US2565221A - Refrigerating apparatus - Google Patents
Refrigerating apparatus Download PDFInfo
- Publication number
- US2565221A US2565221A US660228A US66022846A US2565221A US 2565221 A US2565221 A US 2565221A US 660228 A US660228 A US 660228A US 66022846 A US66022846 A US 66022846A US 2565221 A US2565221 A US 2565221A
- Authority
- US
- United States
- Prior art keywords
- liquid
- tubing
- ribbon
- wire
- flat
- 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
Links
- 239000007788 liquid Substances 0.000 description 32
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000011261 inert gas Substances 0.000 description 4
- 238000005452 bending Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- SRVJKTDHMYAMHA-WUXMJOGZSA-N thioacetazone Chemical compound CC(=O)NC1=CC=C(\C=N\NC(N)=S)C=C1 SRVJKTDHMYAMHA-WUXMJOGZSA-N 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/18—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
- F28F13/185—Heat-exchange surfaces provided with microstructures or with porous coatings
- F28F13/187—Heat-exchange surfaces provided with microstructures or with porous coatings especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites
-
- 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
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
- F25B39/026—Evaporators specially adapted for sorption type systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/18—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/4935—Heat exchanger or boiler making
- Y10T29/49359—Cooling apparatus making, e.g., air conditioner, refrigerator
Definitions
- Fig. 1 is a plan view, partly diagrammatic, of
- Fig. 2 is a sectional view taken along the line 2-2 of Fig. 1.
- FIG. 1 illustrates a typical application in which the tubing 20 is provided with a straight section 22 connected by a degree bend 24 with the serpentine sections 26 which are composed of straight sections connected by degree bends and ending with a 90 degree bend 28.
- wire screens have been placed in the tubing at the points where the straight sections were to remain, after which the proper bends were made to form the tubin to the desired configuration as shown in Fig. 1.
- evaporator liquid is fed into one end of the tubing and covers only a small portion of the bottom of the tubing. The liquid, however, is drawn up and wets the screens to provide an increased liquid surface, which increases the rate of evaporation.
- the inert gas was circulated through the tubing in the opposite direction.
- the increased surface improves the performance in both types of absorption refrigerating apparatus.
- the amount of refrigeration performed in the portions having 90 degree and 180 degree bends is very small, since the wire screens cannot conveniently be applied to these portions.
- I provide the capillary means in. the form of a helix of flat resilient wire ribbon 30.
- the ribbon 30 is preferably made of single braided wire sleeving having 48 ends of steel weaving wire with one end up. This sleeving is preferably pulled and then flattened and coiled into 'a helix. While the tubing is still straight this flattened sleeving is uncoiled within the tubing one coil at a time so that each coil is pressed tightly against the inner surface of the tubing with one of the flat sides pressing against the wall surface.
- the coils of the helix may be made as close together as desired, but preferably they should be spaced sufllciently so that they do not overlap when the tubing is bent. I find that for 3 the configuration shown in Fig. 1 it is desirable to allow a space between each coil which is slightly less than one-half the width of the flat ribbon.
- the braided sleeving in reality forms two thicknesses of wire gauze in flat area contact with each other, and with one outer side pressing tightly. against the wall of the tubing. This helix of flattened wire sleeving extends from the point 32 at the inlet end continuously through the tubing 20 to the point 34 at the outlet end of the heat transfer apparatus.
- the tubing is bent on any suitable forming machine to the shape desired, such as is shown in Fig. 1, without any diillculty caused by the presence of the wire 'ribbon within, since the resilient wire ribbon is extremely flexible and will readily conform itself to the change in shape required by the bending.
- the liquid to be evaporated is fed into the tubing at one end and flows along the bottom of the tubing as indicated by the reference character 36 until it is evaporated.
- This liquid wets the bottom of each coil of the helix of wire ribbon 30 and the two adjacent tightly packed sheets of wire gauze forms a capillary structure which attracts the liquid to be evaporated, such as ammonia.
- the liquid to be evaporated such as ammonia.
- the gas is preferably circulated through the tubing in the opposite direction to the liquid flow and the liquid evaporates from the fiat exposed surface of the ribbon as well as from the edges thereof into the inert gas.
- the liquid merely evaporates because of the reduced vapor pressure caused by the removal of vapor from the tubing.
- a small fillet of liquid forms at the edge of the wire ribbon so that very little surface is not wetted with liquid.
- the surface is increased by the surface provided by the edges of the wire ribbon and some turbulence is provided by the irregular wall surface formed by the coils and the spaces between.
- the heat transfer is improved by having the coils tightly in contact with the outer walls since the heat passing through the walls of the tubing passes directly to the liquid in the coils of wire ribbon. Due to this excellent heat transfer and the large liquid surface the evaporator has a with liquid, and capillary means in the form of a flexible resilient flat ribbon containing 9. p111- rality of layers of wire gauze extending substantially helically throughout the convolutions of the tubular portions with the flat surface of the ribbon in a substantially surface contact with the interior surface of the tubular portions, the bottom of each turn of the helix dipping into the liquid to saturate the capillary means by capillary action to provide an exposed liquid holding surface of large area above the surface of the liquid.
- Heat transfer apparatus including a member having tubular portions with turns therein, said tubular portions being onl partially filled with liquid, and capillary means in the form of a flexible resilient flat ribbon containing a plurality of layers of wire gauze extending substantially helically throughout the convolutions of the tubular portions with the flat surface of the ribbon in a substantially surface contact with the interior surface of the tubular portions, the bottom of each turn of the helix dipping into the liquid to saturate the capillary means by capillary action, said flat ribbon covering the major portion of the interior surface through that part of the tubular portions through which it extends to provide an exposed liquid holding surface of large area above the surface of the liquid.
- Heat transfer apparatus including a contalner only partially filled with liquid, and capillary means in the form of parallel spaced portions of flattened wire sleeving extending from said liquid in flat contact with the interior surface of the container, said capillary means having capillary flow throughout in all directions for exposing liquid above the normal liquid level in heat exchange relation with the walls of the container, the portions of flattened wire sleeving covering the major portion of the interior surface of the container through which the flattened sleeving extends to provide an exposed liquid holding surface of large area above the surface of the liquid.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
Aug. 21, 1951 R. s. GAUGLER REFRIGERATING APPARATUS Filed April 6, 1946 Q05 HOV IN VEN TOR.
LIQUID FLow Patented Aug. 21, 1951 UNITED STATES PATENT OFFICE I p o f 2,565,221
. :REFRIGERATING APPARATUS Richard S. Gaugler, Dayton, Ohio, asslgnor to General Motors Corporation, Dayton, Ohio, a corporation of Delaware. Application April s, 1946, Serial No. 660,228
3 Claims. (Cl. 26l 104) l "This invention relates to heat transfer ap- Paratus such as for example, may' be. used in absorption refrigerating apparatus- In- 'bsorption evaporators'it has been enstomary to place wire screens or wire cloth within the evaporatortubing against the walls thereor after the bendingand as a result they have'f been applied only to the straight portions thereof. This limits the area of the capillary surface which may be exposed in contact with the walls of the tubing and therefore limits the total efi'ective evaporating surface.
It is an object of my invention to provide a heat transferapparatus with a simple inexpensive resilient form of capillary means which may be applied to containers of a. wide variety of configurations in firm contact'with the interior walls thereof.
It is another object of'my invention'to provide a heat transfer apparatus with a simple inexpensive resilient form of capillary means which may be applied to an intermediate form of the container and which can be bent along with the bending of the container.
It is another object of my invention to provide a heat transfer apparatus with a simple inexpensive resilient form of capillary means which may be applied to straight tubing which thereafter can be bent to the desired configuration without damage or without displacing the capillary means.
These objects are attained by forming braided wire sleeving into a flat resilient ribbon and coiling it into the helix after which it is-inserted into the tubing anduncoiled one coil at a time so that it .presses firmly against the interior wall of the tubing. After this, the tubing is bent to a serpentine shape or any other shape desired. The flexibility of the ribbon makes it possible for it to conform to the shape of the tubing after the bending and remain tightly against the interior wall of the tubing without any substantial displacement. The liquid to be evaporated flows and collects in'the bottom of the tubing and saturates the flat ribbon providing a liquid surface of large area from which the liquid evaporates.
Further objects and advantages of the present invention will be apparent from the following description, reference being had to the accompanying drawings, wherein a preferred form of the present invention is clearly shown.
In the drawings:
Fig. 1 is a plan view, partly diagrammatic, of
an absorption refrigeration evaporator or other 7 heat transfer apparatus embodying one form of my invention; and
Fig. 2 is a sectional view taken along the line 2-2 of Fig. 1.
Although my invention may be applied to containers of a wide variety of shapes it is most easily applied to the most common application, namely to tubing. Fig. 1 illustrates a typical application in which the tubing 20 is provided with a straight section 22 connected by a degree bend 24 with the serpentine sections 26 which are composed of straight sections connected by degree bends and ending with a 90 degree bend 28. In the past, wire screens have been placed in the tubing at the points where the straight sections were to remain, after which the proper bends were made to form the tubin to the desired configuration as shown in Fig. 1. In this type of evaporator liquid is fed into one end of the tubing and covers only a small portion of the bottom of the tubing. The liquid, however, is drawn up and wets the screens to provide an increased liquid surface, which increases the rate of evaporation.
In the partial pressure absorption apparatus the inert gas was circulated through the tubing in the opposite direction. However, the increased surface improves the performance in both types of absorption refrigerating apparatus. With this arrangement, however, the amount of refrigeration performed in the portions having 90 degree and 180 degree bends is very small, since the wire screens cannot conveniently be applied to these portions.
According to my invention, I provide the capillary means in. the form of a helix of flat resilient wire ribbon 30. The ribbon 30 is preferably made of single braided wire sleeving having 48 ends of steel weaving wire with one end up. This sleeving is preferably pulled and then flattened and coiled into 'a helix. While the tubing is still straight this flattened sleeving is uncoiled within the tubing one coil at a time so that each coil is pressed tightly against the inner surface of the tubing with one of the flat sides pressing against the wall surface.
The coils of the helix may be made as close together as desired, but preferably they should be spaced sufllciently so that they do not overlap when the tubing is bent. I find that for 3 the configuration shown in Fig. 1 it is desirable to allow a space between each coil which is slightly less than one-half the width of the flat ribbon. The braided sleeving in reality forms two thicknesses of wire gauze in flat area contact with each other, and with one outer side pressing tightly. against the wall of the tubing. This helix of flattened wire sleeving extends from the point 32 at the inlet end continuously through the tubing 20 to the point 34 at the outlet end of the heat transfer apparatus. The tubing is bent on any suitable forming machine to the shape desired, such as is shown in Fig. 1, without any diillculty caused by the presence of the wire 'ribbon within, since the resilient wire ribbon is extremely flexible and will readily conform itself to the change in shape required by the bending.
In use, the liquid to be evaporated is fed into the tubing at one end and flows along the bottom of the tubing as indicated by the reference character 36 until it is evaporated. This liquid wets the bottom of each coil of the helix of wire ribbon 30 and the two adjacent tightly packed sheets of wire gauze forms a capillary structure which attracts the liquid to be evaporated, such as ammonia. This causes the ribbon to be saturated all along the tubing as far as the liquid supply holds out. In the case of inert gas machines the gas is preferably circulated through the tubing in the opposite direction to the liquid flow and the liquid evaporates from the fiat exposed surface of the ribbon as well as from the edges thereof into the inert gas. If no inert gas is used, the liquid merely evaporates because of the reduced vapor pressure caused by the removal of vapor from the tubing. A small fillet of liquid forms at the edge of the wire ribbon so that very little surface is not wetted with liquid. The surface is increased by the surface provided by the edges of the wire ribbon and some turbulence is provided by the irregular wall surface formed by the coils and the spaces between.
The heat transfer is improved by having the coils tightly in contact with the outer walls since the heat passing through the walls of the tubing passes directly to the liquid in the coils of wire ribbon. Due to this excellent heat transfer and the large liquid surface the evaporator has a with liquid, and capillary means in the form of a flexible resilient flat ribbon containing 9. p111- rality of layers of wire gauze extending substantially helically throughout the convolutions of the tubular portions with the flat surface of the ribbon in a substantially surface contact with the interior surface of the tubular portions, the bottom of each turn of the helix dipping into the liquid to saturate the capillary means by capillary action to provide an exposed liquid holding surface of large area above the surface of the liquid.
2. Heat transfer apparatus including a member having tubular portions with turns therein, said tubular portions being onl partially filled with liquid, and capillary means in the form of a flexible resilient flat ribbon containing a plurality of layers of wire gauze extending substantially helically throughout the convolutions of the tubular portions with the flat surface of the ribbon in a substantially surface contact with the interior surface of the tubular portions, the bottom of each turn of the helix dipping into the liquid to saturate the capillary means by capillary action, said flat ribbon covering the major portion of the interior surface through that part of the tubular portions through which it extends to provide an exposed liquid holding surface of large area above the surface of the liquid.
3. Heat transfer apparatus including a contalner only partially filled with liquid, and capillary means in the form of parallel spaced portions of flattened wire sleeving extending from said liquid in flat contact with the interior surface of the container, said capillary means having capillary flow throughout in all directions for exposing liquid above the normal liquid level in heat exchange relation with the walls of the container, the portions of flattened wire sleeving covering the major portion of the interior surface of the container through which the flattened sleeving extends to provide an exposed liquid holding surface of large area above the surface of the liquid.
RICHARD S. GAUGLER.
REFERENCES CITED The following references are of record in the
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US660228A US2565221A (en) | 1946-04-06 | 1946-04-06 | Refrigerating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US660228A US2565221A (en) | 1946-04-06 | 1946-04-06 | Refrigerating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2565221A true US2565221A (en) | 1951-08-21 |
Family
ID=24648656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US660228A Expired - Lifetime US2565221A (en) | 1946-04-06 | 1946-04-06 | Refrigerating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2565221A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2691281A (en) * | 1951-01-16 | 1954-10-12 | Servel Inc | Heat and material transfer apparatus |
| US2720763A (en) * | 1951-05-16 | 1955-10-18 | Doebeli Oscar | Evaporator for absorption type refrigerating systems |
| US2983107A (en) * | 1958-09-29 | 1961-05-09 | British Oxygen Co Ltd | Vaporisation of liquefied gases |
| US3318586A (en) * | 1965-01-11 | 1967-05-09 | Meredith Diven | Mass transfer unit using spaced flexible materials, and method of construction |
| US3384154A (en) * | 1956-08-30 | 1968-05-21 | Union Carbide Corp | Heat exchange system |
| US3523577A (en) * | 1956-08-30 | 1970-08-11 | Union Carbide Corp | Heat exchange system |
| EP0058628A3 (en) * | 1981-02-13 | 1983-04-13 | Yvan Aragou | Heat exchanger with capillary structure for refrigeration machines and/or heat pumps, and method for obtaining the same |
| US5718848A (en) * | 1994-08-18 | 1998-02-17 | F F Seeley Nominees Pty Ltd | Intensification of evaporation and heat transfer |
| US5800595A (en) * | 1994-08-30 | 1998-09-01 | William Allen Trusts Pty Ltd | Spaced evaporative wicks within an air cooler |
| US20080099191A1 (en) * | 2005-02-02 | 2008-05-01 | Carrier Corporation | Parallel Flow Heat Exchangers Incorporating Porous Inserts |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1604779A (en) * | 1923-07-13 | 1926-10-26 | Elliott Co | Desuperheater |
| US1983295A (en) * | 1930-01-24 | 1934-12-04 | Electrolux Servel Corp | Absorber for refrigeration systems |
| US2068955A (en) * | 1935-04-04 | 1937-01-26 | Richard W Kritzer | Refrigerating coil |
| US2122504A (en) * | 1936-05-02 | 1938-07-05 | Wilson Lee | Heating apparatus |
| US2295988A (en) * | 1939-04-24 | 1942-09-15 | Hoover Co | Refrigeration |
| US2300579A (en) * | 1936-09-03 | 1942-11-03 | Servel Inc | Refrigeration |
| US2307947A (en) * | 1941-05-12 | 1943-01-12 | Payne Charles Alfred | Absorption refrigerating machine |
-
1946
- 1946-04-06 US US660228A patent/US2565221A/en not_active Expired - Lifetime
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1604779A (en) * | 1923-07-13 | 1926-10-26 | Elliott Co | Desuperheater |
| US1983295A (en) * | 1930-01-24 | 1934-12-04 | Electrolux Servel Corp | Absorber for refrigeration systems |
| US2068955A (en) * | 1935-04-04 | 1937-01-26 | Richard W Kritzer | Refrigerating coil |
| US2122504A (en) * | 1936-05-02 | 1938-07-05 | Wilson Lee | Heating apparatus |
| US2300579A (en) * | 1936-09-03 | 1942-11-03 | Servel Inc | Refrigeration |
| US2295988A (en) * | 1939-04-24 | 1942-09-15 | Hoover Co | Refrigeration |
| US2307947A (en) * | 1941-05-12 | 1943-01-12 | Payne Charles Alfred | Absorption refrigerating machine |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2691281A (en) * | 1951-01-16 | 1954-10-12 | Servel Inc | Heat and material transfer apparatus |
| US2720763A (en) * | 1951-05-16 | 1955-10-18 | Doebeli Oscar | Evaporator for absorption type refrigerating systems |
| US3384154A (en) * | 1956-08-30 | 1968-05-21 | Union Carbide Corp | Heat exchange system |
| US3523577A (en) * | 1956-08-30 | 1970-08-11 | Union Carbide Corp | Heat exchange system |
| US2983107A (en) * | 1958-09-29 | 1961-05-09 | British Oxygen Co Ltd | Vaporisation of liquefied gases |
| US3318586A (en) * | 1965-01-11 | 1967-05-09 | Meredith Diven | Mass transfer unit using spaced flexible materials, and method of construction |
| EP0058628A3 (en) * | 1981-02-13 | 1983-04-13 | Yvan Aragou | Heat exchanger with capillary structure for refrigeration machines and/or heat pumps, and method for obtaining the same |
| US4448043A (en) * | 1981-02-13 | 1984-05-15 | Yvan Aragou | Heat exchanger with a capillary structure for refrigeration equipment and/or heat pumps and method of making the same |
| US5718848A (en) * | 1994-08-18 | 1998-02-17 | F F Seeley Nominees Pty Ltd | Intensification of evaporation and heat transfer |
| US5800595A (en) * | 1994-08-30 | 1998-09-01 | William Allen Trusts Pty Ltd | Spaced evaporative wicks within an air cooler |
| US20080099191A1 (en) * | 2005-02-02 | 2008-05-01 | Carrier Corporation | Parallel Flow Heat Exchangers Incorporating Porous Inserts |
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