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US20140165641A1 - Distributor for evaporative condenser header or cooler header - Google Patents

Distributor for evaporative condenser header or cooler header Download PDF

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Publication number
US20140165641A1
US20140165641A1 US13/718,563 US201213718563A US2014165641A1 US 20140165641 A1 US20140165641 A1 US 20140165641A1 US 201213718563 A US201213718563 A US 201213718563A US 2014165641 A1 US2014165641 A1 US 2014165641A1
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US
United States
Prior art keywords
header
inlet
distributor
heat exchange
fluid
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.)
Abandoned
Application number
US13/718,563
Inventor
Zahid Ayub
Peng Peng
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.)
American Sino Heat Transfer LLC
AMSI HEAT TRANSFER LLC
Original Assignee
American Sino Heat Transfer LLC
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 American Sino Heat Transfer LLC filed Critical American Sino Heat Transfer LLC
Priority to US13/718,563 priority Critical patent/US20140165641A1/en
Assigned to AMSI HEAT TRANSFER LLC reassignment AMSI HEAT TRANSFER LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: PENG, PENG, AYUB, ZAHID
Publication of US20140165641A1 publication Critical patent/US20140165641A1/en
Abandoned legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/06Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
    • F28C3/08Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour with change of state, e.g. absorption, evaporation, condensation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B1/00Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/06Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D5/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
    • F28D5/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/028Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using inserts for modifying the pattern of flow inside the header box, e.g. by using flow restrictors or permeable bodies or blocks with channels

Definitions

  • the present invention relates to heat exchangers and more particularly to evaporative condensers and coolers.
  • Evaporative condensers are condensers where water is sprayed onto a heat exchanger to condense a gas into a liquid.
  • a compressor compresses a heat exchange fluid, such as ammonia.
  • the output of the compressor is hot, high pressure ammonia gas.
  • the gas is provided to a condenser, where it condenses into a liquid.
  • the liquid ammonia then passes through an expansion valve, where it drops in pressure and decreases in temperature to provide refrigeration.
  • the heat exchanger for the fluid is a set of coils or tubes.
  • the ammonia gas flows into a header and then into the coils. Condensed or liquid ammonia flows out of the coils to an outlet header.
  • the liquid disposes heat to the spraying water on the outside of the coils.
  • the cooler uses an input header for the liquid.
  • a heat exchanger comprises inlet headers.
  • the inlet header has a fluid inlet and an interior cavity.
  • the outlet header has a fluid outlet.
  • Heat exchange elements are coupled to and in fluid communication with the inlet and outlet headers.
  • the heat exchange elements comprise first and second heat exchange elements.
  • the first heat exchange element is coupled to the inlet header at a first location.
  • the second heat exchange element is coupled to the inlet header at a second location. The first location is closer to the fluid inlet than is the second location.
  • a distributor is located in the interior cavity of the inlet header between the fluid inlet and the heat exchange elements and extends between the first and second locations and the fluid inlet. The distributor causes back pressure for fluid entering the inlet header from the fluid inlet.
  • the distributor comprises a perforated wall.
  • the heat exchange elements comprise coils.
  • the inlet header comprises a pipe and the distributor comprises a perforated plate located in the pipe.
  • an evaporative condenser comprises a condenser unit.
  • a water sprayer is located above the condenser unit.
  • a fill section is located below the condenser unit.
  • a basin located below the fill section.
  • At least one fan for flowing air through the condenser unit and the fill section is provided.
  • the condenser unit comprises an inlet header and an outlet header.
  • the inlet header has a fluid inlet at a first location.
  • the inlet header has heat exchange elements at locations other than the first location.
  • a distributor is in the inlet header between the first and other locations. The distributor applies back pressure to incoming fluid in the inlet header.
  • the distributor further comprises a perforated wall.
  • the heat exchange elements comprise coils.
  • the inlet header comprises a pipe and the distributor comprises a perforated plate located in the pipe.
  • the perforated plate is flat. In accordance with still another aspect, the perforated plate is curved.
  • FIG. 1 is a schematic view of an evaporative condenser.
  • FIG. 2 is a top plan view of a portion of the heat exchanger condenser and inlet header.
  • FIG. 3 is a cross-sectional view of the header of FIG. 2 , taken along lines III-III.
  • FIGS. 3A and FIG. 3B are cross-sectional views of the header, similar to FIG. 3 , but of other embodiments.
  • FIG. 4 is a view of a distributor.
  • FIG. 5 shows the distributor in accordance with another embodiment.
  • any heat exchanger depends upon whether the incoming fluid is distributed evenly over all portions of the heat exchanger. For example, if the heat exchanger has coils arranged side by side, if the center coils receive more fluid than the other coils, then efficiency declines.
  • the heat exchanger described herein evenly distributes the incoming fluid throughout all portions thereof, thereby increasing efficiency.
  • the heat exchanger can be a cooler, the particular application shown is in an evaporative cooler.
  • FIG. 1 shows an evaporative condenser 11 .
  • Sprayers 61 spray water onto a heat exchanger 13 .
  • a fan 15 draws air 17 through the wetted heat exchanger 13 to provide evaporative cooling and condensing of a fluid (typically from a gas into a liquid).
  • the evaporative condenser 11 has a housing 19 .
  • the heat exchanger 13 is located in the housing.
  • a fill or stuffing section 21 below the heat exchanger is a fill or stuffing section 21 .
  • the fill section 21 has layers that expose descending water to air flow. The layers can be made of plastic, etc.
  • Below the fill section 21 is a basin 23 to catch the water.
  • the housing also has a plenum 25 that communicates with the heat exchanger and the fill section.
  • the fan 15 draws air through the heat exchanger 13 , in through the fill section 21 , through demisters 27 or dehydrators, into the plenum 25 and out of the housing.
  • the heat exchanger 13 has heat exchange elements 31 that extend from an inlet header 33 to an outlet header 35 .
  • the heat exchanger elements 31 are coils, however the heat exchange elements could be plates.
  • Gas enters the inlet header 33 and then the coils 31 . Once in the coils, the gas condenses to a liquid. The liquid exits the coils 31 into the outlet header 35 .
  • the inlet header 33 has an inlet pipe 37 (see FIG. 1 ) which delivers the gas to the inlet header 33 .
  • the outlet header 35 has an outlet pipe 39 , which removes the liquid from the outlet header.
  • the heat exchanger and inlet header are shown.
  • the inlet header 33 is a pipe with an interior cavity 41 that extends between two ends 43 .
  • the header can be circular in transverse cross-section, rectangular, etc.
  • the inlet pipe 37 and the heat exchange elements 31 all communicate with the interior cavity 41 .
  • the heat exchange elements are connected with the inlet header by way of feed pipe stubs 38 .
  • the ends 43 of the header are closed such as with caps.
  • the inlet pipe 37 is typically located in the center between the ends 43 .
  • the coils 31 are spaced out along the length of the header from one end to the other end 43 . Consequently, some coils are located closer to the inlet pipe 37 than other coils. For example, centrally located coils 31 A- 31 D are closer to the inlet pipe than are end coils 31 E, 31 F, 31 G, 31 H.
  • a distributor 51 is provided in the interior cavity 41 of the inlet header 33 .
  • the distributor 51 is a plate with perforations 53 .
  • the perforations are circular holes; however the perforations could be any shape such as slots, etc.
  • the number and size of the perforations is determined relative to the flow of the incoming gas.
  • the distributor 51 applies a back pressure to the gas in the inlet header 33 . This back pressure causes the gas to move from the central location of the inlet header out along the length of the inlet header toward the ends 43 . This in turn promotes even distribution of the gas to the coils 31 .
  • the inlet pipe 37 and feed pipes 38 are connected to the header.
  • the distributor plate 51 is inserted into the header interior cavity.
  • the length of the distributor plate is slightly less than the length of the header.
  • the distributor plate is positioned (vertically as shown in the orientation of FIG. 3 ) and then tacked or welded in place. The tacked points need only be at the ends and serve to immobilize the distributor inside the header. Then the end caps can be put onto the header.
  • FIG. 5 shows another embodiment of the distributor 51 A, having openings 53 A in the sites adjacent to the header 33 .
  • the distributor plate 51 is located between the inlet pipe 37 and the coils 31 so that gas flowing into the header passes through the distributor plate to flow into the coils.
  • the distributor plate 51 can be positioned along a vertical chord, as shown by solid lines in FIG. 3 .
  • the plate is positioned closer to the feed pipes than to the inlet pipe 37 .
  • the plate 51 could be positioned closer to the inlet pipe 37 , as shown by dashed lines in FIG. 3 .
  • the plate could also be positioned through the center of the header instead of along a chord.
  • FIG. 3 shows the distributor plate 51 as flat.
  • the distributor plate 51 need not be flat but can be curved.
  • FIG. 3A shows the distributor plate as concave relative to the inlet pipe 37 and can be closer to the inlet pipe (as shown by dashed lines) or closer to the feed pipes 38 (as shown in dashed lines).
  • FIG. 3B shows the distributor plate as convex relative to the inlet pipe 37 and can be closer to the feed pipes 38 (as shown in solid lines) or to the inlet pipe 37 (as shown in dashed lines).
  • the outlet header is not provided with a distributor.
  • gas enters the header. While some gas enters the coil or coils 31 A- 31 D adjacent to the inlet pipe 37 , much of the gas flows toward the ends of the header and into the associated coils (for example 31 E- 31 H).
  • the coils which are all the same size, all receive equal amounts of the gas.
  • the heat exchanger operates more efficiently.
  • the distributor has been described in conjunction with an evaporative condenser as the preferred embodiment, it can also be used with other heat exchangers, such as coolers.
  • the heat exchanger described above can be used as a cooler.
  • the distributor When used as a cooler, the distributor is in the inlet header (which is now 35 ). Liquid enters the header and encounters back pressure due to the distributor 51 . The liquid thus extends along the length of the header and enters the coils 31 as spaced along the length of the header.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

A heat exchanger has heat exchange elements and an inlet header and an outlet header that fluidly communicate with the heat exchange elements. The inlet header has a fluid inlet. The heat exchange elements are connected to the inlet header along a length of the inlet header and are various distances from the fluid inlet. A distributor is located inside the inlet header, which distributor forms a perforated wall between the fluid inlet and the heat exchange elements. The distributor provides back pressure to incoming fluid into the inlet header, wherein the fluid is evenly distributed between the heat exchange elements.

Description

    FIELD OF THE INVENTION
  • The present invention relates to heat exchangers and more particularly to evaporative condensers and coolers.
  • BACKGROUND OF THE INVENTION
  • Evaporative condensers are condensers where water is sprayed onto a heat exchanger to condense a gas into a liquid. For example, in a refrigeration system, a compressor compresses a heat exchange fluid, such as ammonia. The output of the compressor is hot, high pressure ammonia gas. The gas is provided to a condenser, where it condenses into a liquid. The liquid ammonia then passes through an expansion valve, where it drops in pressure and decreases in temperature to provide refrigeration.
  • In a conventional evaporative condenser, the heat exchanger for the fluid is a set of coils or tubes. The ammonia gas flows into a header and then into the coils. Condensed or liquid ammonia flows out of the coils to an outlet header.
  • In a cooler, the liquid disposes heat to the spraying water on the outside of the coils. The cooler uses an input header for the liquid.
  • It is desirable to make improvements over conventional condensers. It is also desirable to make improvements to conventional coolers.
  • SUMMARY OF THE INVENTION
  • A heat exchanger comprises inlet headers. The inlet header has a fluid inlet and an interior cavity. The outlet header has a fluid outlet. Heat exchange elements are coupled to and in fluid communication with the inlet and outlet headers. The heat exchange elements comprise first and second heat exchange elements. The first heat exchange element is coupled to the inlet header at a first location. The second heat exchange element is coupled to the inlet header at a second location. The first location is closer to the fluid inlet than is the second location. A distributor is located in the interior cavity of the inlet header between the fluid inlet and the heat exchange elements and extends between the first and second locations and the fluid inlet. The distributor causes back pressure for fluid entering the inlet header from the fluid inlet.
  • In accordance with one aspect, the distributor comprises a perforated wall.
  • In accordance with another aspect, the heat exchange elements comprise coils.
  • In accordance with another aspect, the inlet header comprises a pipe and the distributor comprises a perforated plate located in the pipe.
  • In accordance with another aspect, an evaporative condenser comprises a condenser unit. A water sprayer is located above the condenser unit. A fill section is located below the condenser unit. A basin located below the fill section. At least one fan for flowing air through the condenser unit and the fill section is provided. The condenser unit comprises an inlet header and an outlet header. The inlet header has a fluid inlet at a first location. The inlet header has heat exchange elements at locations other than the first location. A distributor is in the inlet header between the first and other locations. The distributor applies back pressure to incoming fluid in the inlet header.
  • In accordance with still another aspect, the distributor further comprises a perforated wall.
  • In accordance with still another aspect, the heat exchange elements comprise coils.
  • In accordance with another aspect, the inlet header comprises a pipe and the distributor comprises a perforated plate located in the pipe.
  • In accordance with still another aspect, the perforated plate is flat. In accordance with still another aspect, the perforated plate is curved.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 is a schematic view of an evaporative condenser.
  • FIG. 2 is a top plan view of a portion of the heat exchanger condenser and inlet header.
  • FIG. 3 is a cross-sectional view of the header of FIG. 2, taken along lines III-III.
  • FIGS. 3A and FIG. 3B are cross-sectional views of the header, similar to FIG. 3, but of other embodiments.
  • FIG. 4 is a view of a distributor. FIG. 5 shows the distributor in accordance with another embodiment.
  • DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • The efficiency of any heat exchanger depends upon whether the incoming fluid is distributed evenly over all portions of the heat exchanger. For example, if the heat exchanger has coils arranged side by side, if the center coils receive more fluid than the other coils, then efficiency declines.
  • The heat exchanger described herein evenly distributes the incoming fluid throughout all portions thereof, thereby increasing efficiency. Although the heat exchanger can be a cooler, the particular application shown is in an evaporative cooler.
  • FIG. 1 shows an evaporative condenser 11. Sprayers 61 spray water onto a heat exchanger 13. A fan 15 draws air 17 through the wetted heat exchanger 13 to provide evaporative cooling and condensing of a fluid (typically from a gas into a liquid).
  • The evaporative condenser 11 has a housing 19. The heat exchanger 13 is located in the housing. Below the heat exchanger is a fill or stuffing section 21. The fill section 21 has layers that expose descending water to air flow. The layers can be made of plastic, etc. Below the fill section 21 is a basin 23 to catch the water. The housing also has a plenum 25 that communicates with the heat exchanger and the fill section. The fan 15 draws air through the heat exchanger 13, in through the fill section 21, through demisters 27 or dehydrators, into the plenum 25 and out of the housing.
  • The heat exchanger 13 has heat exchange elements 31 that extend from an inlet header 33 to an outlet header 35. In the preferred embodiment, the heat exchanger elements 31 are coils, however the heat exchange elements could be plates. Thus, there is a first set of coils 31A (see FIG. 2), a second set of coils 31B, a third set of coils 31C and so on. Gas enters the inlet header 33 and then the coils 31. Once in the coils, the gas condenses to a liquid. The liquid exits the coils 31 into the outlet header 35.
  • The inlet header 33 has an inlet pipe 37 (see FIG. 1) which delivers the gas to the inlet header 33. Likewise, the outlet header 35 has an outlet pipe 39, which removes the liquid from the outlet header. Referring to FIGS. 2 and 3, the heat exchanger and inlet header are shown. In the preferred embodiment, the inlet header 33 is a pipe with an interior cavity 41 that extends between two ends 43. The header can be circular in transverse cross-section, rectangular, etc. The inlet pipe 37 and the heat exchange elements 31 all communicate with the interior cavity 41. The heat exchange elements are connected with the inlet header by way of feed pipe stubs 38. The ends 43 of the header are closed such as with caps.
  • The inlet pipe 37 is typically located in the center between the ends 43. The coils 31 are spaced out along the length of the header from one end to the other end 43. Consequently, some coils are located closer to the inlet pipe 37 than other coils. For example, centrally located coils 31A-31D are closer to the inlet pipe than are end coils 31E, 31F, 31G, 31H.
  • In order to evenly distribute the end feed fluid to all of the heat exchange coils, a distributor 51 is provided in the interior cavity 41 of the inlet header 33. As shown in FIGS. 3 and 4, the distributor 51 is a plate with perforations 53. In the preferred embodiment, the perforations are circular holes; however the perforations could be any shape such as slots, etc. The number and size of the perforations is determined relative to the flow of the incoming gas. The distributor 51 applies a back pressure to the gas in the inlet header 33. This back pressure causes the gas to move from the central location of the inlet header out along the length of the inlet header toward the ends 43. This in turn promotes even distribution of the gas to the coils 31.
  • To assemble the inlet header 33, the inlet pipe 37 and feed pipes 38 are connected to the header. With the interior cavity 41 of the header exposed by way of an open end 43, the distributor plate 51 is inserted into the header interior cavity. The length of the distributor plate is slightly less than the length of the header. The distributor plate is positioned (vertically as shown in the orientation of FIG. 3) and then tacked or welded in place. The tacked points need only be at the ends and serve to immobilize the distributor inside the header. Then the end caps can be put onto the header.
  • Because the plate is porous, there can be gaps between the plate and the header. FIG. 5 shows another embodiment of the distributor 51A, having openings 53A in the sites adjacent to the header 33.
  • The distributor plate 51 is located between the inlet pipe 37 and the coils 31 so that gas flowing into the header passes through the distributor plate to flow into the coils. The distributor plate 51 can be positioned along a vertical chord, as shown by solid lines in FIG. 3. The plate is positioned closer to the feed pipes than to the inlet pipe 37. The plate 51 could be positioned closer to the inlet pipe 37, as shown by dashed lines in FIG. 3. The plate could also be positioned through the center of the header instead of along a chord.
  • FIG. 3 shows the distributor plate 51 as flat. The distributor plate 51 need not be flat but can be curved. FIG. 3A shows the distributor plate as concave relative to the inlet pipe 37 and can be closer to the inlet pipe (as shown by dashed lines) or closer to the feed pipes 38 (as shown in dashed lines). FIG. 3B shows the distributor plate as convex relative to the inlet pipe 37 and can be closer to the feed pipes 38 (as shown in solid lines) or to the inlet pipe 37 (as shown in dashed lines).
  • The outlet header is not provided with a distributor.
  • In operation, gas enters the header. While some gas enters the coil or coils 31A-31D adjacent to the inlet pipe 37, much of the gas flows toward the ends of the header and into the associated coils (for example 31E-31H). The coils, which are all the same size, all receive equal amounts of the gas. Thus, the heat exchanger operates more efficiently.
  • Although the distributor has been described in conjunction with an evaporative condenser as the preferred embodiment, it can also be used with other heat exchangers, such as coolers. The heat exchanger described above can be used as a cooler. When used as a cooler, the distributor is in the inlet header (which is now 35). Liquid enters the header and encounters back pressure due to the distributor 51. The liquid thus extends along the length of the header and enters the coils 31 as spaced along the length of the header.
  • The foregoing disclosure and showings made in the drawings are merely illustrative of the principles of this invention and are not to be interpreted in a limiting sense.

Claims (10)

1. A heat exchanger, comprising:
a) an inlet header having a fluid inlet and an interior cavity;
b) an outlet header having a fluid outlet;
c) heat exchange elements coupled to and in fluid communication with the inlet and outlet headers, the heat exchange elements comprising first and second heat exchange elements, the first heat exchange element coupled to the inlet header at a first location, the second heat exchange element coupled to the inlet header at a second location, the first location being closer to the fluid inlet than is the second location;
d) a distributor located in the interior cavity of the inlet header between the fluid inlet and the heat exchange elements and extending between the first and second locations and the fluid inlet, the distributor causing back pressure for fluid entering the inlet header from the fluid inlet.
2. The heat exchanger of claim 1 wherein the distributor further comprises a perforated wall.
3. The heat exchanger of claim 2 wherein the heat exchange elements comprise coils.
4. The heat exchanger of claim 1 wherein the inlet header comprises a pipe and the distributor comprises a perforated plate located in the pipe.
5. An evaporative condenser, comprising:
a) a condenser unit;
b) a water sprayer located above the condenser unit;
c) a fill section located below the condenser unit;
d) a basin located below the fill section;
e) at least one fan for flowing air through the condenser unit and the fill section;
f) the condenser unit comprising an inlet header and an outlet header, the inlet header having a fluid inlet at a first location, the inlet header having heat exchange elements at locations other than the first location;
g) a distributor in the inlet header between the first and other locations, the distributor applying back pressure to fluid entering the inlet header from the fluid inlet.
6. The heat exchanger of claim 5 wherein the distributor further comprises a perforated wall.
7. The heat exchanger of claim 6 wherein the heat exchange elements comprise coils.
8. The heat exchanger of claim 5 wherein the inlet header comprises a pipe and the distributor comprises a perforated plate located in the pipe.
9. The heat exchanger of claim 8 wherein the perforated plate is flat.
10. The heat exchanger of claim 8 wherein the perforated plate is curved.
US13/718,563 2012-12-18 2012-12-18 Distributor for evaporative condenser header or cooler header Abandoned US20140165641A1 (en)

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Publication number Priority date Publication date Assignee Title
CN105020925A (en) * 2015-08-18 2015-11-04 重庆达孚制冷设备有限责任公司 Integrated cold/hot water unit adopting evaporative condenser
WO2016118895A1 (en) * 2015-01-23 2016-07-28 Lingelbach John Shell and plate condenser, method for condensing a refrigerant, and method for cooling a liquid
DE102016011879A1 (en) 2016-10-06 2018-04-12 EAW Energieanlagenbau GmbH Westenfeld Cooling device and method for recooling liquids in closed hydraulic systems

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US4683101A (en) * 1985-12-26 1987-07-28 Baltimore Aircoil Company, Inc. Cross flow evaporative coil fluid cooling apparatus and method of cooling
US5203407A (en) * 1990-11-07 1993-04-20 Zexel Corporation Vehicle-loaded parallel flow type heat exchanger
US5435382A (en) * 1993-06-16 1995-07-25 Baltimore Aircoil Company, Inc. Combination direct and indirect closed circuit evaporative heat exchanger
US6142219A (en) * 1999-03-08 2000-11-07 Amstead Industries Incorporated Closed circuit heat exchange system and method with reduced water consumption
US6820685B1 (en) * 2004-02-26 2004-11-23 Baltimore Aircoil Company, Inc. Densified heat transfer tube bundle
US7275394B2 (en) * 2005-04-22 2007-10-02 Visteon Global Technologies, Inc. Heat exchanger having a distributer plate
US20080023185A1 (en) * 2006-07-25 2008-01-31 Henry Earl Beamer Heat exchanger assembly
US7779898B2 (en) * 2006-04-14 2010-08-24 Baltimore Aircoil Company, Inc. Heat transfer tube assembly with serpentine circuits
US7895860B2 (en) * 2006-11-22 2011-03-01 Johnson Controls Technology Company Multichannel evaporator with flow mixing manifold
US7921558B2 (en) * 2008-01-09 2011-04-12 Delphi Technologies, Inc. Non-cylindrical refrigerant conduit and method of making same

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Publication number Priority date Publication date Assignee Title
US4683101A (en) * 1985-12-26 1987-07-28 Baltimore Aircoil Company, Inc. Cross flow evaporative coil fluid cooling apparatus and method of cooling
US5203407A (en) * 1990-11-07 1993-04-20 Zexel Corporation Vehicle-loaded parallel flow type heat exchanger
US5435382A (en) * 1993-06-16 1995-07-25 Baltimore Aircoil Company, Inc. Combination direct and indirect closed circuit evaporative heat exchanger
US6142219A (en) * 1999-03-08 2000-11-07 Amstead Industries Incorporated Closed circuit heat exchange system and method with reduced water consumption
US6820685B1 (en) * 2004-02-26 2004-11-23 Baltimore Aircoil Company, Inc. Densified heat transfer tube bundle
US7275394B2 (en) * 2005-04-22 2007-10-02 Visteon Global Technologies, Inc. Heat exchanger having a distributer plate
US7779898B2 (en) * 2006-04-14 2010-08-24 Baltimore Aircoil Company, Inc. Heat transfer tube assembly with serpentine circuits
US20080023185A1 (en) * 2006-07-25 2008-01-31 Henry Earl Beamer Heat exchanger assembly
US7895860B2 (en) * 2006-11-22 2011-03-01 Johnson Controls Technology Company Multichannel evaporator with flow mixing manifold
US7921558B2 (en) * 2008-01-09 2011-04-12 Delphi Technologies, Inc. Non-cylindrical refrigerant conduit and method of making same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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CN105020925A (en) * 2015-08-18 2015-11-04 重庆达孚制冷设备有限责任公司 Integrated cold/hot water unit adopting evaporative condenser
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