US20140165641A1 - Distributor for evaporative condenser header or cooler header - Google Patents
Distributor for evaporative condenser header or cooler header Download PDFInfo
- 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
- Authority
- 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
Links
- 239000012530 fluid Substances 0.000 claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000007788 liquid Substances 0.000 description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/06—Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
- F28C3/08—Other 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/06—Condensers 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D5/00—Heat-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
- F28D5/02—Heat-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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/028—Header 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
- 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. 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.
- 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.
-
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 ofFIG. 2 , taken along lines III-III. -
FIGS. 3A andFIG. 3B are cross-sectional views of the header, similar toFIG. 3 , but of other embodiments. -
FIG. 4 is a view of a distributor.FIG. 5 shows the distributor in accordance with another embodiment. - 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 anevaporative condenser 11.Sprayers 61 spray water onto aheat exchanger 13. Afan 15 drawsair 17 through the wettedheat exchanger 13 to provide evaporative cooling and condensing of a fluid (typically from a gas into a liquid). - The
evaporative condenser 11 has ahousing 19. Theheat exchanger 13 is located in the housing. Below the heat exchanger is a fill orstuffing section 21. Thefill section 21 has layers that expose descending water to air flow. The layers can be made of plastic, etc. Below thefill section 21 is abasin 23 to catch the water. The housing also has aplenum 25 that communicates with the heat exchanger and the fill section. Thefan 15 draws air through theheat exchanger 13, in through thefill section 21, throughdemisters 27 or dehydrators, into theplenum 25 and out of the housing. - The
heat exchanger 13 hasheat exchange elements 31 that extend from aninlet header 33 to anoutlet header 35. In the preferred embodiment, theheat exchanger elements 31 are coils, however the heat exchange elements could be plates. Thus, there is a first set ofcoils 31A (seeFIG. 2 ), a second set ofcoils 31B, a third set ofcoils 31C and so on. Gas enters theinlet header 33 and then thecoils 31. Once in the coils, the gas condenses to a liquid. The liquid exits thecoils 31 into theoutlet header 35. - The
inlet header 33 has an inlet pipe 37 (seeFIG. 1 ) which delivers the gas to theinlet header 33. Likewise, theoutlet header 35 has anoutlet pipe 39, which removes the liquid from the outlet header. Referring toFIGS. 2 and 3 , the heat exchanger and inlet header are shown. In the preferred embodiment, theinlet header 33 is a pipe with aninterior cavity 41 that extends between two ends 43. The header can be circular in transverse cross-section, rectangular, etc. Theinlet pipe 37 and theheat exchange elements 31 all communicate with theinterior 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. Thecoils 31 are spaced out along the length of the header from one end to theother end 43. Consequently, some coils are located closer to theinlet pipe 37 than other coils. For example, centrally located coils 31A-31D are closer to the inlet pipe than are 31E, 31F, 31G, 31H.end coils - In order to evenly distribute the end feed fluid to all of the heat exchange coils, a
distributor 51 is provided in theinterior cavity 41 of theinlet header 33. As shown inFIGS. 3 and 4 , thedistributor 51 is a plate withperforations 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. Thedistributor 51 applies a back pressure to the gas in theinlet 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 thecoils 31. - To assemble the
inlet header 33, theinlet pipe 37 andfeed pipes 38 are connected to the header. With theinterior cavity 41 of the header exposed by way of anopen end 43, thedistributor 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 ofFIG. 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 thedistributor 51A, havingopenings 53A in the sites adjacent to theheader 33. - The
distributor plate 51 is located between theinlet pipe 37 and thecoils 31 so that gas flowing into the header passes through the distributor plate to flow into the coils. Thedistributor plate 51 can be positioned along a vertical chord, as shown by solid lines inFIG. 3 . The plate is positioned closer to the feed pipes than to theinlet pipe 37. Theplate 51 could be positioned closer to theinlet pipe 37, as shown by dashed lines inFIG. 3 . The plate could also be positioned through the center of the header instead of along a chord. -
FIG. 3 shows thedistributor plate 51 as flat. Thedistributor plate 51 need not be flat but can be curved.FIG. 3A shows the distributor plate as concave relative to theinlet 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 theinlet 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 thecoils 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/718,563 US20140165641A1 (en) | 2012-12-18 | 2012-12-18 | Distributor for evaporative condenser header or cooler header |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/718,563 US20140165641A1 (en) | 2012-12-18 | 2012-12-18 | Distributor for evaporative condenser header or cooler header |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20140165641A1 true US20140165641A1 (en) | 2014-06-19 |
Family
ID=50929353
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13/718,563 Abandoned US20140165641A1 (en) | 2012-12-18 | 2012-12-18 | Distributor for evaporative condenser header or cooler header |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US20140165641A1 (en) |
Cited By (3)
| 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 |
Citations (10)
| 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 |
| 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 |
-
2012
- 2012-12-18 US US13/718,563 patent/US20140165641A1/en not_active Abandoned
Patent Citations (10)
| 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)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| 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 |
| 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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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: AMSI HEAT TRANSFER LLC, CHINA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:AYUB, ZAHID;PENG, PENG;SIGNING DATES FROM 20130321 TO 20130906;REEL/FRAME:031221/0916 |
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| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |