| WO/2018/053145 | INTEGRATED PROPANE DEHYDROGENATION PROCESS |
| JP2023102069 | REACTION SYSTEM |
| JP2583013 | [Title of Invention] New Refrigerant Composition |
| WO1992001762A1 | 1992-02-06 |
| EP0451016A1 | 1991-10-09 | |||
| EP0552075A1 | 1993-07-21 | |||
| EP0537045A1 | 1993-04-14 | |||
| US4024086A | 1977-05-17 | |||
| US4097398A | 1978-06-27 | |||
| US4164471A | 1979-08-14 |
| 1. | A refrigerant composition comprising 1,1,2trifluoroethane and bis (trifluoromethyl) fluoroamine, tris(trifluoromethyl)amine, bis (difluoromethyl) trifluoromethylamine, fluoromethylbis (trifluoromethyl) amine, difluoromethyl sulfur pentafluoride, pentafluoroethyl sulfur pentafluoride, 1,1,2,2,3,3 hexafluoropropane, 1, 1, 1,2,2,3hexafluoropropane, 1, 1,2,3,3,3hexafluoropropane, 1,1,2,2tetrafluoropropane, 1,1,1,2tetrafluoropropane, 1,1,1trifluoropropane, 2,2 difluoropropane, 2fluoropropane, lfluoropropane, 1,1,1,3,3,4,4,4octafluorobutane, 1,1,1,2,3,4,4,5,5,5decafluoropentane, butane, cyclopropane, isobutane, or propane. |
| 2. | A composition comprising effective amounts of 1,1,2 trifluoroethane and a second component to form an azeotropic or azeotropelike composition, wherein said second component is bis (trifluoromethyl) fluoroamine, tris(trifluoromethyl)amine, bis (difluoromethyl) trifluoromethylamine, fluoromethylbis (trifluoromethyl) amine, difluoromethyl sulfur pentafluoride, pentafluoroethyl sulfur pentafluoride, 1,1,2,2,3,3hexafluoropropane, 1,1, 1,2,2,3 hexafluoropropane, 1, 1,2,3,3,3hexafluoropropane, 1, 1,2,2tetrafluoropropane, 1,1,1,2tetrafluoropropane, 1,1,1trifluoropropane, 2,2difluoropropane, 2 fluoropropane, lfluoropropane, 1,1,1,3,3,4,4,4octafluorobutane, 1,1,1,2,3,4,4,5,5,5 decafluoropentane, butane, cyclopropane, isobutane, or propane. |
| 3. | The azeotropic or azeotropelike composition of claim 2, said composition comprising: 142 wt% 1,1,2trifluoroethane and 5899 wt%bis (trifluoromethyl) fluoroamine; 1150 wt% 1,1,2trifluoroethane and 3950 wt% tris(trifluoromethyl)amine; 3499 wt% 1,1,2trifluoroethane and 166 wt% bis (difluoromethyl) trifluoromethylamine; 3499 wt% 1,1,2trifluoroethane and 166 wt% fluoromethylbis (trifluoromethyl) amine; 199 wt% 1,1,2trifluoroethane and 1 99 wt% difluoromethyl sulfur pentafluoride; 1966 wt% 1,1,2trifluoroethane and 3481 wt% pentafluoroethyl sulfur pentafluoride; 199 wt% 1,1,2trifluoroethane and 199 wt% 1,1,2,2,3,3hexafluoropropane; 199 wt% 1,1,2trifluoroethane and 1 99 wt% 1,1, 1,2,2,3hexafluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 1, 1,2,3,3,3hexafluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 1,1,2,2 tetrafluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 1,1,1,2 tetrafluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 1,1,1 trifluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 2,2difluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 2fluoropropane; 199 wt% 1,1,2 trifluoroethane and 199 wt% lfluoropropane; 199 wt% 1,1,2trifluoroethane and 199 wt% 1,1,1,3,3,4,4,4octafluorobutane; 3899 wt% 1,1,2trifluoroethane and 162 wt% 1,1,1,2,3,4,4,5,5,5decafluoropentane; 2878 wt% 1,1,2trifluoroethane and 22 72 wt% butane; 156 wt% 1,1,2trifluoroethane and 4499 wt% cyclopropane; 1869 wt% 1,1,2trifluoroethane and 3182 wt% isobutane; 154 wt% 1,1,2trifluoroethane and 4699 wt% propane. |
| 4. | A process for producing refrigeration, comprising condensing a composition of any of Claims 1 through 3, and thereafter evaporating said composition in the vicinity of the body to be cooled. |
| 5. | A process for producing heat comprising condensing a composition of any of Claims 1 through 3 in the vicinity of a body to be heated, and thereafter evaporating said composition in the vicinity of a body to be heated. |
REFRIGERANT COMPOSITIONS INCLUDING
1,1,2-TRIFLUOROETHANE
FIELD OF THE INVENTION
This invention relates to refrigerant compositions that include 1,1,2- trifluoroethane as a component, said compositions being useful as cleaning agents, expansion agents for polyolefins and polyurethanes, aerosol propellants, refrigerants, heat transfer media, gaseous dielectrics, fire extinguishing agents, power cycle working fluids, polymerization media, particulate removal fluids, carrier fluids, buffing abrasive agents, and displacement drying agents.
BACKGROUND OF THE INVENTION Fluorinated hydrocarbons have many uses, one of which is as a refrigerant. Such refrigerants include dichlorodifluoromethane (CFC-12) and chlorodifluoromethane (HCFC-22).
In recent years it has been pointed out that certain kinds of fluorinated hydrocarbon refrigerants released into the atmosphere may adversely affect the stratospheric ozone layer. Although this proposition has not yet been completely established, there is a movement toward the control of the use and the production of certain chlorofluorocarbons (CFCs) and hydrochlorofluorocarbons (HCFCs) under an international agreement.
Accordingly, there is a demand for the development of refrigerants that have a lower ozone depletion potential than existing refrigerants while still achieving an acceptable performance in refrigeration applications.
Hydrofluorocarbons (HFCs) have been suggested as replacements for CFCs and HCFCs since HFCs have no chlorine and therefore have zero ozone depletion potential.
In refrigeration applications, a refrigerant is often lost during operation through leaks in shaft seals, hose connections, soldered joints and broken lines. In addition, the refrigerant may be released to the atmosphere during maintenance procedures on refrigeration equipment. If the refrigerant is not a pure component or an azeotropic or azeotrope-like composition, the refrigerant composition may change when leaked or discharged to the atmosphere from the refrigeration equipment, which may cause the refrigerant to become flammable or
to have poor refrigeration performance.
Accordingly, it is desirable to use as a refrigerant a single fluorinated hydrocarbon or an azeotropic or azeotrope-like composition that includes one or more fluorinated hydrocarbons.
Fluorinated hydrocarbons may also be used a cleaning agent or solvent to clean, for example, electronic circuit boards. It is desirable that the cleaning agents be azeotropic or azeotrope-like because in vapor degreasing operations the cleaning agent is generally redistilled and reused for final rinse cleaning.
Azeotropic or azeotrope-like compositions that include a fluorinated hydrocarbon are also useful as blowing agents in the manufacture of closed-cell polyurethane, phenolic and thermoplastic foams, as propellants in aerosols, as heat transfer media, gaseous dielectrics, fire extinguishing agents, power cycle working fluids, such as for heat pumps, inert media for polymerization reactions, fluids for removing particulates from metal surfaces, as carrier fluids that may be used, for example, to place a fine film of lubricant on metal parts, or as buffing abrasive agents to remove buffing abrasive compounds from polished surfaces such as metal, as displacement drying agents for removing water, such as from jewelry or metal parts, as resist developers in conventional circuit manufacturing techniques including chlorine-type developing agents, and as strippers for photoresists when used with, for example, a chlorohydrocarbon such as 1,1,1-trichloroethane or trichloroethylene.
SUMMARY OF THE INVENTION The present invention relates to the discovery of compositions of 1,1,2-trifluoroethane and bis (trifluoromethyl) fluoroamine, tris(trifluoromethyl)amine, bis (difluoromethyl) trifluoromethylamine, fluoromethylbis (trifluoromethyl) amine, difluoromethyl sulfur pentafluoride, pentafluoroethyl sulfur pentafluoride, 1,1,2,2,3,3-hexafluoropropane, 1,1,1,2,2,3- hexafluoropropane, 1, 1,2,3,3,3-hexafluoropropane, 1, 1,2,2-tetrafluoropropane, 1,1,1,2-tetrafluoropropane, 1,1,1-trifluoropropane, 2,2-difluoropropane, 2- fluoropropane, 1-fluoropropane, 1,1,1,3,3,4,4,4-octafluorobutane, 1,1,1,2,3,4,4,5,5,5- decafluoropentane, butane, cyclopropane, isobutane, or propane, said compositions being useful as cleaning agents, expansion agents for polyolefins and polyurethanes, aerosol propellants, refrigerants, heat transfer media, gaseous dielectrics, fire extinguishing agents, power cycle working fluids, polymerization media, particulate
removal fluids, carrier fluids, buffing abrasive agents, and displacement drying agents. Further, the invention relates to the discovery of binary azeotropic or azeotrope-like compositions comprising effective amounts of 1,1,2-trifluoroethane and bis (trifluoromethyl) fluoroamine, tris(trifluoromethyl)amine, bis (difluoromethyl) trifluoromethylamine, fluoromethylbis (trifluoromethyl) amine, difluoromethyl sulfur pentafluoride, pentafluoroethyl sulfur pentafluoride, 1, 1,2,2,3,3-hexafluoropropane, 1,1, 1,2,2,3-hexafluoropropane, 1, 1,2,3,3,3- hexafluoropropane, 1,1,2,2-tetrafluoropropane, 1,1,1,2-tetrafluoropropane, 1,1,1- trifluoropropane, 2,2-difluoropropane, 2-fluoropropane, l-fluoropropane, 1, 1,1,3,3,4,4,4-octafluorobutane, 1, 1, 1,2,3,4,4,5,5,5-decafluoropentane, butane, cyclopropane, isobutane, or propane to form an azeotropic or azeotrope-like composition.
DETAILED DESCRIPTION The present invention relates to compositions of 1,1,2-trifluoroethane (HFC-143, or CHF2CH2F, boiling point =4°C), and at least one of the following components:
I. Bis (trifluoromethyl) fluoroamine ((CFβ^NF, boiling point = -40 to -35°C) 2. tris(trifluoromethyl)amine ((CF3)3N, boiling point = -6.5°C),
3. Bis (difluoromethyl) trifluoromethylamine (N(CHF2)2(CF3), boiling point = 26.5°C),
4. Fluoromethylbis (trifluoromethyl) amine (N(CH2F)(CF3)2, boiling point
= 26°C), 5. difluoromethyl sulfur pentafluoride (SF5CF2H, boiling point = 5.1°C),
6. pentafluoroethyl sulfur pentafluoride (SF5C2F5, boiling point = 13.5°C),
7. 1,1,2,2,3,3-hexafluoropropane (HFC-236ca, or CHF2CF2CHF2)
8. 1,1,1,2,2,3-hexafluoropropane (HFC-236cb, or CF3CF2CH2F)
9. 1,1,2,3,3 -hexafluoropropane (HFC-236ea, or CF3CH2CF3) 10. 1,1,2,2-tetrafluoropropane (HFC-254cb, or CHF2CF2CH3)
II. 1,1,1,2-tetrafluoropropane (HFC-254eb, or CF3CFHCH3)
12. 1,1,1-trifluoroproρane (HFC-263fb, or CF3CH2CH3)
13. 2,2-difluoroρroρane (HFC-272ca, or CH3CF2CH3)
14. 2-fluoropropane (HFC-281ea, or CH3CHFCH3) 15. l-fluoropropane (HFC-281fa, or CH2FCH2CH3)
16. 1,1,1,3,3,4,4,4-octafluorobutane (HFC-338mf, or CF3CH2CF2CF3)
17. 1,1,1,2,3,4,4,5,5,5-decafluoropentane (HFC-4310mee, or CF3CFHCFHCF2CF3),
18. butane (C4H10)
19. cyclopropane 20. isobutane (CH(CH 3 ) 3 )
21. propane (C^Hg)
(CF3)3N (CAS Reg. No. 432-03-1) has been made by electrochemical fluorination of trimethyl amine in anhydrous hydrogen fluoride as disclosed by Kauck and Simons in U. S. Patent 2,616,927.
N(CHF 2 )2(CF 3 ) (CAS Reg. No. 73551-02-7) has been prepared by fluorination of trimethyl amine over cobalt trifluoride as reported by Rendell and Wright in Tetrahedron. Vol.35, pp. 2405-2411 (1979).
N(CH2F)(CF 3 ) 2 (CAS Reg. No. 67212-88-8) has been prepared by fluorination of 4-methylmorpholine as reported by Rendell and Wright in Tetrahedron. Vol. 34, pp. 197-203 (1978).
SF5CF2H (CAS Reg. No. 420-67-7) has been prepared by reaction of methyl mercaptan with fluorine gas as disclosed by Silvey and Cady in U.S. Patent No. 2,697,726 and J. Am. Chem. Soc, Vol. 72, pages 3624-26 (1950). SF5C2F5 (CAS Reg. No.354-67-6) has been prepared by electrochemical fluorination of ethyl sulfide in anhydrous hydrogen fluoride as reported by Dresdner in J. Am. Chem. Soc, Vol. 79, pages 69-70 (1957).
The following compositions can be used as refrigerants: 1-99 weight percent HFC-143 and 1-99 weight percent of (CF3)2NF, (CF3)3N, N(CHF 2 )2(CF 3 ), N(CH 2 F)(CF 3 ) 2 , SF 5 CF 2 H, SF 5 C 2 F 55 HFC-236ca, HFC-236cb, HFC-236ea, HFC-254cb, HFC-254eb, HFC-263fb, HFC-272ca, HFC-281ea, HFC- 281fa, HFC-338mf, HFC-4310mee, butane, cyclopropane, isobutane, or propane. The present invention also relates to the discovery of azeotropic or azeotrope-like compositions of effective amounts of HFC-143 and a second component to form an azeotropic or azeotrope-like composition, wherein the second component is (CF 3 ) 2 NF, (CF 3 ) 3 N, N(CHF 2 )2(CF 3 ), N(CH 2 F)(CF 3 ) 2 , SF 5 CF 2 H, SF5C2F5, HFC-236ca, HFC-236cb, HFC-236ea, HFC-254cb, HFC- 254eb, HFC-263fb, HFC-272ca, HFC-281ea, HFC-281fa, HFC-338mf, HFC- 4310mee, butane, cyclopropane, isobutane or propane. By "azeotropic" composition is meant a constant boiling liquid
16. 1,1,1,3,3,4,4,4-octafluorobutane (HFC-338mf, or CF3CH2CF2CF3)
17. 1, 1, 1,2,3,4,4,5,5,5-decafluoropentane (HFC-43 lOmee, or CF3CFHCFHCF2CF3),
18. butane (C4H10)
19. cyclopropane 20. isobutane (CH(CH3) 3 )
21. propane (C3H8)
(CF3)3N (CAS Reg. No. 432-03-1) has been made by electrochemical fluorination of trimethyl amine in anhydrous hydrogen fluoride as disclosed by Kauck and Simons in U. S. Patent 2,616,927.
N(CHF 2 )2(CF 3 ) (CAS Reg. No. 73551-02-7) has been prepared by fluorination of trimethyl amine over cobalt trifluoride as reported by Rendell and Wright in Tetrahedron. Vol.35, pp. 2405-2411 (1979).
N(CH 2 F)(CF 3 )2 (CAS Reg. No. 67212-88-8) has been prepared by fluorination of 4-methylmorpholine as reported by Rendell and Wright in Tetrahedron. Vol. 34, pp. 197-203 (1978).
SF5CF2H (CAS Reg. No.420-67-7) has been prepared by reaction of methyl mercaptan with fluorine gas as disclosed by Silvey and Cady in U.S. Patent No.2,697,726 and J. Am. Chem. Soc, Vol. 72, pages 3624-26 (1950). SF5C2F5 (CAS Reg. No. 354-67-6) has been prepared by electrochemical fluorination of ethyl sulfide in anhydrous hydrogen fluoride as reported by Dresdner in J. Am. Chem. Soc, Vol. 79, pages 69-70 (1957).
The following compositions can be used as refrigerants: 1-99 weight percent HFC-143 and 1-99 weight percent of (CF3)2NF, (CF3)3N, N(CHF 2 )2(CF 3 ), N(CH 2 F)(CF 3 )2 } SF 5 CF 2 H, SF 5 C 2 F 5> HFC-236ca, HFC-236cb, HFC-236ea, HFC-254cb, HFC-254eb, HFC-263fb, HFC-272ca, HFC-281ea, HFC- 28 If a, HFC-338mf, HFC-43 lOmee, butane, cyclopropane, isobutane, or propane. The present invention also relates to the discovery of azeotropic or azeotrope-like compositions of effective amounts of HFC-143 and a second component to form an azeotropic or azeotrope-like composition, wherein the second component is (CF3)2NF, (CF3)3N, N(CHF2)2(CF3), N(CH2F)(CF3)2, SF 5 CF 2 H, SF5C2F5, HFC-236ca, HFC-236cb, HFC-236ea, HFC-254cb, HFC- 254eb, HFC-263fb, HFC-272ca, HFC-281ea, HFC-281fa, HFC-338mf, HFC- 43 lOmee, butane, cyclopropane, isobutane or propane. By "azeotropic" composition is meant a constant boiling liquid
admixture of two or more substances that behaves as a single substance. One way to characterize an azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has the same composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes without compositional change. Constant boiling compositions are characterized as azeotropic because they exhibit either a maximum or minimum boiling point, as compared with that of the non-azeotropic mixtures of the same components. By "azeotrope-like" composition is meant a constant boiling, or substantially constant boiling, liquid admixture of two or more substances that behaves as a single substance. One way to characterize an azeotrope-like composition is that the vapor produced by partial evaporation or distillation of the liquid has substantially the same composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes without substantial composition change.
It is recognized in the art that a composition is azeotrope-like if, after 50 weight percent of the composition is removed such as by evaporation or boiling off, the difference in vapor pressure between the original composition and the composition remaining after 50 weight percent of the original composition has been removed is less than 10 percent, when measured in absolute units. By absolute units, it is meant measurements of pressure and, for example, psia, atmospheres, bars, torr, dynes per square centimeter, millimeters of mercury, inches of water and other equivalent terms well known in the art. If an azeotrope is present, there is no difference in vapor pressure between the original composition and the composition remaining after 50 weight percent of the original composition has been removed. Therefore, included in this invention are compositions of effective amounts of HFC-143 and a second component, wherein the second component is (CF 3 ) 2 NF, (CF 3 ) 3 N, N(CHF 2 ) 2 (CF 3 ), N(CH 2 F)(CF 3 ) 2 , SF 5 CF 2 H, SF 5 C 2 F 5 , HFC-236ca, HFC-236cb, HFC-236ea, HFC-254cb, HFC-254eb, HFC-263fb, HFC- 272ca, HFC-281ea, HFC-281fa, HFC-338mf, HFC-4310mee, butane, cyclopropane, isobutane or propane such that after 50 weight percent of an original composition is evaporated or boiled off to produce a remaining composition, the difference in the vapor pressure between the original composition and the remaining composition is 10 percent or less.
Substantially constant boiling, azeotropic or azeotrope-like compositions of this invention comprise the following (all compositions are measured at 25°C):
COMPONENTS WEIGHT RANGES PREFERRED
(wt. /wt.%) (wt.%/wt.%)
HFC-143/(CF 3 ) 2 NF 1-42/58-99
HFC-143/(CF 3 ) 3 N 11-50/39-50
HFC-143/N(CHF 2 )2(CF 3 ) 34-99/1-66 34-80/20-66
HFC-143/N(CH 2 F)(CF 3 )2 34-99/1-66 34-80/20-66
HFC-143/SF 5 CF 2 H 1-99/1-99 1-60/40-99
HFC-143/SF 5 C 2 F 5 19-66/34-81
HFC-143/HFC-236ca 1-99/1-99 1-70/30-99
HFC-143/HFC-236cb 1-99/1-99 1-70/30-99
HFC-143/HFC-236ea 1-99/1-99 1-70/30-99
HFC-143/HFC-254cb 1-99/1-99 1-70/30-99
HFC-143/HFC-254eb 1-99/1-99 1-70/30-99
HFC-143/HFC-263fb 1-99/1-99 1-70/30-99
HFC-143/HFC-272ca 1-99/1-99 20-80/20-80
HFC-143/HFC-281ea 1-99/1-99 1-70/30-99
HFC-143/HFC-281fa 1-99/1-99 10-70/30-90
HFC-143/HFC-338mf 1-99/1-99 1-80/20-99
HFC-143/4310mee 38-99/1-62 38-90/10-62
HFC-143/butane 28-78/22-72 40-70/30-60
HFC-143/cyclopropane 1-56/44-99 10-50/50-90
HFC-143/isobutane 18-69/31-82 20-60/40-80
HFC-143/propane 1-54/46-99 10-50/50-90
For purposes of this invention, "effective amount" is defined as the amount of each component of the inventive compositions which, when combined, results in the formation of an azeotropic or azeotrope-like composition. This definition includes the amounts of each component, which amounts may vary depending on the pressure applied to the composition so long as the azeotropic or azeotrope-like compositions continue to exist at the different pressures, but with possible different boiling points.
Therefore, effective amount includes the amounts, such as may be expressed in weight percentages, of each component of the compositions of the instant invention which form azeotropic or azeotrope-like compositions at
temperatures or pressures other than as described herein.
For the purposes of this discussion, azeotropic or constant-boiling is intended to mean also essentially azeotropic or essentially-constant boiling. In other words, included within the meaning of these terms are not only the true azeotropes described above, but also other compositions containing the same components in different proportions, which are true azeotropes at other temperatures and pressures, as well as those equivalent compositions which are part of the same azeotropic system and are azeotrope-like in their properties. As is well recognized in this art, there is a range of compositions which contain the same components as the azeotrope, which will not only exhibit essentially equivalent properties for refrigeration and other applications, but which will also exhibit essentially equivalent properties to the true azeotropic composition in terms of constant boiling characteristics or tendency not to segregate or fractionate on boiling.
It is possible to characterize, in effect, a constant boiling admixture which may appear under many guises, depending upon the conditions chosen, by any of several criteria:
* The composition can be defined as an azeotrope of A, B, C (and D...) since the very term "azeotrope" is at once both definitive and limitative, and requires that effective amounts of A, B, C (and D...) for this unique composition of matter which is a constant boiling composition.
* It is well known by those skilled in the art, that, at different pressures, the composition of a given azeotrope will vary at least to some degree, and changes in pressure will also change, at least to some degree, the boiling point temperature. Thus, an azeotrope of A, B, C (and D...) represents a unique type of relationship but with a variable composition which depends on temperature and/or pressure. Therefore, compositional ranges, rather than fixed compositions, are often used to define azeotropes.
* The composition can be defined as a particular weight percent relationship or mole percent relationship of A, B, C (and D...), while recognizing that such specific values point out only one particular relationship and that in actuality, a series of such relationships, represented by A, B, C (and D...) actually exist for a given azeotrope, varied by the influence of pressure. * An azeotrope of A, B, G (and D...) can be characterized by defining
the compositions as an azeotrope characterized by a boiling point at a given pressure, thus giving identifying characteristics without unduly limiting the scope of the invention by a specific numerical composition, which is limited by and is only as accurate as the analytical equipment available. The azeotrope or azeotrope-like compositions of the present invention can be prepared by any convenient method including mixing or combining the desired amounts. A preferred method is to weigh the desired component amounts and thereafter combine them in an appropriate container.
Specific examples illustrating the invention are given below. Unless otherwise stated therein, all percentages are by weight. It is to be understood that these examples are merely illustrative and in no way are to be interpreted as limiting the scope of the invention.
EXAMPLE 1 Phase Study
A phase study shows the following compositions are azeotropes, all at
25°C.
Composition Vapor Press.
No. psia (kPa)
1. 10.6 wt.% HFC-143 89.4 wt.% (CF 3 ) 2 NF 148.9
2. 24.1 wt.% HFC-143 75.9 wt.% (CF 3 ) 3 N 70.2
3. 66.3 wt.% HFC-143 33.7 wt.% N(CHF 2 )2(CF 3 ) 37.2 4. 66.6 wt.% HFC-143 33.4 wt.% N(CH 2 F)(CF 3 ) 2 36.8
5. 40.2 wt.% HFC-143 59.8 wt.% SF 5 CF 2 H 40.3
6. 42.1 wt.% HFC-143 57.9 wt.% SF5C2F5 44.5
7. 2.0 wt.% HFC-143 98.0 wt.% HFC-236ca 25.0
8. 29.6 wt.% HFC-143 70.4 wt.% HFC-236cb 27.7 9. 17.7 wt.% HFC-143 82.3 wt.% HFC-236ea 28.4
10. 51.6 wt.% HFC-143 48.4 wt.% HFC-254cb 32.1
11. 44.6 wt.% HFC-143 55.4 wt.% HFC-254eb 31.4
12. 9.7 wt.% HFC-143 90.3 wt.% HFC-263fb 56.2
13. 36.0 wt.% HFC-143 64.0 wt.% HFC-272ca 41.2 14. 18.4 wt.% HFC-143 81.6 wt.% HFC-28 lea 47.5
Impact of Vapor Leakage on Vapor Pressure at 25°C
A vessel is charged with an initial composition at 25°C, and the vapor pressure of the composition is measured. The composition is allowed to leak from the vessel, while the temperature is held constant at 25°C, until 50 weight percent of the initial composition is removed, at which time the vapor pressure of the composition remaining in the vessel is measured. The results are summarized below.
HFC-143/N(CHF 2 ) 2 (CF 3 )
34.0/66.0 35.8
35.0/65.0 35.9
40.0/60.0 36.3 50.0/50.0 36.9
66.3/33.7 37.2
80.0/20.0 36.9
90.0/10.0 36.1
99.0/1.0 33.6
HFC-143/N(CH 2 F)(CF 3 ) 2
10.0/90.0 24.9 20.0/80.0 25.1 30.0/70.0 25.9 40.0/60.0 27.0 50.0/50.0 28.1 60.0/40.0 29.2 70.0/30.0 30.3 80.0/20.0 31.3 90.0/10.0 32.2 99.0/1.0 33.0
HFC-143/HFC-236cb
1.0/99.0 33.3
10.0/90.0 30.3
20.0/80.0 28.2
29.6/70.4 27.7
40.0/60.0 28.0
50.0/50.0 28.8
60.0/40.0 29.7
70.0/30.0 30.6
80.0/20.0 31.5
90.0/10.0 32.3
99.0/1.0 33.0
HFC-143/HFC-236ea
1.0/99.0 28.7
10.0/90.0 28.5
17.7/82.3 28.4
30.0/70.0 28.7
50.0/50.0 29.8
70.0/30.0 31.2
90.0/10.0 32.5
99.0/1.0 33.0
HFC-143/HFC-254cb
1.0/99.0 34.1
10.0/90.0 33.6
30.0/70.0 32.5
51.6/48.4 32.1
70.0/30.0 32.3
90.0/10.0 32.8
99.0/1.0 33.1
37.8 0.0
10.0/90.0 38.3
30.0/70.0 39.2
44.6/55.4 39.4
70.0/30.0 38.6
90.0/10.0 36.0 99.0/1.0 33.5
HFC-143/HFC-338mf
1.0/99.0 19.3
1.7/98.3 19.3 20.0/80.0 20.5
40.0/60.0 24.7
50.0/50.0 26.6
60.0/40.0 28.3
80.0/20.0 31.0 99.0/1.0 33.0
HFC-143/HFC-43 lOmee
30.0/70.0 33.4
35.0/65.0 33.9 37.0/63.0 34.0
38.0/62.0 34.1
40.0/60.0 34.2
50.0/50.0 34.6
60.0/40.0 34.8 79.4/20.6 34.9
90.0/10.0 34.8
99.0/1.0 33.5
HFC-143/butane 25.0/75.0 50.6
27.0/73.0 50.9
28.0/72.0 51.0
30.0/70.0 51.2
40.0/60.0 51.9 53.2/46.8 52.2
70.0/30.0 51.5
78.0/22.0 50.2
79.0/21.0 49.9
80.0/20.0 49.7
HFC-143/cyclopropane 1.0/99.0 106.3
10.0/90.0 111.2
21.5/78.5 112.1
The results of this Example show that these compositions are azeotropic or azeotrope-like because when 50 wt.% of an original composition is removed, the vapor pressure of the remaining composition is within about 10% of the vapor pressure of the original composition, at a temperature of 25°C.
EXAMPLE 3
Refrigerant Performance The following table shows the performance of various refrigerants. The data are based on the following conditions. Evaporator temperature 40.0°F (4.4°C)
Condenser temperature 100.0°F (37.8°C) Compressor efficiency is 75%.
Evap. Cond. Capacity Refrig. Press. Press. Comp. Dis. BTU/min
Comp. Psia (kPa) Psia (kPa^ Temp. °F (°C) COP fkw)
CFC-11 7.1(49) 23.5(162) 130.0(54.4) 5.68 44.2(0.8) HFC-143/(CF 3 ) 2 NF
1.0/99.0 71.5 186.5 102.0
10.6/89.4 61.0 166.6 108.2
42.0/58.0 32.2 104.9 138.1 HFC-143/(CF 3 ) 3 N
5.0/95.0* 24.2 72.7 101.1
11.0/89.0* 25.2 74.7 103.7
24.1/75.9 25.2 74.1 100.2
50.0/50.0 20.9 64.0 118.3 95.0/5.0 15.3 47.3 134.8
*10°F Superheat
HFC-143/N(CHF 2 )2(CF 3 ) 5.0/95.0 6.7 24.6 102.9
34.0/66.0 10.1 34.6 117.0
66.3/33.7 12.8 41.3 125.9
99.0/1.0 14.4 44.9 135.0
HFC-143/N(CH 2 F)(CF 3 ) 2
5.0/95.0 7.0 25.1 100.5
34.0/66.0 10.6 35.8 114.8
66.6/33.4 13.3 42.4 124.0
99.0/1.0 14.4 44.9 134.9
HFC-143/HFC-236cb 1.0/99.0* 16.6 50.5 104.8 5.17 83.5
29.6/70.4 18.3 54.7 109.5 5.38 95.3
99.0/1.0 14.5 45.2 135.0 5.60 84.1
* 5°F Superheat
HFC-143/HFC-236ea 1.0/99.0 13.8 43.7 103.8
17.7/82.3 15.1 47.1 109.5
99.0/1.0 14.4 45.1 135.0
HFC-143/HFC-254cb 1.0/99.0 16.8 50.5 106.7
51.6/48.4 16.5 50.3 120.7
99.0/1.0 14.4 45.1 135.1
HFC-143/HFC-254eb 1.0/99.0 17.1 51.3 106.6
44.6/55.4 16.9 51.1 118.5
99.0/1.0 14.4 45.1 135.1
HFC-143/HFC-263fb 1.0/99.0 27.6
9.7/90.3 26.5
99.0/1.0 14.5
HFC-143/HFC-272ca 1.0/99.0 17.3
36.0/64.0 16.8
99.0/1.0 14.4 HFC-143/HFC-281ea 1.0/99.0 24.0
18.4/81.6 22.5
99.0/1.0 14.5
HFC-143/HFC-281fa 1.0/99.0 18.7
44.6/55.4 17.2
99.0/1.0 14.5
HFC-143/HFC-338mf 1.0/99.0* 9.1
1.7/88.3* 9.2
99.0/1.0 14.5 *10°F Superheat
HFC-143/cyclopropane
1.0/99.0 56.9 144.1 142.9
21.5/78.5 46.9 125.1 148.5
56.0/44.0 32.3 92.6 152.2
95.0/5.0 16.8 51.3 139.7
HFC-143/isobutane 5.0/95.0 26.2
18.0/82.0 25.4
41.8/58.2 23.0 69.0/31.0 19.7
95.0/5.0 15.4
HFC-143/propane 1.0/99.0 76.8 16.3/83.7 65.4
54.0/46.0 39.9
95.0/5.0 18.3
The novel compositions of this invention, including the azeotropic or azeotrope-like compositions, may be used to produce refrigeration by condensing the compositions and thereafter evaporating the condensate in the vicinity of a body to be cooled. The novel compositions may also be used to produce heat by condensing the refrigerant in the vicinity of the body to be heated and thereafter evaporating the refrigerant. In addition to refrigeration applications, the novel constant boiling or substantially constant boiling compositions of the invention are also useful as aerosol propellants, heat transfer media, gaseous dielectrics, fire extinguishing agents, expansion agents for polyolefins and polyurethanes and power cycle working fluids.
ADDITIONAL COMPOUNDS Other components, such as aliphatic hydrocarbons having a boiling point of -60 to +30°C, hydrofluorocarbonalkanes having a boiling point of -60 to +30°C, hydrofluoropropanes having a boiling point of between -60 to + 30°C, hydrocarbon esters having a boiling point between -60 to +30°C, hydrochlorofluorocarbons having a boiling point between -60 to +30°C, hydrofluorocarbons having a boiling point of -60 to +30°C, hydrochlorocarbons having a boiling point between -60 to +30°C, chlorocarbons and perfluorinated compounds, can be added to the azeotropic or azeotrope-like compositions described above without substantially changing the properties thereof, including the constant boiling behavior, of the compositions.
Additives such as lubricants, corrosion inhibitors, stabilizers, dyes and other appropriate materials may be added to the novel compositions of the invention for a variety of purposes provides they do not have an adverse influence on the composition for its intended application. Preferred lubricants include esters having a molecular weight greater than 250.