Low Environmental Impact Refrigerant Gas Mixtures

申请号 US14651763 申请日 2013-12-18 公开(公告)号 US20150328489A1 公开(公告)日 2015-11-19
申请人 TAZZETTI S.P.A.; 发明人 Riccardo Mondino;
摘要 Use of a gas mixture selected from the group comprising:—trifluoroiodomethane (CF3I) in concentrations from 85% to 99% by weight and a gas selected from the group comprising fluoroethane, pentafluoroiodoethane, pentafluoroethane, dimethyl ether, propylene or their mixtures in concentrations from 15% to 1% by weight as refrigerant, propellant, foaming and/or extinguishing gases as replacements or alternatives for other gases or HFC (hydrofluorocarbon), HFO (hydrofluoro-olefin) and HFE (hydrofluoroether) mixtures.
权利要求 1. Gas mixture for use as a refrigerant, propellant gas, expanding or extinguishing agent comprising:trifluoroiodomethane (CF3I) in a concentration from 81% to 99% by weight anda gas selected from the group comprising fluoroethane, dimethyl ether, pentafluoroiodoethane, pentafluoroethane, propylene or mixtures thereof in a concentration from 15% to 1% by weight, the concentrations relating to the total weight of the mixture.2. Gas mixture according to claim 1 comprising:trifluoroiodomethane (CF3I) in a concentration from 90% to 99% by weight anda gas selected from the group comprising pentafluoroiodoethane, pentafluoroethane and mixtures thereof in a concentration from 10 to 1% by weight.3. Gas mixture according to claim 1, selected from the group comprising:from 85 to 95% by weight of trifluoroiodomethane and from 15% to 5% by weight of fluoroethane, or 85% by weight of trifluoroiodomethane and 15% by weight of fluoroethane;from 85 to 99% by weight of trifluoroiodomethane and from 15 to 1% by weight of dimethyl ether, or 87% by weight of trifluoroiodomethane and 13% by weight of dimethyl ether;from 90 to 95% by weight of trifluoroiodomethane and from 10 to 5% by weight of propylene, or 90% by weight of trifluoroiodomethane and 10% by weight of propylene.4. Gas mixture according to claim 1, selected from the group comprising:from 90 to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of fluoroethane, or 97.5% by weight of trifluoroiodomethane and 2.5% by weight of fluoroethane;from 90 to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of pentafluoroiodoethane, or 95% by weight of trifluoroiodomethane and 5% by weight of pentafluoroiodoethane;from 90 to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of dimethyl ether, or 95% by weight of trifluoroiodomethane and 5% by weight of dimethyl ether, andfrom 90% to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of propylene, or 97.5% by weight of trifluoroiodomethane and 2.5% by weight of propylene.5. The gas mixture according to claim 1, wherein the gas mixture is capable of use as a refrigerant gas and/or propellant as a replacement or alternative for fluids containing HFCs (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).6. The gas mixture according to claim 5, in which the said gas mixture comprises:trifluoroiodomethane in a concentration from 85 to 99% by weight anda gas selected from the group comprising fluoroethane, dimethyl ether, propylene or mixtures thereof in a concentration from 15 to 1% by weight as a refrigerant gas and/or propellant as a replacement or alternative for R134a and/or other refrigerants and/or propellant replacements or alternatives for R134a containing HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).7. The gas mixture according to claim 6, in which the said gas mixture comprises:from 85 to 95% by weight of trifluoroiodomethane and from 15% to 5% by weight of fluoroethane, or 85% by weight of trifluoroiodomethane and 15% by weight of fluoroethane;from 85 to 99% by weight of trifluoroiodomethane and from 15 to 1% by weight of dimethyl ether or 87% by weight of trifluoroiodomethane and 13% by weight of dimethyl ether;from 90 to 95% by weight of trifluoroiodomethane and from 10 to 5% by weight of propylene, or 90% by weight of trifluoroiodomethane and 10% by weight of propylene.8. The gas mixture according to claim 5 in which the said gas mixturefrom 90 to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of fluoroethane, or 97.5% by weight of trifluoroiodomethane and 2.5% by weight of fluoroethane;from 90 to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of pentafluoroiodoethane, or 95% by weight of trifluoroiodomethane and 5% by weight of pentafluoroiodoethane;from 90 to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of dimethyl ether, or 95% by weight of trifluoroiodomethane and 5% by weight of dimethyl ether, andfrom 90% to 99% by weight of trifluoroiodomethane and from 10 to 1% by weight of propylene, or 97.5% by weight of trifluoroiodomethane and 2.5% by weight of propylene.9. The gas mixture according to claim 5, in which the said gas mixture is capable of use in air conditioning systems of motor vehicles, refrigerated counters for supermarkets, cold stores, domestic refrigerators, centrifugal chillers, domestic, commercial and industrial air conditioning systems, domestic, commercial and industrial chillers, air conditioning and refrigeration plant in the process industry, refrigerated transport, chilled water dispensers, commercial ice machines and domestic, commercial and industrial dehumidifiers.10. The gas mixture according to claim 5, in which the said gas mixture is capable of use as propellant in pressurised containers, deodorants, cosmetic and personal hygiene products, in machines for aerosols, in compressed air guns, or in spray products in different fields such as personal care, home care, insecticides, paints, lubricants and technical products.11. The gas mixture according to claim 1, wherein the gas mixture is capable of use as a foaming and/or expanding gas, as a replacement or alternative for HFCs (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).12. The gas mixture according to claim 11 in which the said gas mixture is capable of use as an expanding agent for the production of rigid insulating polyurethane foam, flexible polyurethane products and seals, polyurethane products in contact with human skin, polyurethane or phenolic or polystyrene sheets and insulating panels, expanded products for the insulation of cold stores, homes, automotive upholstery.13. The gas mixture according to claim 2, in which the gas mixture is capable of use as an extinguishing gas, as a replacement or alternative for HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).14. The gas mixture according to claim 13 in which the said gas mixture is capable of use as an automatically discharged fire-fighting agent in unoccupied and non-residential confined areas.15. The gas mixture according to claim 13 in which the said gas mixture is capable of use as a fire-fighting agent in portable fire extinguishers other than in a residential environment.16. Air conditioning or refrigeration systems containing a gas mixture according to claim 1.17. Air conditioning or refrigeration systems according to claim 16, wherein the gas mixture is capable of use in comprising air-conditioning systems for motor vehicles, refrigerated counters for supermarkets, cold stores, home refrigerators, centrifugal chillers, domestic, commercial and industrial air conditioning, domestic, commercial and industrial chillers, air-conditioning and refrigeration plant in the process industry, refrigerated transport, chilled water dispensers, commercial ice machines and domestic, commercial and industrial dehumidifiers.18. A method for retrofitting conditioning or refrigeration systems, comprising replacing the refrigerant gas used in these systems with a gas mixture according claim 1.
说明书全文

This invention relates to gas mixtures which are useful as refrigerants, propellants, extinguishing and/or expanding agents as replacements or alternatives for R134a or gases containing HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).

R134a (1,1,1,2-tetrafluoroethane) is a hydrofluorocarbon that has been used since the early 90s as a refrigerant gas as a substitute for chlorofluorocarbons or hydrochlorofluorocarbons having a significant ozone depletion potential (hereinafter ODP) which have been regulated following the Montreal Protocol.

Unlike chlorofluorocarbons and hydrochlorofluorocarbons, R134a has a non-significant ODP and has and is finding application in particular as a refrigerant in air-conditioning or refrigeration.

R134a nevertheless has a high global warming potential (hereinafter GWP) and subsequent to the Kyoto Protocol, European regulation has restricted it and is progressively restricting its availability and use in air conditioning or refrigeration systems.

The primary object of this invention is to provide refrigerating, propellant and/or expanding gas mixtures which can be used as a replacement or alternative for R134a and/or other gases as replacements or alternatives for R134a containing HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers), which have a lower production cost and better environmental impact properties, particularly in terms of GWP, than R134a together with thermodynamic properties which render them suitable for use as replacement refrigerant gases having improved characteristics for motor vehicle air-conditioning, domestic, commercial and industrial air-conditioning and refrigeration applications.

The invention is based on recognition of the fact that the abovementioned objects can be achieved using a gas mixture which comprises trifluoroiodomethane in combination with specific halogenated or non-halogenated hydrocarbons in specific relative concentrations of the mixture constituents.

Binary mixtures of hydrocarbons containing trifluoroiodomethane have already been proposed in the prior art as refrigerating gases—for example JP2009001651 refers to a refrigerating mixture of CF3I and HFC-152a, having compositions between 50% and 80% of trifluoroiodomethane.

JP2010116506 describes mixtures comprising CF3I and HFC-152a as components of a propellant mixture, in which trifluoroiodomethane may be present in concentrations from 66% to 77% by weight.

WO0039242 describes mixtures comprising CF3I in quantities from 10% to 60% by weight and R-161 in quantities from 40% to 90% by weight as refrigerants replacing R22 and R502.

In this respect this invention provides mixtures which, through specific selection of the concentration ranges of the halogenated hydrocarbons used, have a low GWP of in any event less than 150 and tend to have non-flammability aspects because R134a or HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and FIFE (hydrofluoroethers) have been replaced.

The object of the invention comprises gas mixtures as defined in the appended claims and uses of the aforesaid mixtures in the applications defined in the claims.

One aspect of the invention relates to the use of a gas mixture comprising trifluoroiodomethane (CF3I) in a concentration from 85% to 99% by weight and a gas selected from the group comprising fluoroethane, pentafluoroiodoethane, dimethyl ether, propylene or their mixtures in a concentration from 15% to 1% by weight as a refrigerant, propellant and/or expanding gas as a replacement or alternative for R134a and/or other refrigerants which are replacements or alternatives containing HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers) in air-conditioning or refrigeration systems, in particular in motor vehicle air conditioning systems designed for the use of R134a.

When used as a refrigerant the mixtures according to the invention find application in both newly manufactured systems and as retrofits for existing systems, requiring only the replacement of a few components as the mixtures according to the invention have been designed to have non-flammability properties similar to those of R134a.

In particular, the mixtures according to the invention find application in motor vehicle air-conditioning systems, refrigerated counters for supermarkets, cold stores, domestic refrigerators, centrifugal chillers, domestic, commercial and industrial air-conditioning systems, domestic, commercial and industrial chillers, air-conditioning or refrigeration plant in the processing industry, refrigerated transport, chilled water dispensers, commercial ice machines and domestic, commercial and industrial dehumidifiers.

Air-conditioning or refrigeration systems which use mixtures according to the invention as a refrigerant fall within the scope of the invention.

Refrigerant mixtures comprising trifluoroiodomethane (CF3I) in a concentration from 85% to 99% by weight and a gas selected from the group comprising fluoroethane, pentafluoroiodoethane, dimethyl ether, propylene or their mixtures in a concentration from 15% to 1% by weight also constitute an object of the invention.

Within the concentration range of the gases comprising the mixtures the following mixtures are preferred as replacements or alternatives for R134a:

TABLE 1

Preferred

Preferred

Fluids

composition range

R134a

trifluoroiodomethane

85-95%

85%

fluoroethane

 15-5%

15%

trifluoroiodomethane

90-95%

90%

propylene

 10-5%

10%

trifluoroiodomethane

85-99%

87%

dimethyl ether

 15-1%

13%

trifluoroiodomethane

90-99%

pentafluoroiodomethane

 10-1%

The mixtures proposed in Table 1 have improved characteristics in comparison with the use of R134a in refrigeration cycles for medium and high temperature applications.

Another aspect of the invention relates to the use of a gas mixture selected from the group comprising trifluoroiodomethane (CF3I) in a concentration from 85% to 99% by weight and a gas selected from the group comprising fluoroethane, pentafluoroiodoethane, dimethyl ether, propylene or their mixtures in a concentration from 15% to 1% by weight as a refrigerant and/or propellant gas as a replacement or alternative for other refrigerant and/or propellant gases containing HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).

In particular, the mixtures according to the invention find application in motor vehicle air-conditioning systems, refrigerated counters for supermarkets, cold stores, domestic refrigerators, centrifugal chillers, domestic, commercial and industrial air-conditioning systems, domestic, commercial and industrial chillers, air-conditioning or refrigeration plant in the processing industry, refrigerated transport, chilled water dispensers, commercial ice machines and domestic, commercial and industrial dehumidifiers.

Air-conditioning or refrigeration systems which use mixtures according to the invention as a refrigerant fall within the scope of the invention.

Furthermore, mixtures according to the invention find application as propellants in pressure vessels, deodorants, foams, cosmetic and personal hygiene products, aerosols, compressed air guns and also in spray products in various fields such as: personal care, home care products, insecticides, paints, lubricants and technical products in general.

Within the concentration range of the gases comprising the mixtures the following mixture compositions are preferred:

TABLE 2

Composition

Fluids

range

Preferred

trifluoroiodomethane

90-99%

97.5%

fluoroethane

 10-1%

2.5%

trifluoroiodomethane

90-99%

97.5%

propylene

 10-1%

2.5%

trifluoroiodomethane

90-99%

95.0%

dimethyl ether

 10-1%

5.0%

trifluoroiodomethane

90-99%

95.0%

pentafluoroiodoethane

 10-1%

5.0%

Appended table (Table 3) illustrates some salient characteristics relating to the thermodynamic properties of the mixtures according to the invention within the concentration ranges mentioned above, together with their salient environmental impact characteristics (GWP), in comparison with the corresponding properties of R134a, R1234ze and R1234yf.

TABLE 3

T

Fluids

Boiling point

Glide K

GWP

R134a

−26.3

1300

R1234ze

−18.9

4

R1234yf

−29.5

4

CF3I/fluoroethane

−35.8 to −24.6

3.4-1.9

<2

CF3I/propylene

−39.9 to −24.5

6.8-1.8

<3

CF3I/pentafluoroiodoethane

−19.2 to −21.7

4.1-0.2

<2

CF3I/dimethyl ether

−27.3 to −22.9

0.1-0.5

<3

As may be seen from Table 3 above, the mixtures used according to the invention have low glide values (difference between the boiling point and the dew point at a pressure of 1 atmosphere).

In comparison with R134a, the mixtures drastically reduce the GWP from 1300 to values which do not in any event exceed 27.

Another aspect of the invention relates to use of a gas mixture selected from the group comprising:

    • trifluoroiodomethane (CF3I) in concentrations from 85% to 99% by weight and a gas selected from the group comprising fluoroethane, pentafluoroiodoethane, dimethyl ether, propylene or their mixtures in concentrations from 15% to 1% by weight as an expanding gas as a replacement or alternative for HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers)
    • trifluoroiodomethane (CF3I) in concentrations from 85% to 99% by weight and a gas selected from the group comprising pentafluoroiodoethane, pentafluoroethane or their mixtures in concentrations from 15% to 1% by weight as extinguishing gases as a replacement or alternative for HFC (hydrofluorocarbons), HFO (hydrofluoro-olefins) and HFE (hydrofluoroethers).

In particular, the use as an expanding agent relates to the production of rigid insulating polyurethane foams, flexible polyurethane products and seals, polyurethane products in contact with human skin, polyurethane or phenolic or polystyrene insulating sheets or panels, expanded products for the lagging of cold stores, homes and automotive upholstery.

In the appended drawings:

FIGS. 1 to 3 are diagrams illustrating pressure and temperature graphs for the preferred mixtures according to the invention in comparison with the corresponding graphs for R134a; the corresponding numerical values are shown in Tables 5 to 7,

FIGS. 4 to 7 are diagrams illustrating pressure and temperature graphs for the preferred mixtures according to the invention in comparison with the corresponding graphs for R1234ze; the corresponding numerical values are shown in Tables 8 to 11.

A comparison table between R134a, R1234ze, R1234yf and some replacements which are the subject of this invention is presented below.

TABLE 4

%

Refrigerant

COPh

COPc

pure

R134a

4.693

3.695

pure

R1234ze

4.688

3.690

pure

R1234yf

4.580

3.582

87/13

CF3I/DME

4.746

3.748

85/15

CF3I/R161

4.513

3.515

90/10

CF3I/propylene

4.457

3.459

The table describes the performance coefficients (COP) for specific mixtures which are the object of the invention, comparing these with R134a, R1234ze and R1234yf.

Performance coefficient values for heating (COPh) and cooling (COPc) are indicated in the table.

The values have been calculated for an air-conditioning system having a cooling potential of 17.5 thermal kW, 500 We of auxiliary power and supercooling of 5° C. The excess heat has been regarded as additional heat to the condenser.

The values indicated are the product of a mathematical simulation based on thermodynamic data known from the literature, making use of programs which are recognized internationally.

It will be seen that in all cases the COP for the proposed mixtures is wholly in line in comparison with R134a, R1234ze and R1234yf.

TABLE 5

CF3I/R161 (85/15): P/T Table

P

T

R134a

PL mix

PV mix

° C.

atm

atm

atm

−100

0.006

0.017

0.012

−95

0.009

0.026

0.019

−90

0.015

0.039

0.029

−85

0.024

0.057

0.044

−80

0.036

0.082

0.063

−75

0.054

0.116

0.090

−70

0.079

0.160

0.126

−65

0.112

0.217

0.172

−60

0.157

0.290

0.232

−55

0.215

0.381

0.307

−50

0.291

0.495

0.401

−45

0.386

0.634

0.517

−40

0.505

0.802

0.659

−35

0.653

1.003

0.830

−30

0.833

1.242

1.035

−25

1.050

1.523

1.277

−20

1.310

1.850

1.561

−15

1.618

2.230

1.893

−10

1.980

2.666

2.276

−5

2.402

3.163

2.716

0

2.890

3.728

3.219

5

3.451

4.366

3.789

10

4.092

5.081

4.434

15

4.820

5.880

5.157

20

5.642

6.768

5.966

25

6.567

7.752

6.867

30

7.601

8.837

7.866

35

8.754

10.028

8.970

40

10.033

11.333

10.186

45

11.448

12.757

11.520

50

13.007

14.307

12.980

55

14.720

15.989

14.575

60

16.598

17.810

16.312

65

18.651

19.776

18.201

70

20.891

21.896

20.252

75

23.332

24.177

22.476

80

25.988

26.626

24.886

85

28.876

29.253

27.498

90

32.018

32.066

30.332

95

35.443

35.074

33.417

100

39.204

38.283

36.799

TABLE 6

CF3I/Propylene (90/10): P/T Table

P

T

R134a

PL mix

PV mix

° C.

atm

atm

atm

−100

0.006

0.021

0.011

−95

0.009

0.032

0.018

−90

0.015

0.048

0.027

−85

0.024

0.068

0.040

−80

0.036

0.096

0.058

−75

0.054

0.133

0.083

−70

0.079

0.181

0.115

−65

0.112

0.241

0.158

−60

0.157

0.317

0.212

−55

0.215

0.411

0.281

−50

0.291

0.527

0.368

−45

0.386

0.666

0.474

−40

0.505

0.833

0.604

−35

0.653

1.031

0.761

−30

0.833

1.264

0.948

−25

1.050

1.536

1.170

−20

1.310

1.850

1.430

−15

1.618

2.212

1.734

−10

1.980

2.625

2.084

−5

2.402

3.094

2.487

0

2.890

3.624

2.947

5

3.451

4.218

3.468

10

4.092

4.883

4.057

15

4.820

5.622

4.718

20

5.642

6.440

5.456

25

6.567

7.344

6.278

30

7.601

8.337

7.189

35

8.754

9.424

8.195

40

10.033

10.612

9.302

45

11.448

11.905

10.516

50

13.007

13.308

11.843

55

14.720

14.828

13.290

60

16.598

16.469

14.865

65

18.651

18.238

16.575

70

20.891

20.140

18.428

75

23.332

22.182

20.432

80

25.988

24.370

22.598

85

28.876

26.711

24.937

90

32.018

29.211

27.461

95

35.443

31.877

30.189

100

39.204

34.717

33.143

TABLE 7

CF3I/DME (87/13): P/T Table

P

T

R134a

PL mix

PV mix

° C.

atm

atm

atm

−100

0.006

0.010

0.010

−95

0.009

0.015

0.015

−90

0.015

0.024

0.023

−85

0.024

0.035

0.035

−80

0.036

0.051

0.051

−75

0.054

0.074

0.073

−70

0.079

0.103

0.102

−65

0.112

0.142

0.140

−60

0.157

0.192

0.189

−55

0.215

0.255

0.251

−50

0.291

0.335

0.330

−45

0.386

0.434

0.426

−40

0.505

0.554

0.545

−35

0.653

0.701

0.688

−30

0.833

0.876

0.859

−25

1.050

1.083

1.062

−20

1.310

1.328

1.302

−15

1.618

1.613

1.581

−10

1.980

1.943

1.905

−5

2.402

2.323

2.277

0

2.890

2.757

2.702

5

3.451

3.251

3.186

10

4.092

3.808

3.733

15

4.820

4.435

4.347

20

5.642

5.135

5.035

25

6.567

5.915

5.801

30

7.601

6.780

6.651

35

8.754

7.735

7.591

40

10.033

8.786

8.625

45

11.448

9.938

9.760

50

13.007

11.198

11.002

55

14.720

12.571

12.357

60

16.598

14.063

13.831

65

18.651

15.681

15.431

70

20.891

17.432

17.164

75

23.332

19.323

19.037

80

25.988

21.360

21.059

85

28.876

23.552

23.238

90

32.018

25.908

25.584

95

35.443

28.436

28.108

100

39.204

31.149

30.823

TABLE 8

CF3I/R161 (97.5/2.5): P/T Table

P

T

R1234ze

PL mix

PV mix

° C.

atm

atm

atm

−100

0.004

0.012

0.009

−95

0.006

0.018

0.014

−90

0.010

0.027

0.021

−85

0.016

0.040

0.031

−80

0.025

0.058

0.045

−75

0.038

0.082

0.065

−70

0.055

0.114

0.090

−65

0.079

0.155

0.124

−60

0.111

0.207

0.168

−55

0.153

0.273

0.224

−50

0.207

0.355

0.293

−45

0.276

0.455

0.379

−40

0.363

0.577

0.485

−35

0.471

0.724

0.613

−30

0.603

0.898

0.766

−25

0.763

1.104

0.949

−20

0.955

1.346

1.163

−15

1.184

1.626

1.414

−10

1.454

1.948

1.705

−5

1.770

2.318

2.041

0

2.137

2.739

2.424

5

2.559

3.215

2.861

10

3.043

3.751

3.355

15

3.594

4.352

3.911

20

4.218

5.022

4.534

25

4.921

5.765

5.229

30

5.709

6.586

6.001

35

6.588

7.491

6.854

40

7.566

8.484

7.795

45

8.649

9.570

8.829

50

9.844

10.754

9.961

55

11.159

12.042

11.196

60

12.601

13.438

12.542

65

14.179

14.948

14.004

70

15.901

16.577

15.589

75

17.776

18.332

17.303

80

19.814

20.217

19.155

85

22.027

22.241

21.152

90

24.428

24.408

23.304

95

27.032

26.727

25.622

100

29.860

29.205

28.118

TABLE 9

CF3I/Propylene (97.5/2.5): P/T Table

P

T

R1234ze

PL mix

PV mix

° C.

atm

atm

atm

−100

0.004

0.013

0.009

−95

0.006

0.020

0.014

−90

0.010

0.030

0.021

−85

0.016

0.043

0.031

−80

0.025

0.061

0.046

−75

0.038

0.086

0.065

−70

0.055

0.118

0.091

−65

0.079

0.160

0.125

−60

0.111

0.213

0.169

−55

0.153

0.279

0.225

−50

0.207

0.361

0.295

−45

0.276

0.462

0.382

−40

0.363

0.584

0.488

−35

0.471

0.730

0.617

−30

0.603

0.903

0.771

−25

0.763

1.107

0.954

−20

0.955

1.346

1.169

−15

1.184

1.623

1.421

−10

1.454

1.941

1.713

−5

1.770

2.305

2.049

0

2.137

2.720

2.433

5

2.559

3.189

2.870

10

3.043

3.716

3.364

15

3.594

4.306

3.920

20

4.218

4.964

4.543

25

4.921

5.694

5.237

30

5.709

6.501

6.007

35

6.588

7.389

6.859

40

7.566

8.364

7.798

45

8.649

9.431

8.828

50

9.844

10.594

9.956

55

11.159

11.858

11.186

60

12.601

13.230

12.525

65

14.179

14.714

13.980

70

15.901

16.316

15.555

75

17.776

18.042

17.257

80

19.814

19.897

19.095

85

22.027

21.889

21.075

90

24.428

24.024

23.206

95

27.032

26.309

25.499

100

29.860

28.754

27.964

TABLE 10

CF3I/DME (95/5): P/T Table

P

T

R1234ze

PL mix

PV mix

° C.

atm

atm

atm

−100

0.004

0.009

0.009

−95

0.006

0.015

0.014

−90

0.010

0.022

0.021

−85

0.016

0.033

0.032

−80

0.025

0.049

0.046

−75

0.038

0.070

0.066

−70

0.055

0.097

0.093

−65

0.079

0.134

0.127

−60

0.111

0.181

0.172

−55

0.153

0.240

0.229

−50

0.207

0.315

0.300

−45

0.276

0.407

0.388

−40

0.363

0.519

0.496

−35

0.471

0.655

0.626

−30

0.603

0.818

0.783

−25

0.763

1.012

0.969

−20

0.955

1.239

1.187

−15

1.184

1.504

1.443

−10

1.454

1.811

1.739

−5

1.770

2.165

2.081

0

2.137

2.568

2.471

5

2.559

3.026

2.915

10

3.043

3.544

3.417

15

3.594

4.125

3.982

20

4.218

4.776

4.615

25

4.921

5.500

5.320

30

5.709

6.302

6.103

35

6.588

7.188

6.969

40

7.566

8.163

7.922

45

8.649

9.232

8.969

50

9.844

10.400

10.115

55

11.159

11.672

11.365

60

12.601

13.056

12.726

65

14.179

14.555

14.204

70

15.901

16.176

15.804

75

17.776

17.926

17.535

80

19.814

19.811

19.402

85

22.027

21.837

21.414

90

24.428

24.013

23.580

95

27.032

26.347

25.908

100

29.860

28.847

28.411

TABLE 11

CF3I/Pentafluoroiodoethane (95/5): P/T Table

P

T

R1234ze

PL mix

PV mix

° C.

atm

atm

atm

−100

0.004

0.008

0.007

−95

0.006

0.012

0.011

−90

0.010

0.019

0.017

−85

0.016

0.028

0.025

−80

0.025

0.040

0.037

−75

0.038

0.058

0.053

−70

0.055

0.081

0.074

−65

0.079

0.111

0.103

−60

0.111

0.151

0.140

−55

0.153

0.201

0.188

−50

0.207

0.263

0.248

−45

0.276

0.341

0.322

−40

0.363

0.436

0.414

−35

0.471

0.552

0.525

−30

0.603

0.691

0.659

−25

0.763

0.856

0.818

−20

0.955

1.050

1.007

−15

1.184

1.277

1.228

−10

1.454

1.541

1.484

−5

1.770

1.845

1.781

0

2.137

2.193

2.121

5

2.559

2.590

2.508

10

3.043

3.038

2.948

15

3.594

3.543

3.443

20

4.218

4.109

3.999

25

4.921

4.740

4.619

30

5.709

5.441

5.309

35

6.588

6.216

6.073

40

7.566

7.070

6.916

45

8.649

8.008

7.842

50

9.844

9.034

8.857

55

11.159

10.154

9.966

60

12.601

11.373

11.174

65

14.179

12.696

12.486

70

15.901

14.128

13.909

75

17.776

15.675

15.447

80

19.814

17.343

17.106

85

22.027

19.137

18.895

90

24.428

21.066

20.819

95

27.032

23.134

22.886

100

29.860

25.352

25.105

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