US3095698A - Heat transfer medium - Google Patents

Heat transfer medium Download PDF

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US3095698A
US3095698A US684719A US68471957A US3095698A US 3095698 A US3095698 A US 3095698A US 684719 A US684719 A US 684719A US 68471957 A US68471957 A US 68471957A US 3095698 A US3095698 A US 3095698A
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rubidium
heat transfer
vapor
mixture
transfer medium
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US684719A
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David R Stern
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American Potash and Chemical Corp
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American Potash and Chemical Corp
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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

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  • FIGURE 1 is a phase diagram illustrating the compositions of this invention which are defined by the region ABCDLGFEHA.
  • FIGURE 2 is a graphic showing of the values along a plane through points H, I, J and K in FIGURE 1.
  • FIGURE 3 is a schematic apparatus and flow sheet for use with the composition.
  • thermodynamic data comparing a typical mixed metal composition of this invention with the (thermodynamic properties of sodium, potassium, mercury and rubidium.
  • FIGURE :1 attention is called to another aspect of my invention which is that I discovered, name- 3,095,698 Patented July 2, 1963 ice freezes at 21 C. and boils at 883, C., a 904 C.
  • a mixed metal composition within this invention is liquid over a range 46 C. below the usual ambient temperature; since this is a physical mixture, the composition is a liquid over a 904 C. range, from -21 C. to 883 C., the boiling point of pure sodium.
  • the mixed metal heat transfer composition can be typically utilized in a heat transfer cycle such as that set forth diagrammatically in the accompanying drawing, FIGURE 3.
  • a mixture of the metals is withdrawn through pipe 5 from a storage tank 6 and is transferred by a pump 7 to a fractionator 20 and a boiler, generally indicated at 8.
  • the boiler is supplied by a suitable energy source, generally indicated at 9, e.g., a thermal or atomic source.
  • the rubidium is vaporized from the mixture into the overhead fractionator 20. Under atmospheric pressure, the temperature of the rubidium vapor will be 696 C.
  • the enriched rubidium vapor may be superheated, as in the superheater 12.
  • the heated vapor is then transferred to a suitable device for extracting heat from the rubidium vapor whereby work is accomplished, such as the turbine, generally indicated at 14.
  • the cooled rubidium vapor issuing from the turbine is transferred from line 16 to an air condenser 17, and the condensed liquid rubidium is returned through barometric leg 18 to the mixed metals storage vessel 6.
  • Rubidium lean mixed metal is withdrawn through line 19 and is also returned to the mixed metal tank 6; thus, the rubidium vapor can be utilized effectively as a heat source and yet one need not deal with pure rubidium as such.
  • a method of heat transfer comprising heating a ternary mixture of sodium, potassium and rubidium to provide a stream of hot rubidium vapor and a liquid residue lean in rubidium, extracting energy from the rubidium vapor whereby the vapor is cooled, condensing the cooled rubidium vapor, and returning the condensed rubidium to said liquid residue to provide said mixture for reuse, said mixture having a percentage composition falling along the line connecting points I, I and K of the drawing.

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  • 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

July 2, 1963 D. R. STERN ,095,
HEAT TRANSFER MEDIUM Filed Sept. 18, 1957 2 Sheets-Sheet 2 a B L 7 '10 aromefr/c 83 Energy Mixed Me7a/s 6 I Q M/xed Mefa/ EL M? I 1 "1'! i a u 1 E K -19 i E d l'i "2 I p a= 0. a E 18.0% Rb= 27.9% Rb 39.8%
Campos/#0115 1/7 Mo/ Per Cem INVENTOR. 2 David Aussefl Sfem AT ORNEYS W a I BY A MEMBER 0F 7'HE F/ United States Patent 3,095,698 HEAT TRANSFER MEDIUM David R. Stern, Fullerton, Califi, assignor to American Potash & Chemical Corporation, a corporation of Dela- Ware Filed Sept. 18, 1957, Ser. No. 684,719 2 Claims. (on. 60-36) This invention relates to heat transfer and particularly to a new and novel non-aqueous heat transfer composition having certain valuable properties.
There are many advantages in the use of a non-aqueous heat transfer composition and such materials as sodium, potassium, lithium, mercury, and various mixtures of these, have been proposed for utilization in power cycles. However, each of these suffers from a number of disadvantages which are absent from the composition of this invention. For example, they are either solids at ambient temperatures, have objectionable viscosities, or possess low thermal conductivity.
I have discovered that a composition of sodium, potassiurn and rubidium, in which the rubidium is the principal component, has many advantages over previously proposed heat transfer media. I have determined that the rubidium should comprise the major component, that sodium should be present in from about 16.1 percent to 49.8 percent, potassium from about 1.0 percent to 73.5 percent, with the balance rubidium.
In the drawings accompanying and forming a part hereof, FIGURE 1 is a phase diagram illustrating the compositions of this invention which are defined by the region ABCDLGFEHA.
FIGURE 2 is a graphic showing of the values along a plane through points H, I, J and K in FIGURE 1.
FIGURE 3 is a schematic apparatus and flow sheet for use with the composition.
In the following table, I have set forth pertinent thermodynamic data, comparing a typical mixed metal composition of this invention with the (thermodynamic properties of sodium, potassium, mercury and rubidium.
An examination of this data shows that the mixed metals of this invention have anextremely low melting point, 21 C., a high boiling point of 767 C., a high heat capacity, low viscosity and excellent thermoconductivity. Further, the materials have reasonable density.
Referring to FIGURE :1, attention is called to another aspect of my invention which is that I discovered, name- 3,095,698 Patented July 2, 1963 ice freezes at 21 C. and boils at 883, C., a 904 C.
range.
If one considers the usual ambient temperature to be 25 C., a mixed metal composition within this invention (point I), is liquid over a range 46 C. below the usual ambient temperature; since this is a physical mixture, the composition is a liquid over a 904 C. range, from -21 C. to 883 C., the boiling point of pure sodium.
The mixed metal heat transfer composition can be typically utilized in a heat transfer cycle such as that set forth diagrammatically in the accompanying drawing, FIGURE 3. In this, a mixture of the metals is withdrawn through pipe 5 from a storage tank 6 and is transferred by a pump 7 to a fractionator 20 and a boiler, generally indicated at 8. The boiler is supplied by a suitable energy source, generally indicated at 9, e.g., a thermal or atomic source. The rubidium is vaporized from the mixture into the overhead fractionator 20. Under atmospheric pressure, the temperature of the rubidium vapor will be 696 C.
The enriched rubidium vapor may be superheated, as in the superheater 12. The heated vapor is then transferred to a suitable device for extracting heat from the rubidium vapor whereby work is accomplished, such as the turbine, generally indicated at 14. The cooled rubidium vapor issuing from the turbine is transferred from line 16 to an air condenser 17, and the condensed liquid rubidium is returned through barometric leg 18 to the mixed metals storage vessel 6. Rubidium lean mixed metal is withdrawn through line 19 and is also returned to the mixed metal tank 6; thus, the rubidium vapor can be utilized effectively as a heat source and yet one need not deal with pure rubidium as such.
I claim:
1. A method of heat transfer comprising heating a ternary mixture of sodium, potassium and rubidium to provide a stream of hot rubidium vapor and a liquid residue lean in rubidium, extracting energy from the rubidium vapor whereby the vapor is cooled, condensing the cooled rubidium vapor, and returning the condensed rubidium to said liquid residue to provide said mixture for reuse, said mixture having a percentage composition falling along the line connecting points I, I and K of the drawing.
2. A ternary heat transfer mixture of sodium, potassium and rubidium and of a. composition falling along the line I, J and K of the drawing.
References Cited in the file of this patent UNITED STATES PATENTS 427,399 Campbell May 6, 1890 1,922,509 Thurm Aug. 15, 1933 1,982,745 Koenemann Dec. 4, 1934 2,575,322 Case Nov. 20, 1951 2,692,234 Insinger Oct. 19, 1954

Claims (1)

1. A METHOD OF HEAT TRANSFER COMPRISING HEATING A TERNARY MIXTURE OF SODIUM, POTASSIUM AND RUBIDIUM TO PROVIDE A STREAM OF HOT RUBIDIUM VAPOR AND A LIQUID RESIDUE LEAN IN RUBIDIUM, EXTRACTING ENREGY FROM THE RUBIDIUM VAPOR WHEREBY THE VAPOR IS COOLED, CONDENSING THE COOLED RUBIDIUM VAPOR, AND RETURNING THE CONDENSED RUBIDIUM TO SAID LIQUID RESIDUE TO PROVIDE SAID MIXTURE FOR REUSE, SAID MIXTURE HAVING A PERCENTAGE COMPOSITION
US684719A 1957-09-18 1957-09-18 Heat transfer medium Expired - Lifetime US3095698A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3195304A (en) * 1962-07-16 1965-07-20 American Potash & Chem Corp Process for producing power
US4041709A (en) * 1973-06-22 1977-08-16 Vereinigte Edelstahlwerke Aktiengesellschaft Thermal power plants and method of operating a thermal power plant
DE3202547A1 (en) * 1981-01-29 1982-11-04 Minnesota Mining and Manufacturing Co., 55133 Saint Paul, Minn. Heat-shrinkable article

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US427399A (en) * 1890-05-06 Joseph ii
US1922509A (en) * 1929-10-28 1933-08-15 Baker Perkins Co Inc Heating by circulating heat-transferring liquids
US1982745A (en) * 1928-01-31 1934-12-04 Drucktransformatoren Koenemann Method of transforming heat energy
US2575322A (en) * 1948-11-19 1951-11-20 American Cyanamid Co Salt bath rectifier
US2692234A (en) * 1949-11-05 1954-10-19 Koppers Co Inc Heat transfer media

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US427399A (en) * 1890-05-06 Joseph ii
US1982745A (en) * 1928-01-31 1934-12-04 Drucktransformatoren Koenemann Method of transforming heat energy
US1922509A (en) * 1929-10-28 1933-08-15 Baker Perkins Co Inc Heating by circulating heat-transferring liquids
US2575322A (en) * 1948-11-19 1951-11-20 American Cyanamid Co Salt bath rectifier
US2692234A (en) * 1949-11-05 1954-10-19 Koppers Co Inc Heat transfer media

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3195304A (en) * 1962-07-16 1965-07-20 American Potash & Chem Corp Process for producing power
US4041709A (en) * 1973-06-22 1977-08-16 Vereinigte Edelstahlwerke Aktiengesellschaft Thermal power plants and method of operating a thermal power plant
DE3202547A1 (en) * 1981-01-29 1982-11-04 Minnesota Mining and Manufacturing Co., 55133 Saint Paul, Minn. Heat-shrinkable article

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