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Infinite dilution activity coefficient measurements of organic solutes in fluorinated ionic liquids by gas-liquid chromatography and the inert gas stripping method

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par Kaniki TUMBA
University of Kwazalu-Natal - Master 2009
  

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APPENDIX B: STRUCTURE OF IONIC LIQUIDS

[3C6C14P]+ [Tf2N] - [PF6]

[BF4]- [OMIM] + [SbF6]

[BMIM]+ [EMIM] + [TfO] - [C83C1N] +

Figure B-1: Ions present in the structure of ionic liquids used in this work.

Appendix C: Origin and purity of chemicals

APPENDIX C: ORIGIN AND PURITY OF CHEMICALS

Table C-1: Origin and Stated purity of solutes and solvents.

Compound

Origin

Stated purity (Mass %)

[3C6C14P] [Tf2N]

Cytec

= 0.98

[3C6C14P] [BF4]

Cytec

= 0.98

[3C6C14P] [PF6]

Cytec

= 0.98

[3C8C1N] [Tf2N]

Solvent innovation

0.98

[BMIM] [SbF6]

Capital Lab

= 0.98

[EMIM] TfO]

Capital Lab

= 0.98

[MOIM] [PF6]

Capital Lab

= 0.95

NMP

Merck

= 0.98

n-hexadecane

Acros

0.99

n-alkanes (C5 to C12)

Capital Lab

= 0.98

Alk-1-enes (C5 to C12)

Capital Lab

= 0.98

Alk-1-ynes (C5 to C12)

Capital Lab

= 0.98

Cycloalkanes (C5 to C10)

Capital Lab

= 0.98

n-alkanols (C1 to C4)

Capital Lab

= 0.98

Alkylbenzenes (C6 to C9)

Capital Lab

= 0.98

Ket-2-ones (C3 to C4)

Capital Lab

= 0.98

Table C-2: Densities of solvents after purification at different temperatures-Accuracy: #177; 0.4
%.;*Interpolated value;# Extrapolated data aFrom Rodriguez and Brennecke (2006); b From
Pereiro et al. (2007); c From Kneisl and Zondlo, (1987); d From Khasanshin et al (2009).

Solvents

293.15 K

303.15 K

313.15 K

323.15 K

333.15 K

Literature Data at
293.15 K

[3C6C14P] [Tf2N]

1.068870

1.062387

1.056497

1.051422

1.047132

 

[3C6C14P] [BF4]

-

-

-

0.925100

-

 

[3C6C14P] [PF6]

-

-

-

0.987150

-

 

[3C8C1N] [Tf2N]

1.112700

-

-

-

-

 

[BMIM] [SbF6]

1.694300

-

-

-

-

 

[EMIM] TfO]

1.387070

1.375511

1.369032

1.363705

1.359564

1.387392a*

[MOIM] [PF6]

1.238510

-

-

-

-

1.23957b

NMP

-

1.025173

1.017633

1.010888

1.004919

1.032313c#

n-hexadecane

0.770522

-

-

-

-

0.77418d#

Table C-3: Refractive indices of solvents after purification at 293.15 K. #Extrapolated data;
aMehra, (2003); bFrom www.haochem.com?; cFrom Pereiro et al. (2007).

Solvents

Refractive index

Literature Data

[3C6C14P] [Tf2N]

1.45069

 

[3C8C1N] [Tf2N]

-

 

[BMIM] [SbF6]

1.41568

 

[EMIM] TfO]

1.43434

 

[MOIM] [PF6]

1.42430

1.42440c

NMP

1.47047

1.465-1.470b

n-Hexadecane

1.43463

1.4356a#

Appendix D: Fugacities, critical data and ionization energies

APPENDIX D: FUGACITIES, CRITICAL DATA AND
IONIZATION ENERGIES

Table D-1: Saturation fugacity coefficients of selected solutes at different temperatures
determined from second virial coefficients (Smith et al (2005).

Solutes

303.15 K

313.15 K

323.15 K

n-hexane

0.982

0.977

0.970

Hex-1-ene

0.981

0.974

0.967

Cyclohexane

0.988

0.983

0.978

Methanol

0.997

0.995

0.993

Benzene

0.989

0.986

0.981

Acetone

0.988

0.984

0.980

Table D-2: Critical volumes, critical temperatures,and ionization energies, IC of the

solutes and the carrier gas used in the calculation of the virial coefficients. (Reference: CRC
Handbook of Chemistry and Physics).

Solute

TC /K

VC/ cm3.mol-1

IC/ kJ.mol-1

n-pentane

469.7

304

998.62

n-hexane

507.4

370

977.39

n-heptane

540.3

432

957.13

n-octane

568.8

492

947.48

n-nonane

594.7

555.2

937.83

Pent-1-ene

464.7

300

917.57

Hex-1-ene

504

350

910.82

Hept-1-ene

537.2

405

910.82

Oct-1-ene

566.6

464

909.85

Pent-1-yne

493.4

278

969.67

Hex-1-yne

539.29

331

960.02

Hept-1-yne

551.621

376.53

960.02

Oct-1-yne

598.46

441

960.02

Nony-1-ne

611

513.3

955.20

Cyclopentane

511.7

259

1014.05

Cyclohexane

553.8

308

951.34

Cycloheptane

604.2

353

961.95

Cyclooctane

647.2

410

941.69

Methanol

512.6

118

1046.86

Ethanol

516.2

167

1010.20

Propan-1-ol

536.7

218.5

986.07

Butan-1-ol

562.9

274

970.64

Benzene

562.1

259

892.10

Toluene

591.7

316

851.00

Acetone

508.1

209

935.90

Butan-2-one

535.6

267

918.54

Helium

5.2

57.5

2372.56

Appendix E: Calibration data

APPENDIX E: CALIBRATION DATA

y = 1.001x - 0.229
R2 = 0.999

20 30 40 50 60 70

Display Temperature, (oC)

70

Actual Temperature, (°C)

60

50

40

30

20

Figure E-1: Temperature calibration curve for the dilutor cell Pt 100.

y = 1.149x + 3.572
R2 = 0.999

84 86 88 90 92 94

Display Pressure (kPa)

112

Actual Temperature (kPa)

110

108

106

104

102

100

Figure E-2: Pressure calibration curve for the dilutor cell pressure transducer.

Appendix F: Selectivities and capacities

APPENDIX F: SELECTIVITIES AND CAPACITIES

Table F-1: Infinite dilution selectivity and capacity data at 313.15 K for FIL`s and selected industrial solvents investigated in the literature (Subscripts are references given in Chapter 6) as well as in this work*; #Data obtained at 298.15 K.

Butan-2-one (2)

Benzene (2)

Hex-1-ene (2)

Acetone (2)

Hexane (1)

/benzene (2)

Cyclohexale

(1 )/benzene (2)

Methanol (1) /benzene (2)

Benzene (1)

/butan-2-one (2)

Hexane (1)

/he(-1-ene (2)

Methanol (1) /acetone (2)

Ethanol (1)

/butan-2-one (2)

Limiting Selectivity Limiting Capacity

[EMIM][BF4][1][2]

38.65

20.06

0.17

1.54

2.02

0.39

0.47

0.41

0.02

0.91

0.62

[EMIM] [Tf2N] [3][4][5]

21.12

9.75

1.08

2.40

2.08

3.17

3.54

0.83

0.08

2.44

2.00

[MMIM] [Tf2N] [4]

27.26

15.48

-

-

2.24

-

-

0.74

0.06

-

-

[BMIM][BF4][2][6][7]

23.84

12.53

0.52

1.51

1.70

1.23

0.87

0.41

0.03

0.98

0.63

[BMIM] [Tf2N] [4][8]

15.13

9.16

1.23

-

1.89

2.97

-

1.12

0.14

2.70

-

[BMIM][TfO][9]

23.04

10.66

0.44

-

2.23

0.79

-

0.63

0.06

1.13

-

[DMPIM][BF4][10][11]

70.40

31.77

0.24

-

-

0.34

-

0.28

-

0.40

-

[EDMIM] [Tf2N] [3]

23.03

13.22

1.33

1.92

2.07

3.56

3.58

0.91

0.08

2.44

1.75

[HMIM][BF4][2][12]

19.53

5.61

0.41

1.49

2.00

0.82

1.42

0.61

0.11

1.22

0.91

[HMIM][PF6][13]

18.46

10.19

1.54

-

2.11

-

-

0.96

0.11

-

-

[HMIM] [Tf2N] [14][15][16]

11.22

6.70

1.65

1.64

1.69

3.54

3.50

1.46

0.22

3.13

2.38

[MOIM][BF4][17]

10.01

7.04

0.83

1.17

1.71

1.29

1.48

0.85

0.15

1.33

1.00

[MOIM] [Tf2N] [16]

7.89

5.52

1.75

-

1.57

-

-

1.54

0.31

-

-

[C16MIM][BF4][18]

3.10

2.13

1.52

0.76

1.35

1.29

1.47

1.27

0.55

1.08

0.96

[3C6C14P][BF4]*

3.41

2.38

1.31

0.92

1.26

1.25

1.30

2.44

0.90

2.32

2.25

[3C6C14P] [Tf2N]*

2.80

2.03

2.77

1.23

1.21

3.80

4.00

2.56

1.10

3.51

3.15

[3C6C14P][(C2F5)3PF3][20]

3.25

2.40

5.83

-

1.23

-

-

5.00

1.89

-

-

[3C1C4N] [Tf2N] [21]

13.94

0.58

1.07

-

1.89

3.38

-

0.75

0.10

2.38

-

[BMPy][BF4][22][23]

36.88

17.71

0.66

1.66

-

1.52

1.78

0.61

-

1.41

1.01

[BMPyrr] [Tf2N] [16]

15.47

-

-

1.62

1.92

-

3.26

1.16

0.14

-

1.89

[Et3S] [Tf2N] [24]

22.71

12.76

1.28

-

2.17

-

-

0.90

0.09

-

-

[Epy] [Tf2N] [25][26]

24.38

14.31

0.95

2.00

2.33

2.62

2.65

0.77

0.07

2.13

1.54

[3C6C14P][PF6]*

2.96

2.15

3.12

0.97

1.20

3.17

3.21

1.47

0.59

1.49

1.42

[C13C8N] [Tf2N] [27]*

3.77

2.70

2.68

1.22

1.33

3.11

3.44

2.27

0.80

2.63

2.78

[EMIM][TfO][28]*

30.20

15.19

0.33

-

2.31

-

-

0.45

0.03

-

-

[MOIM][PF6][29]*

11.27

7.03

1.88

-

1.72

-

-

1.04

0.16

-

-

[BMIM][SbF6][30]*

22.25

12.52

1.41

1.98

2.08

4.26

3.74

0.79

0.07

2.38

1.56

[BMIM][PF6][31]

-

-

-

-

3.06

3.06

-

-

-

1.41

1.01

[EMIM][TFA][32]

27.03

12.97

0.08

-

2.34

-

-

0.36

0.03

-

-

[HMIM][TfO][33]

14.37

7.37

-

-

-

-

-

0.68

-

-

-

[BMPyrr][TfO][34]

-

-

-

2.45

-

-

-

-

0.05

-

-

[HMPyrr] [Tf2N] [35]

-

-

-

1.70

-

-

-

-

0.22

-

-

[OMPyrr] [Tf2N] [35]

-

-

-

1.53

-

-

-

-

0.30

-

-

Sulfolane[36]

18.17

9.81

0.91

1.20

-

1.38

1.52

0.43

-

0.64

0.51

NMP[37]

11.24

7.05

-

-

0.53

-

-

0.95

0.16

-

-

Chlorobenzene[38][39]

-

-

-

-

-

0.17*

8.29

-

-

-

0.47

Dimethylsulfoxide[38][39]

-

-

-

-

-

0.35*

0.20*

-

-

0.38*

0.35*

Appendix G: Effect of structure on infinite dilution activity coefficient values

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