US1968050A - Heat transfer and refrigeration - Google Patents

Heat transfer and refrigeration Download PDF

Info

Publication number
US1968050A
US1968050A US723278A US72327834A US1968050A US 1968050 A US1968050 A US 1968050A US 723278 A US723278 A US 723278A US 72327834 A US72327834 A US 72327834A US 1968050 A US1968050 A US 1968050A
Authority
US
United States
Prior art keywords
refrigeration
halogen
heat transfer
substitution
hydrogen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US723278A
Inventor
Jr Thomas Midgley
Albert L Henne
Robert R Mcnary
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Motors Liquidation Co
Original Assignee
General Motors Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US576052A external-priority patent/US1968049A/en
Application filed by General Motors Corp filed Critical General Motors Corp
Priority to US723278A priority Critical patent/US1968050A/en
Application granted granted Critical
Publication of US1968050A publication Critical patent/US1968050A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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

Definitions

  • application relates to the art of transferring heat from one point to another and specifically to the art of refrigeration and is a division of application Serial Number 576352.
  • refrigerants and heat transfer agents have been chosen chiefly :for their boiling points and stability in the refrigerating or heat transfer cycle irrespective of other desirable properties, such as noninflammability and non-toxicity.
  • the part of our process which deals with the controlling of the properties of the refrigerating or heat transfer agents consists in replacing hydrogen by fluorine or other halogen, or both, in aliphatic hydrocarbons in which at least one hydrogen has already been replaced by iiuorine.
  • the part of our process which relates to the transfer of heat or the production of refrigeration comprises changing the physical state of, for example, by condensing or evaporating, a halo-nuoro derivative of an aliphatic hydrocarbon, and dissipating to, or withdrawing from, an object to be heated or'cooled, the latent heat necessary for changing the physical state of the said derivative.
  • a halo-nuoro derivative of an aliphatic hydrocarbon we mean a derivative containing more than one fluorine atom with or Without other halogen atoms, or one fluorine atom With one or more other halogen atoms.
  • Fig. 2 is a plot applying the rules Vto groups having two carbon atoms.
  • Fig. 3 isa key to Fig. 2, showing the radicals corresponding to the numbers used in Fig. 2.
  • the dashed lines indicate fluorine substitutions and the solid lines indicate chlorine substitution. Similar plots are obtained with bromine and iodine in place of chlorine except that the plot is elongated in one direction of higher temperatures with br'omine, while with iodine the temperatures are still more elevated. The amount of elongation is readily determinedby applying the boiling points of some of these compounds.
  • this plot contains all the compounds which can be derived from CH3F by chlorine and/or fiuorine substitutions, together with data which assist in the formation of the plot.
  • the base line appear the numerals zero to four which show halogen content, and the vertical Amsterdam-gives the approximate boiling points in degrees centigrade.
  • the chlorine and uorine content At each point of intersection is givenrthe chlorine and uorine content and the complete formula' of the corresponding compound is found by making this halogen substitution for hydrogen in the formula CH4.
  • Fig. 2 we have shown the same mode of controlling the properties of a refrigerant carried to compounds of the same type as in Fig. 1 but having two carbon atoms.
  • the key to the chart is given in Fig. 3.
  • compound 0.1 is CHLCHnF
  • compound 2.9 is CHFn.CCl2F
  • compound 1.5 is CH:F.CHC1:
  • compound 2.2 is CI-IIEaCHFx.
  • the structural formula of 02H51 is CI-Ia-CI-IzF, which has a boiling point at about 32 C. 1f Awe make a fiuorine substitution for hydrogen in the second radical of this structural formula so that it reads CHa-CHFz, we have a refrigerating agent' whose boiling point is about 26 C. If we make the fluorine substitution for hydrogen onto the other carbon atom so that the formula reads CHzF-CHmthe boiling point of this refrigerant is about 5 C.
  • the first type of substitution yields a compound boiling substantially lower than the compound obtained by the second type of substitution and the chart shows this to be general.
  • the substitution of chlorine, .bromine or iodine for hydrogen raises the boiling point, but the substitution in a radical which does not already contain a halogen raises the boiling point more than when the substitution is made in a radical which already contains a halogen.
  • the plot may be expanded in like manner with other aliphatic mono-fiuorides. As the number of carbon. atoms increases the complexity and extent of the plot will increase together with the number of halogens present.
  • These halogen derivatives of aliphatic mono-fluorides may be represented by the formula in which C represents carbon and n the number of carbon atoms in the molecule which is always equal to one or more.
  • H represents hydrogen and m the number of atoms thereof, which may equal zero and still fulfill th'e requirements of our invention.
  • F represents iluorine and p the number of atoms thereof which is always equal to one or more.
  • X represents chlorine, bromine or iodine or combinations thereof and r the total number of such atoms. 1- may be zero when p is greater than one.
  • halogen derivatives of aliphatic mono-fiuorides halogen derivatives of alkyl mono-iiuorides, aliphatic iiuoro halides alkyl uoro halides, uoro derivatives of methyl fluoride, fluoro-halo derivatives of methane and fiuoro chloro derivatives of methane.
  • Our invention will probably find its greatest utility by adjusting both the mode of preparing the refrigerant to obtain desirable characteristics and the mode of using the refrigerant to obtain a process of refrigeration or heat 'transfer which meets the limitations imposed.
  • the method of transferring heat which comprises condensing and subsequently evaporating any of the following derivatives of methane; CHClFz; CClF3 and CClaF.
  • the method of producing refrigeration which comprises evaporating in the vicinity of a body to be cooled and subsequently condensing any of the following derivatives of methane; CHClFz; CClFs and CClaF.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

July 31, 1934- T. MIDGLEY, JR., ET Al. 1,968,050
HEAT TRANSFER AND REFRIGERATION Original Filed Nov. 19. 1951 CL 5\5 60 y /fLsF/eo Z CHE? lg 3 of :PMs/NG -60 l- 4-C//ZCL Ke] to 2 3 y J 5.: 0 0
inatenteci July El, i934 ann aerarcana'rron Midgley, Sir.,
Worthington, Albert @riginal application November 19, i951, Serial No. 576,052. Divided and this application April 30, 1934, Serial No. ZEZS 2 illaims.
application relates to the art of transferring heat from one point to another and specifically to the art of refrigeration and is a division of application Serial Number 576352.
Heretofore, as far as We are aware, refrigerants and heat transfer agents have been chosen chiefly :for their boiling points and stability in the refrigerating or heat transfer cycle irrespective of other desirable properties, such as noninflammability and non-toxicity.
It is the object of our invention, on the other hand, to provide a process of refrigeration and, generically, a process of heat transfer in which these desirable properties, such as non-inflammability and non-toxicity, are obtained in combination with the desired boiling points.
Broadly stated, the part of our process which deals with the controlling of the properties of the refrigerating or heat transfer agents consists in replacing hydrogen by fluorine or other halogen, or both, in aliphatic hydrocarbons in which at least one hydrogen has already been replaced by iiuorine.
Broadly stated, the part of our process which relates to the transfer of heat or the production of refrigeration comprises changing the physical state of, for example, by condensing or evaporating, a halo-nuoro derivative of an aliphatic hydrocarbon, and dissipating to, or withdrawing from, an object to be heated or'cooled, the latent heat necessary for changing the physical state of the said derivative. By a halo-nuoro derivative of an aliphatic hydrocarbon we mean a derivative containing more than one fluorine atom with or Without other halogen atoms, or one fluorine atom With one or more other halogen atoms.
Referring now specifically to our mode of controlling the properties of the refrigerating or 40 heat transfer agent, aliphatic monofluorides form the structural nucleus on which the agents are built. Broadly speaking, if in the structural formula CHsF we increase the fluorine content (number of atoms) by the substitution of fluorine for hydrogen, stability increases, in-
flammability decreases, and toxicity decreases. 1f we keep the fluorine content constant and substitute another -halogen for hydrogen in the nucleus, the boiling point increases, the stability 5u decreases, thetoxicity increases, and the innammability decreases. The degree to which these variations take place depends on what the other halogen (chlorine, bromine, or iodine) is.
As the ratio of the halogen content to' the hydrogen content increases the infiammabilit decreases.
Because there are several variables, and because of the value of relative proportions, we have placed the compounds of the group just discussed on piots wherein Fig. l is a plot applying the rules of substitution to typical groups having one carbon atom, and
Fig. 2 is a plot applying the rules Vto groups having two carbon atoms.
Fig. 3 isa key to Fig. 2, showing the radicals corresponding to the numbers used in Fig. 2.
Referring to the plots generally, the dashed lines indicate fluorine substitutions and the solid lines indicate chlorine substitution. Similar plots are obtained with bromine and iodine in place of chlorine except that the plot is elongated in one direction of higher temperatures with br'omine, while with iodine the temperatures are still more elevated. The amount of elongation is readily determinedby applying the boiling points of some of these compounds.
Referring speciiically to Fig. l, this plot contains all the compounds which can be derived from CH3F by chlorine and/or fiuorine substitutions, together with data which assist in the formation of the plot. 0n the base line appear the numerals zero to four which show halogen content, and the vertical Eine-gives the approximate boiling points in degrees centigrade. At each point of intersection is givenrthe chlorine and uorine content and the complete formula' of the corresponding compound is found by making this halogen substitution for hydrogen in the formula CH4. We have drawn a horizontal dashed line at about 25 centigrade to indicate approximately the optimum vapor pressure conditions whichv We dsire for operating an air cooled refrigerator. It is obvious that one may deviate more or less from this line to obtain optimum conditions which include some other factors, so that Within the neighborhood of this line we can provide a suitable refrigerant to meet a wide variation in limitations imposed. If under other refrigerating conditions another optimum line is found desirable, the same choice may be made in the neighborhood of that line. In fact, the actual operation of the refrigerator and the providing of the characteristics of the refrigerant are here combined as one problem so as to obtain the most desirable process of refrigeration under a given set of conditions.
In Fig. 2 we have shown the same mode of controlling the properties of a refrigerant carried to compounds of the same type as in Fig. 1 but having two carbon atoms. The key to the chart is given in Fig. 3. For example, compound 0.1 is CHLCHnF, compound 2.9 is CHFn.CCl2F, compound 1.5 is CH:F.CHC1:, and compound 2.2 is CI-IIEaCHFx.
When we choose as our nucleus a compound having two or more carbon atoms we find that the structuralformula gives a choice as to where the substitutions of the halogens shall be made. For example, the structural formula of 02H51 is CI-Ia-CI-IzF, which has a boiling point at about 32 C. 1f Awe make a fiuorine substitution for hydrogen in the second radical of this structural formula so that it reads CHa-CHFz, we have a refrigerating agent' whose boiling point is about 26 C. If we make the fluorine substitution for hydrogen onto the other carbon atom so that the formula reads CHzF-CHmthe boiling point of this refrigerant is about 5 C. Thus the first type of substitution yields a compound boiling substantially lower than the compound obtained by the second type of substitution and the chart shows this to be general. The substitution of chlorine, .bromine or iodine for hydrogen raises the boiling point, but the substitution in a radical which does not already contain a halogen raises the boiling point more than when the substitution is made in a radical which already contains a halogen. l
The plot may be expanded in like manner with other aliphatic mono-fiuorides. As the number of carbon. atoms increases the complexity and extent of the plot will increase together with the number of halogens present. These halogen derivatives of aliphatic mono-fluorides may be represented by the formula in which C represents carbon and n the number of carbon atoms in the molecule which is always equal to one or more.
H represents hydrogen and m the number of atoms thereof, which may equal zero and still fulfill th'e requirements of our invention.
F represents iluorine and p the number of atoms thereof which is always equal to one or more.
X represents chlorine, bromine or iodine or combinations thereof and r the total number of such atoms. 1- may be zero when p is greater than one.
Among the chemical groups that these refrigerants fall in are halogen derivatives of aliphatic mono-fiuorides, halogen derivatives of alkyl mono-iiuorides, aliphatic iiuoro halides alkyl uoro halides, uoro derivatives of methyl fluoride, fluoro-halo derivatives of methane and fiuoro chloro derivatives of methane.
Thus by our mode of making fluorine and/or i other halogen substitution in a monofluoride, we can meet any conditions of refrigeration and provide our refrigerant with the desired properties, such as non-toxicity and non-inflammability, .along with such properties as stability and proper boiling points.
Referring more specifically to the part lof our process which relates to the actual transfer of heat, we accomplish this transfer of heat by changing the physical state of, for example, condensing or evaporating our aliphatic lwdrocarbon derivative which contains 4more than one fluorine atom with or without other halogen atoms, or one fluorine atom with one or more other halogen atoms, and by dissipating to or withdrawing fromvan object to be heated or cooled, the latent heat necessary for the change in physical state. More specifically, to produce refrigeration, we may evaporate the desired derivative in the vicinity of a body to be cooled, while if a heating effect is desired, We may condense the derivative in the vicinity of a body to be heated, it being understood, of course, that the terms evaporation" and condensation include the separation of a gas from, and the absorption of a gas in, an absorbent respectively.
Our invention will probably find its greatest utility by adjusting both the mode of preparing the refrigerant to obtain desirable characteristics and the mode of using the refrigerant to obtain a process of refrigeration or heat 'transfer which meets the limitations imposed.
We pr'efer to employ refrigerants boiling above 60 C.
Obviously our invention is not limited in its application to any specific form of apparatus for carrying out the mode of operation described and it will not be necessary for a com-- plete understanding of the invention to sh'ow a specific embodiment of apparatus. Nor is the present invention limited to the example set forth, for a particular advance of the present invention resides in the fact that a great number of new refrigerants with graduated properties is rendered available, and that one is accordingly enabled to secure the most suitable refrigerant for varied purposes.
What is claimed is as follows:
1. The method of transferring heat which comprises condensing and subsequently evaporating any of the following derivatives of methane; CHClFz; CClF3 and CClaF.
2. The method of producing refrigeration which comprises evaporating in the vicinity of a body to be cooled and subsequently condensing any of the following derivatives of methane; CHClFz; CClFs and CClaF.
THOMAS MIDGLEY, Jn. ALBERT L. HENNE. ROBERT R. MCNARY.
US723278A 1931-11-19 1934-04-30 Heat transfer and refrigeration Expired - Lifetime US1968050A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US723278A US1968050A (en) 1931-11-19 1934-04-30 Heat transfer and refrigeration

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US576052A US1968049A (en) 1930-02-08 1931-11-19 Heat transfer and refrigeration
US723278A US1968050A (en) 1931-11-19 1934-04-30 Heat transfer and refrigeration

Publications (1)

Publication Number Publication Date
US1968050A true US1968050A (en) 1934-07-31

Family

ID=27076862

Family Applications (1)

Application Number Title Priority Date Filing Date
US723278A Expired - Lifetime US1968050A (en) 1931-11-19 1934-04-30 Heat transfer and refrigeration

Country Status (1)

Country Link
US (1) US1968050A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2511993A (en) * 1946-08-30 1950-06-20 Carrier Corp Azeotropic mixture for use as a refrigerant
US3173872A (en) * 1962-03-12 1965-03-16 Allied Chem Compositions of fluorocarbons
US3249546A (en) * 1963-10-30 1966-05-03 Du Pont Azeotrope refrigerant compositions
US3336763A (en) * 1965-06-30 1967-08-22 Carrier Corp Refrigeration systems
US3470101A (en) * 1963-10-03 1969-09-30 Allied Chem Fluorinated hydrocarbon compositions
US3640869A (en) * 1964-09-18 1972-02-08 Allied Chem Fluorocarbon compositions
US3901817A (en) * 1974-04-22 1975-08-26 Allied Chem Halocarbon compositions
US4172043A (en) * 1976-10-22 1979-10-23 Allied Chemical Corporation Composition for absorption heating with furan-derivative absorbent
FR2682683A1 (en) * 1991-10-22 1993-04-23 Froilabo Nonazeotropic refrigerating mixture
US5248433A (en) * 1992-04-30 1993-09-28 E. I. Du Pont De Nemours And Company Binary azeotropic mixtures of octafluoropropane and fluoroethane

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2511993A (en) * 1946-08-30 1950-06-20 Carrier Corp Azeotropic mixture for use as a refrigerant
US3173872A (en) * 1962-03-12 1965-03-16 Allied Chem Compositions of fluorocarbons
US3470101A (en) * 1963-10-03 1969-09-30 Allied Chem Fluorinated hydrocarbon compositions
US3249546A (en) * 1963-10-30 1966-05-03 Du Pont Azeotrope refrigerant compositions
US3640869A (en) * 1964-09-18 1972-02-08 Allied Chem Fluorocarbon compositions
US3336763A (en) * 1965-06-30 1967-08-22 Carrier Corp Refrigeration systems
US3901817A (en) * 1974-04-22 1975-08-26 Allied Chem Halocarbon compositions
US4172043A (en) * 1976-10-22 1979-10-23 Allied Chemical Corporation Composition for absorption heating with furan-derivative absorbent
FR2682683A1 (en) * 1991-10-22 1993-04-23 Froilabo Nonazeotropic refrigerating mixture
US5248433A (en) * 1992-04-30 1993-09-28 E. I. Du Pont De Nemours And Company Binary azeotropic mixtures of octafluoropropane and fluoroethane

Similar Documents

Publication Publication Date Title
USRE19265E (en) Heat transfer
US7713434B2 (en) Refrigerant compositions
US1968050A (en) Heat transfer and refrigeration
US20070295930A1 (en) Refrigerant compositions
US6655160B2 (en) Refrigerant compositions
CA2264303A1 (en) Refrigerant compositions
EP0840768B1 (en) Mixtures of pentafluoropropane and a hydrofluorocarbon having 4 to 6 carbon atoms
US3394878A (en) Azeotropic compositions
US2101993A (en) Refrigerant mixture and the method of using the same
US3597183A (en) Trifluoromethane-ethane azeotropic composition
US4057974A (en) Constant boiling mixtures of 1-chloro-2,2,2-trifluoroethane and octafluorocyclobutane
JPH04110386A (en) Fluid for heat transfer
US1968049A (en) Heat transfer and refrigeration
US2479259A (en) Process for producing increased refrigeration
US3409555A (en) Refrigerant composition
JPH04110385A (en) Fluid for heat transfer
US2104882A (en) Heat transfer and refrigeration
EP0558763A1 (en) Refrigerant and refrigerator
JPH03170588A (en) Working fluid
US1833847A (en) Heat transfer
US4101436A (en) Constant boiling mixtures of 1-chloro-2,2,2-trifluoroethane and hydrocarbons
WO1984001165A1 (en) Fluids for use in sorption refrigerators and heat pumps
JPH04110384A (en) Fluid for heat transfer
EP0858490B1 (en) Refrigerant compositions
US8444873B2 (en) Refrigerant composition