column B

Column A

% mol #hloroform (liquid)

form (vapor)

0 20 0 60 80 100 120

60

65

70

75

80

85

Sistem Chloroform-$en"ene

#iquid

$apor

Komposisi Chloroform (%mol)

(ᵒC)



A ethanol B (en)ene


A A C mmHg

3 5.8 78 760

2.7 11.3 77.1

3.7 20.2 755.1 22 7.6

7.25 25.2 72.8

7.6 30.3 71.2

10. 3.3 70.3

12.2 37.3 6!

1. 1.! 68.5

2 2 68.3

32.6 2.2 68.1

33.2 2.5 68

38.2 2.6 67.!2.5 .1 67.!

7. .7 67.!

52.3 6.2 68

56. 7.7 68

61.3 8.2 68.1

66.1 !.8 68.2

68.7 51.8 68.3

73 52. 68.6

76.1 5.1 68.8

Temperatur



0 10 20 30 0

10

20

30

0

50

60

Kesetimbangan eth

% mol ethan

% mol ethanol (vapor)

0 10 20 30 0 50 60 70 80

60

65

70

75

80

Sistem Ethanol-$en"ene

#iquid

$apor

Komposisi ethanol (%mol)

(ᵒC)



50 60 70 80

nol ben"ene

Column B

l (liquid)



A ethanol B &ater


A A C mmHg

0 0 100 760

1.! 17 !5.5

7.21 38.!1 8!!.66 3.75 86.7

12.38 7.0 85.3

16.61 50.8! 8.1

23.37 5.5 82.7

26.08 55.8 82.3

32.73 58.26 81.5

3!.65 61.22 80.7

50.7! 65.6 7!.8

51.!8 65.!! 7!.7

57.32 68.1 7!.367.63 73.85 78.7

7.72 78.15 78.1

8!.3 8!.3 78.15

% mol etha

Temperatur



0 20 0 60 80 1000

20

0

60

80

100

esetimbangan ethanol-ater

Column B

Column A

% mol ethanol (liquid)

ol (vapor)

0 10 20 30 0 50 60 70 80 !0 100

70

80

!0

100

110

Sistem Ethanol-!ater

#iquid

$apor

Komposisi Ethanol (%mol)

(ᵒC)



A eth*l a'etate B ethanol


A A C mmHg

0 0 78.3 760

5 10.2 76.6

10 18.7 75.520 30.5 73.!

30 38.! 72.8

0 5.7 72.1

50 51.6 71.8

5 5 71.8

60 57.6 71.!

70 6. 72.2

80 72.6 73

!0 83.7 7.7

!5 !1. 76100 100 77.1

Kese

% mol ethl

Temperatu



0 20 0 60 80 100 1200

20

0

60

80

100

120

timbangan ethl a#etate - ethanol

Column B

Column A

% mol ethl a#etate (liquid)

a#etate ( vapor)

0 20 0 60 80 100 120

68

70

72

7

76

78

80

Sistem ethl a#etate - ethanol

#iquid

$apor

Komposisi ethl a#etate (%mol)

r (ᵒC)



A eth*l (romide B (en)ene


A A C mmHg

0 0 80.2 760

1 10 7!.

2 20 78.5 30 77.

6 0 76.1

8 50 7.7

10 60 72.8

1 70 70.5

21 80 66.8

3 !0 5!.8

61 !7 !.2

100 100 38.

Keset

% mol ethl

Temperatur



0 20 0 60 80 100 1200

20

0

60

80

100

120

imbangan ethl bromide - ben"ene

Column B

Column A

% mol ethl bromide (liquid)

bromide (vapor)

0 20 0 60 80 100 120

istem ethl bromide - ben"ene

#iquid

$apor

Komposisi ethl bromide (%mol)

(ᵒC)



A eth*l ether B 'ar(on tetra'hloride


A A C mmHg

0 0 77.75 760

18.8 !.6 73.7

3.2 6!.6 6!.737.1 7!.6 65.5

58 85.8 61.

67.5 !0.1 57.16

75.7 !3.2 53.0!

82.! !6 8.!8

8!.2 !8 .8

!5 !!.2 1.35

100 100 3.75

Kesetim

% mol et

Siste

Temperatur



0 20 0 60 80 100 1200

20

0

60

80

100

120

angan ethl ether - #arbon tetra#hloride

Column B

Column A

% mol ethl ether (liquid)

l ether (vapor)

0 20 0 60 80 100 120

30

0

50

60

70

80

ethl ether - #arbon tetra#hloride

#iquid

$apor

Komposisi ethl ether (%mol)

(ᵒC)



A methanol B (en)ene


A A C mmHg

6!. 760

2.8 31 66.8

5 3!.5 65.75.7 2 61.

! 8.5 5!

11.8 56.5 5!.2

12 56 58

27 57.5 57.8

58.5 57.7

58.6 61 57.6

6!.5 62.5 58.1

81.7 65.5 58.!

88.3 70 5!.6!0.2 73 60.

!3. 80.1 61.2

!.5 82.2 62.

!6.8 !0 63.

!8.8 !.2

Ke

% mol meth

Temperatur



0 20 0 60 80 100 1200

20

0

60

80

100

etimbangan methanol-ben"ene

Column B

% mol methanol (liquid)

anol (vapor)

0 20 0 60 80 100 120

50

55

60

65

70

Sistem &ethanol-$en"ene

#iquid

$apor

Komposisi methanol (%mol)

(ᵒC)



volume temperature

0 6

10 50

20 51

30 53.5

0 5

50 5560 56.5

70 57.5

80 58.5

!0 61'ra

Temperatue



0 10 20 30 0 50 60 70 80 !0 100

0

10

20

30

0

50

60

70

f+,- 0.136363636, / 7.836363636

0.!610!02!31

ubungan antara*olume vs Temperatur

Column B

#inear +Column B-

*olume +,stilat (ml)

(ᵒC)

Documents

PMT Equilibrium Data