US2131119A - Refrigeration - Google Patents
Refrigeration Download PDFInfo
- Publication number
- US2131119A US2131119A US124953A US12495337A US2131119A US 2131119 A US2131119 A US 2131119A US 124953 A US124953 A US 124953A US 12495337 A US12495337 A US 12495337A US 2131119 A US2131119 A US 2131119A
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- refrigerant
- metal
- gas
- copper
- nitrogen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B17/00—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type
- F25B17/08—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type the absorbent or adsorbent being a solid, e.g. salt
- F25B17/083—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type the absorbent or adsorbent being a solid, e.g. salt with two or more boiler-sorbers operating alternately
Definitions
- This invention relates to refrigeration, and is described as carried out in an apparatus operating on an absorption cycle.
- An object is to provide for absorption refrigeration in an apparatus which is compact and simple, so that (for example) it is suitable for use in house trailers and the like.
- the absorber consists of a body of metal, which is usually copper, preferably in a finely divided state, and the refrigerant consists of nitrogen peroxide (which is a mixture of N02 and N204, the proportions depending on temperature and pressure).
- the refrigerant consists of nitrogen peroxide (which is a mixture of N02 and N204, the proportions depending on temperature and pressure).
- N02 and N204 nitrogen peroxide
- the figure is a diagram of the apparatus used.
- the metal (usually copper) is caused in any desired manner to adhere to the inner surfaces of two absorbers l and I2, arranged to be heated alternately by two sources of heat such as burners l4 and I6.
- the metal is in finely divided form to increase the surface area, but it will be understood that metal plate or sheets could be used.
- These absorbers are connected, by conduits l8 and 20, with communicating connecting conduits 22 and 24 leading from the top of an evaporator 26 containing the refrigerant 28 spread out to provide a large evaporating surface. being the cooling medium, is arranged within and at the top of the space 30 to be cooled.
- the refrigerant 2B is preferably nitrogen peroxide, which is a mixture (varying according to the temperature and pressure) of N02 and N204.
- Check valves 32 and 34 permit the refrigerant vapor to pass from the evaporator 26 to the absorber ill or l2 (whichever one at the time is not being heated), but prevent any return of the vapors directly to the evaporator during the heating phase of the cycles of the absorbers.
- check valves 36 and 38 openv upwardly, to operate during the heating of the absorber ill or [2 to direct the gaseous nitrogen peroxide through a conduit 40 to a condenser 42, whence The evaporator 26,
- a sub-. merged float-operated valve 48 feeds excess liquid from the reservoir 46 to the evaporator 26, without allowing the passage of any vapor.
- one of the absorbers (the one indicated at l2 as shown in the diagram) is cool, and its metal-absorbent takes up nitrogen peroxide vapor through conduits 20 and 22, thereby reducingthe pressure in evaporator 26 and causing evaporation of some of the refrigerant 28, and causing the desired lowering of temperature in the. space 30, which must supply the heat ab-. sorbed by the evaporating refrigerant.
- the nitrogen peroxide combines with the metal in the absorber l2 to form an unstable compound usually referred to as a nitro-metal.
- the group N02 behaves as a monad radical, being called nitroxyl.
- the nitrometal is decomposed by heat from the burner l6, while at the sametime since burner I4 is extinguished the absorber Ill is taking up nitrogen peroxide.
- N02 copper nitroxyl breaks down above 90 C. into metallic copper and nitrogen peroxide vapor, thus: Cu(N02)-2 -Cu+2N02.
- N204 has a melting point of 9.3 C. and a boiling point of 213 0., above which it decomposes almost completely into N02 with the absorption of heat, thus: N2O4+5.571 kilogram ca1ories22N02.
- the cooling phase of the absorbers l0 and I2 can be substantially longer than the heating phase, so that the cooling phases of the two absorbers overlap.
- That method of cooling which comprises plating a body of refrigerant comprising an oxide of nitrogen having an extended evaporative surface, in communication with a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron, whereby the metal will absorb said refrigerant to form a compound of the metal and an oxide of nitrogen, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
- That method of cooling which comprises placing a body of refrigerant, consisting of nitrogen peroxide (mixture of N02 and N204), and having an extended evaporative surface, in communication with a body of metal selected from the group consisting of copper, cobalt,
- the metal will absorb said refrigerant to form a compound of the metal and the nitrogen peroxide, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
- That method of cooling which comprises placing a body of refrigerant comprising an oxide of nitrogen having an extended evaporative surface, in communication with a body of metal consisting mainly of copper, whereby the metal will absorb said refrigerant to form a compound of the metal and an oxide of nitrogen, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
- That method of cooling which comprises placing a body of refrigerant, consisting of nitrogen peroxide (mixture N02 and N204), and having an extended evaporative surface, in communication with a body of metal consisting mainly of copper, whereby the metal will-absorb said refrigerant to form a compound of the metal and the nitrogen peroxide, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
- a body of refrigerant consisting of nitrogen peroxide (mixture N02 and N204)
- a body of metal consisting mainly of copper
- Refrigerating apparatus comprising absorption means consisting of a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron, a body of refrigerant comprising an oxide of nitrogen having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
- absorption means consisting of a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron
- a body of refrigerant comprising an oxide of nitrogen having its surface in communication with the absorption means
- means for driving off refrigerant as a gas from said body of metal means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
- Refrigerating apparatus comprising absorption means consisting of a body of metal consisting mainly of copper, a body of refrigerant comprising an oxide of nitrogen having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
- Refrigerating apparatus comprising absorption means consisting of a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron, a body of refrigerant consisting of nitrogen peroxide (mixture NO: and N204) and having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
- absorption means consisting of a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron
- a body of refrigerant consisting of nitrogen peroxide (mixture NO: and N204) and having its surface in communication with the absorption means
- means for driving off refrigerant as a gas from said body of metal means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
- Refrigerating apparatus comprising absorp tion means consisting of a body of metal consisting mainly of copper, a body of refrigerant consisting of nitrogen peroxide (mixture of N02 and N204) and having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Sorption Type Refrigeration Machines (AREA)
Description
Sept. 27, 1938.
J. J. ROOT ET AL REFRIGERATION Filed Feb. 10, 1957 INVENTOR. Jzz mv J. Roar FRANK J. 30W]? ma Damon Patented ept. 27, IQB
REFRIGERATION nois Application February 10, 1937, Serial No. 124,953
8 Claims.
This invention relates to refrigeration, and is described as carried out in an apparatus operating on an absorption cycle. An object is to provide for absorption refrigeration in an apparatus which is compact and simple, so that (for example) it is suitable for use in house trailers and the like.
In the arrangement illustrated, the absorber consists of a body of metal, which is usually copper, preferably in a finely divided state, and the refrigerant consists of nitrogen peroxide (which is a mixture of N02 and N204, the proportions depending on temperature and pressure). In place of copper, cobalt and nickel and barium and silver and iron, and various mixtures of these metals, can be used.
The above and other objects and features of the invention, including various novel combinations and desirable particular arrangements, will be apparent from the following description of the process as carried out in the apparatus illustrated in the accompanying drawing, in which:
The figure is a diagram of the apparatus used.
In the illustrated apparatus, the metal (usually copper) is caused in any desired manner to adhere to the inner surfaces of two absorbers l and I2, arranged to be heated alternately by two sources of heat such as burners l4 and I6. Preferably the metal is in finely divided form to increase the surface area, but it will be understood that metal plate or sheets could be used. These absorbers are connected, by conduits l8 and 20, with communicating connecting conduits 22 and 24 leading from the top of an evaporator 26 containing the refrigerant 28 spread out to provide a large evaporating surface. being the cooling medium, is arranged within and at the top of the space 30 to be cooled.
While we prefer to use finely divided copper as the metal in the absorbers l0 and I2, it is possible to use cobalt, nickel, barium, silver, or iron, or a mixture of these metals. The refrigerant 2B is preferably nitrogen peroxide, which is a mixture (varying according to the temperature and pressure) of N02 and N204.
it is delivered as liquid to a reservoir 46. A sub-. merged float-operated valve 48 feeds excess liquid from the reservoir 46 to the evaporator 26, without allowing the passage of any vapor.
In operation, one of the absorbers (the one indicated at l2 as shown in the diagram) is cool, and its metal-absorbent takes up nitrogen peroxide vapor through conduits 20 and 22, thereby reducingthe pressure in evaporator 26 and causing evaporation of some of the refrigerant 28, and causing the desired lowering of temperature in the. space 30, which must supply the heat ab-. sorbed by the evaporating refrigerant. I
The nitrogen peroxide combines with the metal in the absorber l2 to form an unstable compound usually referred to as a nitro-metal. In forming this compound, the group N02 behaves as a monad radical, being called nitroxyl. In. the next phase of the cycle, the nitrometal is decomposed by heat from the burner l6, while at the sametime since burner I4 is extinguished the absorber Ill is taking up nitrogen peroxide.
For example copper nitroxyl breaks down above 90 C. into metallic copper and nitrogen peroxide vapor, thus: Cu(N02)-2 -Cu+2N02. The dark brown N02 changes partially into colorless N204, the exact proportion being dependent on the temperature and pressure. N204 has a melting point of 9.3 C. and a boiling point of 213 0., above which it decomposes almost completely into N02 with the absorption of heat, thus: N2O4+5.571 kilogram ca1ories22N02.
The cooling phase of the absorbers l0 and I2 can be substantially longer than the heating phase, so that the cooling phases of the two absorbers overlap.
While one particular process and apparatus has been described, it is not our intention to limit the scope of the invention by that description, or otherwise than by the terms of the appended claims.
-We claim:
1. That method of cooling which comprises plating a body of refrigerant comprising an oxide of nitrogen having an extended evaporative surface, in communication with a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron, whereby the metal will absorb said refrigerant to form a compound of the metal and an oxide of nitrogen, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
2. That method of cooling which comprises placing a body of refrigerant, consisting of nitrogen peroxide (mixture of N02 and N204), and having an extended evaporative surface, in communication with a body of metal selected from the group consisting of copper, cobalt,
nickel, barium, silver, and iron, whereby the metal will absorb said refrigerant to form a compound of the metal and the nitrogen peroxide, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
3. That method of cooling which comprises placing a body of refrigerant comprising an oxide of nitrogen having an extended evaporative surface, in communication with a body of metal consisting mainly of copper, whereby the metal will absorb said refrigerant to form a compound of the metal and an oxide of nitrogen, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
4. That method of cooling which comprises placing a body of refrigerant, consisting of nitrogen peroxide (mixture N02 and N204), and having an extended evaporative surface, in communication with a body of metal consisting mainly of copper, whereby the metal will-absorb said refrigerant to form a compound of the metal and the nitrogen peroxide, then decomposing the compound by heat and driving off the refrigerant as a gas, condensing said gas, and returning the condensed gas to said body of refrigerant.
5. Refrigerating apparatus comprising absorption means consisting of a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron, a body of refrigerant comprising an oxide of nitrogen having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
6. Refrigerating apparatus comprising absorption means consisting of a body of metal consisting mainly of copper, a body of refrigerant comprising an oxide of nitrogen having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
'7. Refrigerating apparatus comprising absorption means consisting of a body of metal selected from the group consisting of copper, cobalt, nickel, barium, silver, and iron, a body of refrigerant consisting of nitrogen peroxide (mixture NO: and N204) and having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
8. Refrigerating apparatus comprising absorp tion means consisting of a body of metal consisting mainly of copper, a body of refrigerant consisting of nitrogen peroxide (mixture of N02 and N204) and having its surface in communication with the absorption means, means for driving off refrigerant as a gas from said body of metal, and means for condensing the gaseous refrigerant and returning it to the body of refrigerant.
JOHN J. ROOT. FRANK J. SOWA.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US124953A US2131119A (en) | 1937-02-10 | 1937-02-10 | Refrigeration |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US124953A US2131119A (en) | 1937-02-10 | 1937-02-10 | Refrigeration |
Publications (1)
Publication Number | Publication Date |
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US2131119A true US2131119A (en) | 1938-09-27 |
Family
ID=22417575
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US124953A Expired - Lifetime US2131119A (en) | 1937-02-10 | 1937-02-10 | Refrigeration |
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2496459A (en) * | 1942-06-06 | 1950-02-07 | Kleen Refrigerator Inc | Absorption or adsorption refrigeration |
US3293877A (en) * | 1964-08-13 | 1966-12-27 | Continental Oil Co | Refrigerant flow control means |
US4224803A (en) * | 1978-11-07 | 1980-09-30 | Leonard Greiner | Chemical heat pump |
US4272268A (en) * | 1977-10-17 | 1981-06-09 | Leonard Greiner | Chemical heat pump |
US4332139A (en) * | 1978-12-27 | 1982-06-01 | The Director-General Of The Agency Of Industrial Science And Technology | Method for storage and recovery of thermal energy |
US4610148A (en) * | 1985-05-03 | 1986-09-09 | Shelton Samuel V | Solid adsorbent heat pump system |
US4694659A (en) * | 1985-05-03 | 1987-09-22 | Shelton Samuel V | Dual bed heat pump |
US5505059A (en) * | 1994-01-13 | 1996-04-09 | Gas Research Institute | Direct heated adsorbent bed heat pump |
EP0763701A2 (en) * | 1990-11-13 | 1997-03-19 | Rocky Research | Appliance for rapid cooling and freezing |
US5638696A (en) * | 1995-11-15 | 1997-06-17 | Cline; Calvin D. | Absorption refrigeration system |
DE102004049408A1 (en) * | 2004-10-08 | 2006-04-20 | Viessmann Werke Gmbh & Co Kg | Vacuum-sorption device, has closing unit formed as cover, which is connected with floating unit that controllably passes on cooling medium and brings closing unit to opening and closing position based on cooling medium level |
-
1937
- 1937-02-10 US US124953A patent/US2131119A/en not_active Expired - Lifetime
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2496459A (en) * | 1942-06-06 | 1950-02-07 | Kleen Refrigerator Inc | Absorption or adsorption refrigeration |
US3293877A (en) * | 1964-08-13 | 1966-12-27 | Continental Oil Co | Refrigerant flow control means |
US4272268A (en) * | 1977-10-17 | 1981-06-09 | Leonard Greiner | Chemical heat pump |
US4224803A (en) * | 1978-11-07 | 1980-09-30 | Leonard Greiner | Chemical heat pump |
US4332139A (en) * | 1978-12-27 | 1982-06-01 | The Director-General Of The Agency Of Industrial Science And Technology | Method for storage and recovery of thermal energy |
US4694659A (en) * | 1985-05-03 | 1987-09-22 | Shelton Samuel V | Dual bed heat pump |
US4610148A (en) * | 1985-05-03 | 1986-09-09 | Shelton Samuel V | Solid adsorbent heat pump system |
WO1988002089A1 (en) * | 1986-09-08 | 1988-03-24 | Shelton Samuel V | Dual bed heat pump |
EP0763701A2 (en) * | 1990-11-13 | 1997-03-19 | Rocky Research | Appliance for rapid cooling and freezing |
EP0763701A3 (en) * | 1990-11-13 | 2000-09-13 | Rocky Research | Appliance for rapid cooling and freezing |
US5505059A (en) * | 1994-01-13 | 1996-04-09 | Gas Research Institute | Direct heated adsorbent bed heat pump |
US5638696A (en) * | 1995-11-15 | 1997-06-17 | Cline; Calvin D. | Absorption refrigeration system |
DE102004049408A1 (en) * | 2004-10-08 | 2006-04-20 | Viessmann Werke Gmbh & Co Kg | Vacuum-sorption device, has closing unit formed as cover, which is connected with floating unit that controllably passes on cooling medium and brings closing unit to opening and closing position based on cooling medium level |
DE102004049408B4 (en) * | 2004-10-08 | 2006-11-23 | Viessmann Werke Gmbh & Co Kg | Vacuum sorption |
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