US20140096555A1 - Plate evaporative condenser and cooler - Google Patents
Plate evaporative condenser and cooler Download PDFInfo
- Publication number
- US20140096555A1 US20140096555A1 US13/648,607 US201213648607A US2014096555A1 US 20140096555 A1 US20140096555 A1 US 20140096555A1 US 201213648607 A US201213648607 A US 201213648607A US 2014096555 A1 US2014096555 A1 US 2014096555A1
- Authority
- US
- United States
- Prior art keywords
- edge
- line
- channel
- channels
- evaporative condenser
- 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
- 230000007423 decrease Effects 0.000 claims abstract description 7
- 239000012530 fluid Substances 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 238000003466 welding Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910000746 Structural steel Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
Images
Classifications
-
- 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
- F25B39/04—Condensers
-
- 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
- F28D1/00—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, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—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, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/03—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, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
- F28D1/0308—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, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
- F28D1/035—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, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other with U-flow or serpentine-flow inside the conduits
-
- 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
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
- F28F3/044—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being pontual, e.g. dimples
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/12—Elements constructed in the shape of a hollow panel, e.g. with channels
-
- 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
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/041—Details of condensers of evaporative condensers
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0061—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
- F28D2021/0066—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications with combined condensation and evaporation
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/007—Condensers
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 the coils and condensed or liquid ammonia flows out.
- An evaporative condenser comprises a condenser unit and a water sprayer located above the condenser unit.
- a fill section is located below the condenser unit.
- a basin is located below the fill section.
- At least one fan flows air through the condenser unit and the fill section.
- the condenser unit comprises plural plate units separated from one another by air gaps.
- Each plate unit comprises first and second plates coupled together about a perimeter thereof.
- Each plate unit has a first edge and an opposite second edge.
- Each plate unit has an inlet and an outlet.
- the first and second plates are coupled together along at least one line so as to form a first channel that extends from the first edge to the second edge and a second channel that communicates with the first channel and extends back to the first edge.
- the first and second plates are coupled together at spots located in the channel.
- the first channel extends from the inlet.
- a third channel extends to the outlet.
- the first channel has a larger volume than the third channel.
- the intermediate channel has a smaller volume than the first channel and a larger volume than the third channel.
- the at least one line extends from the first edge toward the second edge.
- the first channel is bounded by the one line and an outside edge.
- a second line extends from the second edge toward the first edge.
- the second channel is bounded by the one line and the second line.
- the one line and the second line are discontinuous.
- the one line has gaps that decrease in size from the first edge to the second edge and the second line has gaps that decrease in size from the second edge to the first edge.
- the one line has gaps of equal size and the second line has gaps of equal size.
- the gaps of the second line are misaligned with the gaps of the one line in a direction perpendicular to the first and second edges.
- the first channel extends from the inlet.
- a third channel extends to the outlet.
- the third channel has a third line that extends from one of the first or second edges to the other of the first or second edges.
- the one line has a first gap for the second edge.
- the third line has a third gap with the other of the first or second edges. The first gap is larger than the third gap.
- the one line is continuous.
- the one line is discontinuous.
- the plates in each plate unit are coupled together at spots located in the first and second channels.
- the spots are arranged in a triangular pattern.
- the triangular pattern has triangles with bases that are parallel to the flow of fluid through the first and second channels.
- the plates in each plate unit are coupled together at spots located in the first and second channels.
- the spots are arranged in a triangular pattern.
- the triangular pattern has triangles with bases that are perpendicular to the flow of fluid through the first and second channels.
- the plates in each plate unit are coupled together at spots located in the first and second channels.
- the spots are arranged in a rectangular pattern.
- the rectangular pattern has a side that is parallel to the fluid flow through the first and second channels.
- the plates in each plate unit are coupled together at spots located in the first and second channels.
- the spots are arranged in a rectangular pattern.
- the rectangular pattern has a side that is angled 15 to 60 degrees to fluid flow through the first and second channels.
- each of the plate units has sides.
- the plate units are oriented with respect to each other along adjacent sides.
- Frames extend across the plate units and are coupled thereto.
- FIG. 1 is a schematic view of an evaporative condenser.
- FIG. 2 is a side view of a plate unit, in accordance with one embodiment.
- FIG. 3 is a cross-sectional view of the plate unit, taken along lines III-III of FIG. 2 .
- FIG. 4 is a side view of a plate unit, in accordance with another embodiment.
- FIG. 5 is a side view of a plate unit, in accordance with another embodiment.
- FIG. 6 is a side view of a plate unit, in accordance with another embodiment.
- FIG. 7 is an end view of the plate assembly.
- FIG. 8 is a side view of a plate unit, in accordance with another embodiment.
- FIG. 9 is a side view of a plate unit, in accordance with another embodiment.
- FIGS. 9A and 9B are side views of a plate unit, in accordance with other embodiments.
- FIG. 10 is a side view of a plate unit, in accordance with another embodiment.
- FIG. 11 is a side view of a plate unit, in accordance with another embodiment.
- FIG. 1 shows an evaporative condenser 11 .
- Water is sprayed onto a plate assembly 13 which is a heat exchanger.
- a fan 15 draws air 17 through the wetted plate assembly 13 to provide evaporative cooling and condensing of a fluid inside of the plate assembly (typically from a gas into a liquid).
- the plate assembly 13 provides an efficient, cost effective condenser.
- the evaporative condenser 11 has a housing 19 .
- the plate assembly 13 is located in the housing.
- a fill or stuffing section 21 below the plate assembly 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 plate assembly section and the fill section.
- the fan 15 draws air through the plate assembly 13 , in through the fill section 21 , through demisters 27 or dehydrators, into the plenum 25 and out of the housing.
- the plate assembly 13 includes a number of plate units 31 vertically oriented and spaced apart from each other. Referring to FIGS. 2 and 3 , a plate unit 31 is shown. Each plate unit has two plates 33 , each of generally rectangular shape. Each plate 33 is metal, such as carbon steel or stainless steel. The plates are coupled together along their outside edges 35 A, 35 B, 35 C, 35 D, with edge or perimeter welds. Once coupled together, the plates form an interior cavity 37 . An inlet pipe 39 is provided at one corner of the plate unit. An outlet pipe 41 is provided at another corner of the plate unit. The inlet and outlet can be on the same side 35 A as shown in FIG. 2 , or in opposite corners. The inlet and outlet pipes 39 , 41 communicate with the interior cavity 37 .
- Channels 43 are formed in the interior cavity 37 by welding the plates together along inside locations.
- the fluid flows from the inlet pipe in the first edge 35 A, in one channel to the opposite, or second edge 35 C, and enters the adjacent channel where it flows back to the first edge 35 A and so on in a zig-zag manner to the outlet 41 .
- the channels are made by lines 45 of welding (in the example shown in FIG. 2 , there are weld lines 45 A, 45 B, 45 C, 45 D, 45 E, 45 F and 45 G).
- the channel receiving fluid from the inlet pipe 39 is bounded by the outside edge 35 D and a weld line 45 A extending from the first edge 35 A toward the second edge 35 C.
- the weld line 45 A stops short of the second edge 35 C leaving a gap 47 A to allow fluid to exit the inlet channel and enter the next channel.
- a second weld line 45 B extends from the second edge 35 C toward the first edge 35 A. This next channel is formed by the first and second weld lines 45 A, 45 B.
- the second weld line 45 B stops short of the first edge 35 A, leaving a gap.
- the channels 43 are formed by the weld lines 45 A- 45 G and the outside edges.
- the volumes of the individual channels 43 change from the inlet to the outlet. Because the plate unit operates as a condenser, the volumes of the channels are larger near the inlet 39 than near the outlet 41 .
- the height of the first two channels near the inlet (the channels bound by the edge 35 D and the weld line 45 A and the channel between weld lines 45 A, 45 B), is A, with the height of the next few channels (bounded by weld lines 45 B and 45 C; 45 C and 45 D; 45 D and 45 E; and 45 E and 45 F) is B, where A>B.
- the height of the channels nearest the outlet is C, where B>C. Because the lengths of the channels are equal (from edge 35 A to edge 35 C), the distance between the weld lines determines the channel volumes. Alternatively, the cross-sectional areas of the channels decrease from the inlet 39 to the outlet 41 where the cross-section is perpendicular to the general flow of fluid in the channels.
- gaps 47 at the ends of the weld lines, leading from one channel to the next, change size, diminishing from the inlet to the outlet.
- the first two gaps 47 A nearest the inlet are larger than the next few gaps 47 B.
- the gap or gaps 47 C nearest the outlet is the smallest, with 47 A> 47 B> 47 C.
- the plate unit operates as a cooler instead of a condenser, the flow through the plate unit is reversed, from the smaller channels to the larger channels to accommodate the expansion fluid. If no phase change occurs in the plate unit, then the channels will be of equal dimensions.
- spot welding 49 is used in or along the channels.
- the spot welds enhance heat transfer by creating elliptical cross-sections of the channels (see FIG. 3 ).
- Elliptical cross-sections of the channels are more efficient at heat transfer than are circular cross-sections.
- Fluid in the channels flow generally from one edge 35 A to the opposite edge 35 C and back, and parallel to the weld lines 45 .
- Spot welding contributes to turbulent flow of fluid in the channels. As the fluid flows in the channels, a spot weld 49 diverts flow around the weld. Such turbulent flow enhances heat transfer.
- the spot welds 49 can be arranged in pattern or configuration.
- spot welds are arranged in a triangular pattern, with each spot weld forming an apex of an equilateral triangle.
- dashed lines between spot welds 49 indicate the pattern).
- the triangles have bases 51 that are parallel to the general fluid flow in the channels.
- FIG. 4 illustrates a spot weld pattern where the triangles are rotated 90 degrees so that the triangle bases 51 are perpendicular to the general fluid flow in the channels.
- the pattern of FIG. 4 presents a different aspect of the triangles of fluid flowing in the channels around the spot welds than the pattern of FIG. 2 .
- FIG. 5 illustrates a spot weld pattern in a rectangular arrangement.
- the sides 53 of the rectangles are parallel to the edges 35 ( 35 C, 35 D) of the plate unit.
- FIG. 6 illustrates a rectangular spot weld pattern rotated from that of FIG. 5 .
- FIG. 6 shows the sides 53 oriented at 45 degrees relative to the weld lines 45 .
- the sides 53 could be oriented 15 to 60 degrees.
- the distance between spot welds 49 can be varied according to the design.
- the spot welds can be spaced apart a constant distance.
- the spot welds can be located closer together in the channels nearest the outlet than in the channels nearest the inlet.
- the plates are positioned together with little volume in the interior cavity. Pressurized air is introduced into the interior cavity through the inlet or outlet. This causes the unwelded portions of the plates to expand outward as shown in FIG. 3 .
- the individual plate units 31 are assembled together into the plate assembly 13 .
- the plate units are parallel to each other and separated from the adjacent plate units by gaps for air circulation.
- Frames 55 extend across the edges of plate units 31 to join them together (see FIG. 7 ).
- the frames 55 contact the outside edges 35 of the plate units 31 .
- the frames can be angle iron.
- each frame can have notches 57 therein for receiving an edge of a plate unit.
- the plate units may be welded to the frames.
- the inlet pipes and outlet pipes are coupled to respective headers 59 (see FIG. 1 ).
- the plate assembly 13 is mounted in the housing 19 .
- water is sprayed from spray heads 61 onto the plate units 13 .
- the water moves down the plate units. Air is drawn across the plate units by the fan 15 . Fluid in the plate units enters the inlets as a gas and leaves the outlets as a liquid.
- the water now hot, falls onto the fill section 21 , where it is cooled by air flowing across the fill section.
- the water then falls into the basin 23 , where a pump 63 returns it to the spray head 65 .
- a float switch 65 controls the pump.
- FIG. 8 illustrates another embodiment of the plate unit 31 .
- the plate units of FIGS. 8-10 are designed to handle an excess amount of gas.
- the weld lines 45 dividing the channels 43 are continuous.
- the weld lines 71 are discontinuous for those weld lines located closest to the inlet 39 .
- Gaps 73 are provided in the weld lines 71 , wherein fluid can flow through the gaps 73 from one channel to the next. As the weld lines extend from the first edge 35 A, there is a gap a, then gap b, gap c and gap d between the end of the weld line and the second edge 35 C.
- next weld line extends from the second edge 35 C and has a gap a, then gap b, gap c and gap d.
- Subsequent weld lines 45 can be solid because the volume of gas diminishes.
- FIG. 9 shows another embodiment of the plate unit 31 where the first two weld lines 71 have gaps 73 of uniform dimension.
- the gaps in the second weld line are vertically staggered (referring to the orientation shown in the drawing) from the gaps of the first weld line.
- Subsequent weld lines 45 are solid.
- FIG. 9A shows an alternate embodiment to FIG. 9 .
- the embodiment of FIG. 9A has the first two weld lines 71 with gaps 73 but lacks subsequent solid weld lines.
- FIG. 9B shows another embodiment which has a single weld line 71 with gaps 73 but no subsequent weld lines.
- FIG. 10 shows another embodiment of the plate unit 31 where the first weld line 71 is discontinuous and nonparallel to the other weld lines.
- the weld line extends from the first edge 35 A toward the second edge 35 C and inclines upward toward the upper edge 35 D so as to reduce the volume of the inlet channel at the second edge.
- the gaps 73 can be of the same size or decreasing in size: a>b>c>d>e.
- Subsequent weld lines 45 are continuous and parallel.
- FIG. 11 shows another embodiment of the plate unit 31 .
- a series of weld lines 71 is provided near the upper edge 35 D.
- the weld lines 71 are separated by gaps 73 .
- the weld lines have first and second ends 81 , 83 .
- the first ends 81 are progressively closer to the upper edge 35 D for those weld lines 81 that are closer to the second edge 35 B than to the first edge 35 A.
- the second ends 83 are progressively closer to the upper edge 35 D for those weld lines 81 that are closer to the second edge 35 B.
- the second ends 83 are closer to the upper edge 35 D than are the first ends 81 .
- the condenser component can be made inexpensively since the plate units are simply welded around the perimeter edges and then the interior so as to form channels and also spot welding to increase the turbulence of flow of fluid inside the plate units.
- the plate units 31 are then assembled together into a plate assembly 13 in an inexpensive manner.
- the plate assembly provides an efficient heat exchanger as the exterior of the plate units has large surface areas for being wetted with the water spray, while the interior provides elliptically shaped channels to increase the surface area with the fluid inside.
- the spot welding provides turbulence for fluid flow.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
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 the coils and condensed or liquid ammonia flows out.
- It is desirable to make improvements over the conventional coil condenser.
- An evaporative condenser comprises a condenser unit and a water sprayer located above the condenser unit. A fill section is located below the condenser unit. A basin is located below the fill section. At least one fan flows air through the condenser unit and the fill section. The condenser unit comprises plural plate units separated from one another by air gaps. Each plate unit comprises first and second plates coupled together about a perimeter thereof. Each plate unit has a first edge and an opposite second edge. Each plate unit has an inlet and an outlet. The first and second plates are coupled together along at least one line so as to form a first channel that extends from the first edge to the second edge and a second channel that communicates with the first channel and extends back to the first edge. The first and second plates are coupled together at spots located in the channel.
- In accordance with one aspect, the first channel extends from the inlet. A third channel extends to the outlet. The first channel has a larger volume than the third channel.
- In accordance with another aspect, there is an intermediate channel between the first and third channels. The intermediate channel has a smaller volume than the first channel and a larger volume than the third channel.
- In accordance with another aspect, the at least one line extends from the first edge toward the second edge. The first channel is bounded by the one line and an outside edge. A second line extends from the second edge toward the first edge. The second channel is bounded by the one line and the second line.
- In accordance with another aspect, the one line and the second line are discontinuous.
- In accordance with still another aspect, the one line has gaps that decrease in size from the first edge to the second edge and the second line has gaps that decrease in size from the second edge to the first edge.
- In accordance with another aspect, the one line has gaps of equal size and the second line has gaps of equal size. The gaps of the second line are misaligned with the gaps of the one line in a direction perpendicular to the first and second edges.
- In accordance with another aspect, the first channel extends from the inlet. A third channel extends to the outlet. The third channel has a third line that extends from one of the first or second edges to the other of the first or second edges. The one line has a first gap for the second edge. The third line has a third gap with the other of the first or second edges. The first gap is larger than the third gap.
- In accordance with another aspect, the one line is continuous.
- In accordance with another aspect, the one line is discontinuous.
- In accordance with another aspect, the plates in each plate unit are coupled together at spots located in the first and second channels. The spots are arranged in a triangular pattern. The triangular pattern has triangles with bases that are parallel to the flow of fluid through the first and second channels.
- In accordance with another aspect, the plates in each plate unit are coupled together at spots located in the first and second channels. The spots are arranged in a triangular pattern. The triangular pattern has triangles with bases that are perpendicular to the flow of fluid through the first and second channels.
- In accordance with another aspect, the plates in each plate unit are coupled together at spots located in the first and second channels. The spots are arranged in a rectangular pattern. The rectangular pattern has a side that is parallel to the fluid flow through the first and second channels.
- In accordance with another aspect, the plates in each plate unit are coupled together at spots located in the first and second channels. The spots are arranged in a rectangular pattern. The rectangular pattern has a side that is angled 15 to 60 degrees to fluid flow through the first and second channels.
- In accordance with another aspect, each of the plate units has sides. The plate units are oriented with respect to each other along adjacent sides. Frames extend across the plate units and are coupled thereto.
-
FIG. 1 is a schematic view of an evaporative condenser. -
FIG. 2 is a side view of a plate unit, in accordance with one embodiment. -
FIG. 3 is a cross-sectional view of the plate unit, taken along lines III-III ofFIG. 2 . -
FIG. 4 is a side view of a plate unit, in accordance with another embodiment. -
FIG. 5 is a side view of a plate unit, in accordance with another embodiment. -
FIG. 6 is a side view of a plate unit, in accordance with another embodiment. -
FIG. 7 is an end view of the plate assembly. -
FIG. 8 is a side view of a plate unit, in accordance with another embodiment. -
FIG. 9 is a side view of a plate unit, in accordance with another embodiment. -
FIGS. 9A and 9B are side views of a plate unit, in accordance with other embodiments. -
FIG. 10 is a side view of a plate unit, in accordance with another embodiment. -
FIG. 11 is a side view of a plate unit, in accordance with another embodiment. -
FIG. 1 shows anevaporative condenser 11. Water is sprayed onto aplate assembly 13 which is a heat exchanger. A fan 15 draws air 17 through the wettedplate assembly 13 to provide evaporative cooling and condensing of a fluid inside of the plate assembly (typically from a gas into a liquid). Theplate assembly 13 provides an efficient, cost effective condenser. - The various components of the
evaporative condenser 11 will now be described. Theevaporative condenser 11 has ahousing 19. Theplate assembly 13 is located in the housing. Below the plate assembly 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 plate assembly section and the fill section. The fan 15 draws air through theplate assembly 13, in through thefill section 21, throughdemisters 27 or dehydrators, into theplenum 25 and out of the housing. - The
plate assembly 13 includes a number ofplate units 31 vertically oriented and spaced apart from each other. Referring toFIGS. 2 and 3 , aplate unit 31 is shown. Each plate unit has twoplates 33, each of generally rectangular shape. Eachplate 33 is metal, such as carbon steel or stainless steel. The plates are coupled together along theiroutside edges interior cavity 37. Aninlet pipe 39 is provided at one corner of the plate unit. Anoutlet pipe 41 is provided at another corner of the plate unit. The inlet and outlet can be on thesame side 35A as shown inFIG. 2 , or in opposite corners. The inlet andoutlet pipes interior cavity 37. -
Channels 43 are formed in theinterior cavity 37 by welding the plates together along inside locations. In the embodiment shown inFIG. 2 , the fluid flows from the inlet pipe in thefirst edge 35A, in one channel to the opposite, orsecond edge 35C, and enters the adjacent channel where it flows back to thefirst edge 35A and so on in a zig-zag manner to theoutlet 41. The channels are made bylines 45 of welding (in the example shown inFIG. 2 , there areweld lines inlet pipe 39 is bounded by theoutside edge 35D and aweld line 45A extending from thefirst edge 35A toward thesecond edge 35C. Theweld line 45A stops short of thesecond edge 35C leaving agap 47A to allow fluid to exit the inlet channel and enter the next channel. Asecond weld line 45B extends from thesecond edge 35C toward thefirst edge 35A. This next channel is formed by the first and second weld lines 45A, 45B. Thesecond weld line 45B stops short of thefirst edge 35A, leaving a gap. - Thus, the
channels 43 are formed by the weld lines 45A-45G and the outside edges. - The volumes of the
individual channels 43 change from the inlet to the outlet. Because the plate unit operates as a condenser, the volumes of the channels are larger near theinlet 39 than near theoutlet 41. For example, and referring to the orientation ofFIG. 2 , the height of the first two channels near the inlet (the channels bound by theedge 35D and theweld line 45A and the channel betweenweld lines weld lines weld lines edge 35B) is C, where B>C. Because the lengths of the channels are equal (fromedge 35A to edge 35C), the distance between the weld lines determines the channel volumes. Alternatively, the cross-sectional areas of the channels decrease from theinlet 39 to theoutlet 41 where the cross-section is perpendicular to the general flow of fluid in the channels. - Likewise, the gaps 47 at the ends of the weld lines, leading from one channel to the next, change size, diminishing from the inlet to the outlet. The first two
gaps 47A nearest the inlet are larger than the nextfew gaps 47B. The gap orgaps 47C nearest the outlet is the smallest, with 47A>47B>47C. - If the plate unit operates as a cooler instead of a condenser, the flow through the plate unit is reversed, from the smaller channels to the larger channels to accommodate the expansion fluid. If no phase change occurs in the plate unit, then the channels will be of equal dimensions.
- In addition to the weld lines 45,
spot welding 49 is used in or along the channels. The spot welds enhance heat transfer by creating elliptical cross-sections of the channels (seeFIG. 3 ). Elliptical cross-sections of the channels are more efficient at heat transfer than are circular cross-sections. - Fluid in the channels flow generally from one
edge 35A to theopposite edge 35C and back, and parallel to the weld lines 45. Spot welding contributes to turbulent flow of fluid in the channels. As the fluid flows in the channels, aspot weld 49 diverts flow around the weld. Such turbulent flow enhances heat transfer. - The spot welds 49 can be arranged in pattern or configuration. In
FIG. 2 , spot welds are arranged in a triangular pattern, with each spot weld forming an apex of an equilateral triangle. (InFIGS. 2 , 4-6, dashed lines betweenspot welds 49 indicate the pattern). The triangles havebases 51 that are parallel to the general fluid flow in the channels.FIG. 4 illustrates a spot weld pattern where the triangles are rotated 90 degrees so that the triangle bases 51 are perpendicular to the general fluid flow in the channels. The pattern ofFIG. 4 presents a different aspect of the triangles of fluid flowing in the channels around the spot welds than the pattern ofFIG. 2 . -
FIG. 5 illustrates a spot weld pattern in a rectangular arrangement. Thesides 53 of the rectangles are parallel to the edges 35 (35C, 35D) of the plate unit.FIG. 6 illustrates a rectangular spot weld pattern rotated from that ofFIG. 5 .FIG. 6 shows thesides 53 oriented at 45 degrees relative to the weld lines 45. However, thesides 53 could be oriented 15 to 60 degrees. - The distance between
spot welds 49 can be varied according to the design. The spot welds can be spaced apart a constant distance. Alternatively, the spot welds can be located closer together in the channels nearest the outlet than in the channels nearest the inlet. - After the plate unit has been welded, the plates are positioned together with little volume in the interior cavity. Pressurized air is introduced into the interior cavity through the inlet or outlet. This causes the unwelded portions of the plates to expand outward as shown in
FIG. 3 . - The
individual plate units 31 are assembled together into theplate assembly 13. The plate units are parallel to each other and separated from the adjacent plate units by gaps for air circulation.Frames 55 extend across the edges ofplate units 31 to join them together (seeFIG. 7 ). Theframes 55 contact theoutside edges 35 of theplate units 31. The frames can be angle iron. Alternatively, each frame can havenotches 57 therein for receiving an edge of a plate unit. The plate units may be welded to the frames. The inlet pipes and outlet pipes are coupled to respective headers 59 (seeFIG. 1 ). Theplate assembly 13 is mounted in thehousing 19. - In operation, referring back to
FIG. 1 , water is sprayed from spray heads 61 onto theplate units 13. The water moves down the plate units. Air is drawn across the plate units by the fan 15. Fluid in the plate units enters the inlets as a gas and leaves the outlets as a liquid. The water, now hot, falls onto thefill section 21, where it is cooled by air flowing across the fill section. The water then falls into thebasin 23, where apump 63 returns it to thespray head 65. Afloat switch 65 controls the pump. -
FIG. 8 illustrates another embodiment of theplate unit 31. The plate units ofFIGS. 8-10 are designed to handle an excess amount of gas. InFIG. 2 , the weld lines 45 dividing thechannels 43 are continuous. InFIG. 8 , the weld lines 71 are discontinuous for those weld lines located closest to theinlet 39.Gaps 73 are provided in the weld lines 71, wherein fluid can flow through thegaps 73 from one channel to the next. As the weld lines extend from thefirst edge 35A, there is a gap a, then gap b, gap c and gap d between the end of the weld line and thesecond edge 35C. The next weld line extends from thesecond edge 35C and has a gap a, then gap b, gap c and gap d. For the gaps, a>b>c>d.Subsequent weld lines 45 can be solid because the volume of gas diminishes. -
FIG. 9 shows another embodiment of theplate unit 31 where the first twoweld lines 71 havegaps 73 of uniform dimension. The gaps in the second weld line are vertically staggered (referring to the orientation shown in the drawing) from the gaps of the first weld line.Subsequent weld lines 45 are solid. -
FIG. 9A shows an alternate embodiment toFIG. 9 . The embodiment ofFIG. 9A has the first twoweld lines 71 withgaps 73 but lacks subsequent solid weld lines.FIG. 9B shows another embodiment which has asingle weld line 71 withgaps 73 but no subsequent weld lines. -
FIG. 10 shows another embodiment of theplate unit 31 where thefirst weld line 71 is discontinuous and nonparallel to the other weld lines. The weld line extends from thefirst edge 35A toward thesecond edge 35C and inclines upward toward theupper edge 35D so as to reduce the volume of the inlet channel at the second edge. Thegaps 73 can be of the same size or decreasing in size: a>b>c>d>e.Subsequent weld lines 45 are continuous and parallel. -
FIG. 11 shows another embodiment of theplate unit 31. A series ofweld lines 71 is provided near theupper edge 35D. The weld lines 71 are separated bygaps 73. The weld lines have first and second ends 81, 83. The first ends 81 are progressively closer to theupper edge 35D for thoseweld lines 81 that are closer to thesecond edge 35B than to thefirst edge 35A. Likewise, the second ends 83 are progressively closer to theupper edge 35D for thoseweld lines 81 that are closer to thesecond edge 35B. Also the second ends 83 are closer to theupper edge 35D than are the first ends 81. - Thus, by providing
plate units 31 for the condenser, the condenser component can be made inexpensively since the plate units are simply welded around the perimeter edges and then the interior so as to form channels and also spot welding to increase the turbulence of flow of fluid inside the plate units. Theplate units 31 are then assembled together into aplate assembly 13 in an inexpensive manner. - The plate assembly provides an efficient heat exchanger as the exterior of the plate units has large surface areas for being wetted with the water spray, while the interior provides elliptically shaped channels to increase the surface area with the fluid inside. In addition, the spot welding provides turbulence for fluid flow.
- 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 (15)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/648,607 US20140096555A1 (en) | 2012-10-10 | 2012-10-10 | Plate evaporative condenser and cooler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/648,607 US20140096555A1 (en) | 2012-10-10 | 2012-10-10 | Plate evaporative condenser and cooler |
Publications (1)
Publication Number | Publication Date |
---|---|
US20140096555A1 true US20140096555A1 (en) | 2014-04-10 |
Family
ID=50431665
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US13/648,607 Abandoned US20140096555A1 (en) | 2012-10-10 | 2012-10-10 | Plate evaporative condenser and cooler |
Country Status (1)
Country | Link |
---|---|
US (1) | US20140096555A1 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9004463B2 (en) | 2012-12-17 | 2015-04-14 | Baltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
US9057563B2 (en) | 2012-12-17 | 2015-06-16 | Baltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
US9057564B2 (en) | 2012-12-17 | 2015-06-16 | Baltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
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 |
WO2018018049A1 (en) * | 2016-07-22 | 2018-01-25 | Evapco, Inc. | Ultra narrow channel ultra low refrigerant charge evaporative condenser |
US20190041135A1 (en) * | 2015-09-18 | 2019-02-07 | Nopparat Thipchuwong | Double plated heat exchanger |
US10571197B2 (en) | 2016-10-12 | 2020-02-25 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger |
US10641554B2 (en) | 2016-10-12 | 2020-05-05 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger |
US10655918B2 (en) | 2016-10-12 | 2020-05-19 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger having circuit tubes with varying dimensions |
US11029093B2 (en) | 2017-03-30 | 2021-06-08 | Baltimore Aircoil Company, Inc. | Cooling tower with direct and indirect heat exchanger |
US20210404749A1 (en) * | 2020-06-30 | 2021-12-30 | Treau, Inc. | Multilayer sheets for heat exchangers |
US11781758B2 (en) | 2009-03-13 | 2023-10-10 | Treau, Inc. | Window-mounted climate control system and method |
US11885577B2 (en) | 2015-05-20 | 2024-01-30 | Other Lab, Llc | Heat exchanger array system and method for an air thermal conditioner |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3458917A (en) * | 1966-01-03 | 1969-08-05 | Mueller Co Paul | Method of fabricating metal sheets with fluid passages |
US4305456A (en) * | 1977-08-12 | 1981-12-15 | Paul Mueller Company | Condenser and hot water system |
US4574876A (en) * | 1981-05-11 | 1986-03-11 | Extracorporeal Medical Specialties, Inc. | Container with tapered walls for heating or cooling fluids |
US5167274A (en) * | 1988-08-26 | 1992-12-01 | Cominco Ltd. | Method and apparatus for cooling particulate solids |
US5860471A (en) * | 1994-05-13 | 1999-01-19 | Perryment; Alan John | Heat exchange device |
US20010032716A1 (en) * | 2000-03-09 | 2001-10-25 | Wolf-Dieter Consilius | Heat exchanger element |
US20040025864A1 (en) * | 2000-04-10 | 2004-02-12 | Edwin Aronds | Device for heating of liquids |
US7055583B2 (en) * | 2001-10-19 | 2006-06-06 | Methanol Casale S.A. | Heat exchange unit for isothermal chemical reactors |
US20080314574A1 (en) * | 2005-11-18 | 2008-12-25 | Methanol Casale S.A. | Method for the Production of a Plate Type Heat Exchanger and Related Heat Exchanger |
US20090183862A1 (en) * | 2004-01-12 | 2009-07-23 | Sylvain Benezech | Heat exchanger and related exchange module |
US20100189609A1 (en) * | 2007-07-19 | 2010-07-29 | Methanol Casale S.A. | Heat Exchange Unit for Isothermal Chemical Reactors |
-
2012
- 2012-10-10 US US13/648,607 patent/US20140096555A1/en not_active Abandoned
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3458917A (en) * | 1966-01-03 | 1969-08-05 | Mueller Co Paul | Method of fabricating metal sheets with fluid passages |
US4305456A (en) * | 1977-08-12 | 1981-12-15 | Paul Mueller Company | Condenser and hot water system |
US4574876A (en) * | 1981-05-11 | 1986-03-11 | Extracorporeal Medical Specialties, Inc. | Container with tapered walls for heating or cooling fluids |
US5167274A (en) * | 1988-08-26 | 1992-12-01 | Cominco Ltd. | Method and apparatus for cooling particulate solids |
US5860471A (en) * | 1994-05-13 | 1999-01-19 | Perryment; Alan John | Heat exchange device |
US20010032716A1 (en) * | 2000-03-09 | 2001-10-25 | Wolf-Dieter Consilius | Heat exchanger element |
US20040025864A1 (en) * | 2000-04-10 | 2004-02-12 | Edwin Aronds | Device for heating of liquids |
US7055583B2 (en) * | 2001-10-19 | 2006-06-06 | Methanol Casale S.A. | Heat exchange unit for isothermal chemical reactors |
US20090183862A1 (en) * | 2004-01-12 | 2009-07-23 | Sylvain Benezech | Heat exchanger and related exchange module |
US20080314574A1 (en) * | 2005-11-18 | 2008-12-25 | Methanol Casale S.A. | Method for the Production of a Plate Type Heat Exchanger and Related Heat Exchanger |
US20100189609A1 (en) * | 2007-07-19 | 2010-07-29 | Methanol Casale S.A. | Heat Exchange Unit for Isothermal Chemical Reactors |
US8404188B2 (en) * | 2007-07-19 | 2013-03-26 | Methanol Casale S.A. | Heat exchange unit for isothermal chemical reactors |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11781758B2 (en) | 2009-03-13 | 2023-10-10 | Treau, Inc. | Window-mounted climate control system and method |
US9057563B2 (en) | 2012-12-17 | 2015-06-16 | Baltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
US9057564B2 (en) | 2012-12-17 | 2015-06-16 | Baltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
JP2017172964A (en) * | 2012-12-17 | 2017-09-28 | バルチモア、エアコイル、カンパニー、インコーポレーテッドBaltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
US9004463B2 (en) | 2012-12-17 | 2015-04-14 | Baltimore Aircoil Company, Inc. | Cooling tower with indirect heat exchanger |
US11885577B2 (en) | 2015-05-20 | 2024-01-30 | Other Lab, Llc | Heat exchanger array system and method for an air thermal conditioner |
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 |
US20190041135A1 (en) * | 2015-09-18 | 2019-02-07 | Nopparat Thipchuwong | Double plated heat exchanger |
WO2018018049A1 (en) * | 2016-07-22 | 2018-01-25 | Evapco, Inc. | Ultra narrow channel ultra low refrigerant charge evaporative condenser |
US10641554B2 (en) | 2016-10-12 | 2020-05-05 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger |
US10655918B2 (en) | 2016-10-12 | 2020-05-19 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger having circuit tubes with varying dimensions |
US11644245B2 (en) | 2016-10-12 | 2023-05-09 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger having circuit tubes with varying dimensions |
US10571197B2 (en) | 2016-10-12 | 2020-02-25 | Baltimore Aircoil Company, Inc. | Indirect heat exchanger |
US11029093B2 (en) | 2017-03-30 | 2021-06-08 | Baltimore Aircoil Company, Inc. | Cooling tower with direct and indirect heat exchanger |
US20210404749A1 (en) * | 2020-06-30 | 2021-12-30 | Treau, Inc. | Multilayer sheets for heat exchangers |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20140096555A1 (en) | Plate evaporative condenser and cooler | |
KR101263559B1 (en) | heat exchanger | |
US20200300548A1 (en) | Evaporative heat exchange apparatus with finned elliptical tube coil assembly | |
US6973805B2 (en) | Layered heat exchanger, layered evaporator for motor vehicle air conditioners and refrigeration system | |
US20230184493A1 (en) | Plate heat exchanger with overlapping fins and tubes heat exchanger | |
US20190212075A1 (en) | Indirect heat exchanger | |
US3916644A (en) | Dehumidifier with a plate-type evaporator | |
JP2009156532A (en) | Heat exchanger | |
EP3875878B1 (en) | Heat exchanger and refrigeration cycle device | |
US6431264B2 (en) | Heat exchanger with fluid-phase change | |
CN104603243A (en) | Air-to-air atmospheric heat exchanger | |
US7073572B2 (en) | Flooded evaporator with various kinds of tubes | |
US6340052B1 (en) | Heat exchanger | |
JP2021500523A (en) | Flowing liquid film heat exchanger | |
JP3911604B2 (en) | Heat exchanger and refrigeration cycle | |
JP2001027484A (en) | Serpentine heat-exchanger | |
US20080184734A1 (en) | Flat Tube Single Serpentine Co2 Heat Exchanger | |
JP5338950B2 (en) | Heat exchanger | |
CN211147362U (en) | Heat exchange dewatering structure of compressed gas dryer | |
CN102062502B (en) | Flat-pipe heat exchanger structure and assembling table thereof | |
US20140165641A1 (en) | Distributor for evaporative condenser header or cooler header | |
CN104748592A (en) | Brazed heat exchanger with fluid flow and performing heat exchange by series connection with different refrigerant loops | |
JP2001133172A (en) | Heat exchanger and refrigeration air conditioner | |
WO2019198554A1 (en) | Shell-and-tube-type heat exchanger and spray method thereof | |
JPH1082594A (en) | Plate type heat exchanger and absorption cooling-heating apparatus using the same |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: AMERICAN SINO HEAT TRANSFER LLC, CHINA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:AYUB, ZAHID;PENG, PENG;SIGNING DATES FROM 20120830 TO 20120831;REEL/FRAME:029113/0104 |
|
AS | Assignment |
Owner name: AMERICAN SINO HEAT TRANSFER LLC, CHINA Free format text: CORRECTIVE ASSIGNMENT TO CORRECT THE PATENT APPLICATION NUMBER ON COVER SHEET PREVIOUSLY RECORDED ON REEL 029113 FRAME 0104. ASSIGNOR(S) HEREBY CONFIRMS THE CORRECTION OF APPLICATION NUMBER;ASSIGNORS:AYUB, ZAHID;PENG, PENG;SIGNING DATES FROM 20120830 TO 20120831;REEL/FRAME:029171/0173 |
|
AS | Assignment |
Owner name: AMSI HEAT TRANSFER LLC, CHINA Free format text: CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE INCORRECTLY IDENTIFED AS AMERICAN SINO HEAT TRANSFER LLC. CORRECT ASSIGNEE NAME IS AMSI HEAT TRANSFER LLC. PREVIOUSLY RECORDED ON REEL 029171 FRAME 0173. ASSIGNOR(S) HEREBY CONFIRMS THE CORRECTION OF THE ASSIGNEE NAME OF AMSI HEAT TRANSFER LLC;ASSIGNORS:AYUB, ZAHID;PENG, PENG;SIGNING DATES FROM 20130321 TO 20130906;REEL/FRAME:031220/0494 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |