[go: up one dir, main page]

US2565221A - Refrigerating apparatus - Google Patents

Refrigerating apparatus Download PDF

Info

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
Application number
US660228A
Inventor
Richard S Gaugler
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
Application filed by General Motors Corp filed Critical General Motors Corp
Priority to US660228A priority Critical patent/US2565221A/en
Application granted granted Critical
Publication of US2565221A publication Critical patent/US2565221A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/18Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
    • F28F13/185Heat-exchange surfaces provided with microstructures or with porous coatings
    • F28F13/187Heat-exchange surfaces provided with microstructures or with porous coatings especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • F25B39/026Evaporators specially adapted for sorption type systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/18Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/4935Heat exchanger or boiler making
    • Y10T29/49359Cooling 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.

Landscapes

  • 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
US660228A 1946-04-06 1946-04-06 Refrigerating apparatus Expired - Lifetime US2565221A (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (7)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US2565221A (en) Refrigerating apparatus
US2615686A (en) Heat transfer device
US3826304A (en) Advantageous configuration of tubing for internal boiling
US3537514A (en) Heat pipe for low thermal conductivity working fluids
US3734135A (en) Heat exchanger with internal turbulator
US2690653A (en) Stamped plate
US1965553A (en) Beverage cooler
US1987422A (en) Method of making heat exchange apparatus
US2503595A (en) Refrigerating apparatus
US2868515A (en) Heat exchanger construction
US1915352A (en) Heat interchanger and process of making the same
US2307947A (en) Absorption refrigerating machine
US2118206A (en) Finned type cooling unit
FR2344803A1 (en) Heat exchanger for motor vehicle air conditioner - has heat exchanger made from flat tube bent into convoluted shape
US2143171A (en) Evaporator
US2595472A (en) Heat exchanger
US2532301A (en) Condenser
JPS5816187A (en) Heat transfer device
US2517654A (en) Refrigerating apparatus
US2995807A (en) Heat exchangers and methods of making the same
US1955837A (en) Method of making alpha refrigerator element
US2032134A (en) Heat exchanger
US6640885B2 (en) Three-layer condenser
DE10033972B4 (en) heat exchangers
US3555845A (en) Forced-flow evaporator for compression refrigeration equipment