US2511993A - Azeotropic mixture for use as a refrigerant - Google Patents

Azeotropic mixture for use as a refrigerant Download PDF

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Publication number
US2511993A
US2511993A US694145A US69414546A US2511993A US 2511993 A US2511993 A US 2511993A US 694145 A US694145 A US 694145A US 69414546 A US69414546 A US 69414546A US 2511993 A US2511993 A US 2511993A
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United States
Prior art keywords
refrigerant
propane
boiling point
azeotropic mixture
monochlorodifluoromethane
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Expired - Lifetime
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US694145A
Inventor
Reed Winston Harrison
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Carrier Corp
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Carrier Corp
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Priority to US694145A priority Critical patent/US2511993A/en
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/04Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
    • C09K5/041Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
    • C09K5/044Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2205/00Aspects relating to compounds used in compression type refrigeration systems
    • C09K2205/10Components
    • C09K2205/12Hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2205/00Aspects relating to compounds used in compression type refrigeration systems
    • C09K2205/32The mixture being azeotropic

Definitions

  • the chief object of my invention is to provide a refrigerant mixture composed of two or more refrigerants capable of forming an azeotropic mixture, which boils at a constant temperature as if it were composed of a single substance.

Description

Patented June 20, 1950 L AZEOTROPIC MIXTURE FOR USE AS A REFRIGERANT Winston Harrison Reed, Syracuse, N. Y., assignor to Carrier Corporation, Syracuse, N. Y., a corporation of Delaware No Drawing. Application August 30, 1946, Serial No. 694,145
3 Claims. 1
This invention relates to refrigerant mixtures and to a method of using the same.
The chief object of my invention is to provide a refrigerant mixture composed of two or more refrigerants capable of forming an azeotropic mixture, which boils at a constant temperature as if it were composed of a single substance.
I have found a mixture of monochlorodifiuoromethane and propane to be particularly advantageous. Monoohlorodifluoromethane possesses a boiling point of -41.4 F. at atmospheric pressure while propane possesses a boiling point of --48.1 F. at atmospheric pressure (14.69 pounds per square inch). Monochlorodifluoromethane at a temperature of 32 F. provides a pressure of about 73 pounds per square inch absolute. Propane at a temperature of 32 F. possesses a pressure of about '75 pounds per square inch absolute. According to Raoults law, any mixture of such materials should possess a pressure between 20 the two extremes. Contrary to this law, however, the addition of propane to monochlorodifluoromethane increases the pressure over a wide range to provide a highly desirable increase in capacity of a refrigeration system designed for While I have described a preferred embodiconsisting in introducing into a refrigeration use with monochlorodifluoromethane. Such increase in capacity amounts to about 18% depending upon the quantity of propane mixed with monochlorodifluoromethane.
The azeotropic mixture is formed having a constant boiling point of 32 F. at an absolute pressure of approximately 86.2 pounds per square inch when monochlorodifluoromethane and propane are mixed in the proportions of approximately 68 parts to 32 parts by weight. The azeotropic mixture so formed possesses a lower boiling point than either monochlorodlfluoromethane or propane. The azeotropic mixture is stable, non-corrosive in the system and is lower in cost than monochlorodifiuoromethane.
The azeotropic mixture of my invention may be employed in equipment designed for use at a condensing temperature of about 105 F. and at an evaporating temperature of about 40 F. In operation the azeotropic mixture may be condensed at a condensing temperature of about 105 F., then transferred to the evaporator or heat exchanger and evaporated at a. temperature of about 40 F. to provide the required heat transfer.
It will be appreciated that the respective amounts of propane and monochlorodifluoromethane in the azeotrope vary in accordance with temperature and pressure; that is, the amount of propane contained in the azeotrope varies slightly as the temperature, for example, increases.
system of a refrigerant consisting of monochlorodifluoromethane having a boiling point of -41.4 F. at atmospheric pressure and propane having a boiling point of about -48.1 F. at atmospheric pressure, the refrigerant having a boiling point of 32 F. at about 86.2 p.s.i.a., evaporating the refrigerant, the concentration of the refrigerant remainin the same as it is vaporized with each of the components remaining in the same ratio with respect to the other, and then successively compressing and condens ing the refrigerant, the components in the refrigerant remaining in the same ratio during the compression and condensation stages.
2. A refrigerant for use in a compressorcondenser-expander refrigeration system consisting of a mixture of monochlorodifluoromethane and propane having a pressure at a predetermined temperature greater than the pressure of either component at such temperature, said mixture at its boiling temperature containing the same proportions of the components in both liquid and vapor phases.
3. A refrigerant for use in a compressor-condenser-expander refrigeration system consisting of an azeotropic mixture of monochlorodifluoromethane and propane and containing approximately 32% by weight of propane, said mixture having a boiling point of 32 F. at an absolute pressure of about 86.2 pounds per square inch, said mixture at its boiling temperature containing the same proportions of the components in both liquid and vapor phases.
' WINSTON HARRISON REED.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS

Claims (1)

1. A METHOD OF PRODUCING REFRIGERATION EFFECT CONSISTING IN INTRODUCING INTO A REFRIGERATION SYSTEM OF REFRIGERANT CONSISTING OF MONOCHLORODIFLUOROMETHANE HAVING A BOILING POINT OF -41.4*F. AT ATMOSPHERIC PRESSURE AND PROPANE HAVING A BOILING POINT OF ABOUT -48.1*F AT ATMOSPHERIC PRESSURE, THE REFRIGERANT HAVING A BOILING POINT OF 32*F. AT ABOUT 86.2 P.S.I.A., EVAPORATING THE REFRIGERANT, THE CONCENTRATION OF THE REFRIGERANT REMAINING THE SAME AS IT IS VAPORIZED WITH EACH OF THE COMPONENTS REMAINING IN THE SAME RATIO WITH RESPECT TO THE OTHER, AND THEN SUCCESSIVELY COMPRESSING AND CONDENSING THE REFRIGERANT, THE COMPONENTS IN THE REFRIGERANT REMAINING IN THE SAME RATIO DURING THE COMPRESSION AND CONDENSATION STAGES.
US694145A 1946-08-30 1946-08-30 Azeotropic mixture for use as a refrigerant Expired - Lifetime US2511993A (en)

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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2641579A (en) * 1951-03-02 1953-06-09 Du Pont Azeotropic refrigerant composition of monochlorodifluoromethane and chloropentafluoroethane
US2984987A (en) * 1960-02-26 1961-05-23 Schlumbohm Peter Method of operating a combustiondriven compression-refrigerating system
US3431211A (en) * 1965-03-05 1969-03-04 Du Pont Azeotropic compositions
JPS5044541A (en) * 1973-08-24 1975-04-22
EP0011971A1 (en) * 1978-11-22 1980-06-11 Daikin Kogyo Co., Ltd. Refrigerant mixture
EP0065858A1 (en) * 1981-05-19 1982-12-01 Exxon Research And Engineering Company Working fluid for heat pumps
EP0419042A1 (en) * 1989-09-12 1991-03-27 Star Refrigeration Ltd. Three component refrigerant
US5080823A (en) * 1990-04-02 1992-01-14 Societe Atochem Azeotropic mixture with 1,1,1-trifluoroethane and propane a low boiling point and its applicatons as a refrigerant fluid, as an aerosol propellant, or as a blowing agent for plastic foams
US5234613A (en) * 1991-09-30 1993-08-10 E.I. Du Pont De Nemours And Company Substantially constant boiling compositions of difluoromethane and propane
US5360566A (en) * 1992-11-06 1994-11-01 Intermagnetics General Corporation Hydrocarbon refrigerant for closed cycle refrigerant systems
US5616276A (en) * 1990-07-26 1997-04-01 E. I. Du Pont De Nemours And Company Azeotrope-like refrigerants with chlorodifluoromethane, pentafluoroethane, and C2 -C4 hydrocarbon

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1968050A (en) * 1931-11-19 1934-07-31 Gen Motors Corp Heat transfer and refrigeration
US1986959A (en) * 1931-02-06 1935-01-08 Chicago Pneumatic Tool Co Refrigerant composition
US2120559A (en) * 1937-04-20 1938-06-14 Philadelphia And Reading Coal Absorption refrigeration
US2191196A (en) * 1932-04-30 1940-02-20 Gen Motors Corp Refrigerants and methods of transferring heat
US2229711A (en) * 1938-06-29 1941-01-28 Ansul Chemical Co Method of preventing formation of ice crystals in refrigerants
US2255584A (en) * 1937-12-11 1941-09-09 Borg Warner Method of and apparatus for heat transfer
US2408802A (en) * 1940-01-15 1946-10-08 Glen W Miller Absorption refrigeration cycle

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1986959A (en) * 1931-02-06 1935-01-08 Chicago Pneumatic Tool Co Refrigerant composition
US1968050A (en) * 1931-11-19 1934-07-31 Gen Motors Corp Heat transfer and refrigeration
US2191196A (en) * 1932-04-30 1940-02-20 Gen Motors Corp Refrigerants and methods of transferring heat
US2120559A (en) * 1937-04-20 1938-06-14 Philadelphia And Reading Coal Absorption refrigeration
US2255584A (en) * 1937-12-11 1941-09-09 Borg Warner Method of and apparatus for heat transfer
US2229711A (en) * 1938-06-29 1941-01-28 Ansul Chemical Co Method of preventing formation of ice crystals in refrigerants
US2408802A (en) * 1940-01-15 1946-10-08 Glen W Miller Absorption refrigeration cycle

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2641579A (en) * 1951-03-02 1953-06-09 Du Pont Azeotropic refrigerant composition of monochlorodifluoromethane and chloropentafluoroethane
US2984987A (en) * 1960-02-26 1961-05-23 Schlumbohm Peter Method of operating a combustiondriven compression-refrigerating system
US3431211A (en) * 1965-03-05 1969-03-04 Du Pont Azeotropic compositions
JPS5044541A (en) * 1973-08-24 1975-04-22
JPS5437327B2 (en) * 1973-08-24 1979-11-14
EP0011971A1 (en) * 1978-11-22 1980-06-11 Daikin Kogyo Co., Ltd. Refrigerant mixture
EP0065858A1 (en) * 1981-05-19 1982-12-01 Exxon Research And Engineering Company Working fluid for heat pumps
GB2244492A (en) * 1989-09-12 1991-12-04 Star Refrigeration Three-component refrigerant mixture
EP0419042A1 (en) * 1989-09-12 1991-03-27 Star Refrigeration Ltd. Three component refrigerant
WO1992016596A1 (en) * 1989-09-12 1992-10-01 Star Refrigeration Limited Three-component refrigerant
GB2244492B (en) * 1989-09-12 1993-08-04 Star Refrigeration Three-component refrigerant mixture
EP0621328A1 (en) * 1989-09-12 1994-10-26 Star Refrigeration Ltd. Three-component refrigerant
US5080823A (en) * 1990-04-02 1992-01-14 Societe Atochem Azeotropic mixture with 1,1,1-trifluoroethane and propane a low boiling point and its applicatons as a refrigerant fluid, as an aerosol propellant, or as a blowing agent for plastic foams
US5616276A (en) * 1990-07-26 1997-04-01 E. I. Du Pont De Nemours And Company Azeotrope-like refrigerants with chlorodifluoromethane, pentafluoroethane, and C2 -C4 hydrocarbon
US5234613A (en) * 1991-09-30 1993-08-10 E.I. Du Pont De Nemours And Company Substantially constant boiling compositions of difluoromethane and propane
US5360566A (en) * 1992-11-06 1994-11-01 Intermagnetics General Corporation Hydrocarbon refrigerant for closed cycle refrigerant systems

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