Abstract: A method of liquid delivery in an evaporative cooler having an assembly of plates may include delivering liquid from a fill tube to a first trough formed on a first plate of the assembly of plates, the first trough including a first perforation in fluid communication with a second trough formed on a second plate of the assembly of plates, the fill tube configured to deliver the liquid above the first perforation such that an exit point of the fill tube is not submerged in liquid at any point during liquid delivery or operation of the evaporative cooler, draining the liquid from the first trough to the second trough via the first perforation, and filling the second trough to an overflow level before permitting the liquid to exit the second trough via a second perforation, the overflow level defined by a bottom of the second perforation.

Abstract: A direct evaporative cooler includes a liquid delivery system and an assembly of two or more plates. At least one plate of the assembly of two or more plates may include a top surface having a wicking material with an exposed surface for receiving a liquid thereon from the liquid delivery system, and one or more masks lining a portion of the exposed surface. The one or more masks may be impermeable to the liquid thereby preventing the liquid from evaporating through the one or more masks, and the one or more masks may be sized and shaped such that a wick rate of the liquid on the exposed surface exceeds an evaporation rate of the liquid.

Abstract: A method of liquid delivery in an evaporative cooler having an assembly of plates may include delivering liquid from a fill tube to a first trough formed on a first plate of the assembly of plates, the first trough including a first perforation in fluid communication with a second trough formed on a second plate of the assembly of plates, the fill tube configured to deliver the liquid above the first perforation such that an exit point of the fill tube is not submerged in liquid at any point during liquid delivery or operation of the evaporative cooler, draining the liquid from the first trough to the second trough via the first perforation, and filling the second trough to an overflow level before permitting the liquid to exit the second trough via a second perforation, the overflow level defined by a bottom of the second perforation.

Abstract: In one embodiment, an evaporative cooler is described. The evaporative cooler may comprise an assembly of one or more plates. At least one trough proximate the one or more plates. A water delivery system may be proximate the at least one trough. The water delivery system may comprise at least one supply tube and at least one fill tube, wherein the water delivery system is positioned to siphon air from the evaporative cooler when a continuous water supply is suspended.

Abstract: A direct evaporative cooler includes a liquid delivery system and an assembly of two or more plates. At least one plate of the assembly of two or more plates may include a top surface having a wicking material with an exposed surface for receiving a liquid thereon from the liquid delivery system, and one or more masks lining a portion of the exposed surface. The one or more masks may be impermeable to the liquid thereby preventing the liquid from evaporating through the one or more masks, and the one or more masks may be sized and shaped such that a wick rate of the liquid on the exposed surface exceeds an evaporation rate of the liquid.

Abstract: In one embodiment, a plate for an evaporative cooler is disclosed. The plate may comprise a wicking material with an exposed surface and a sealed surface opposite the exposed surface. An impermeable barrier may be coupled to the sealed surface. One or more masks may line a portion of the exposed surface, wherein the masks may comprise an impermeable material. In some embodiments, the mask may be a strip of impermeable material and may be coupled to a flat area of the top surface. In further embodiments, the one or more masks may align with a liquid wick path of the wicking material. In further embodiments, the one or more masks may line the edge of perforations that pass at least partially through the plate.

Abstract: In one embodiment, an evaporative cooler is described. The evaporative cooler may comprise an assembly of one or more plates. At least one trough proximate the one or more plates. A water delivery system may be proximate the at least one trough. The water delivery system may comprise at least one supply tube and at least one fill tube, wherein the water delivery system is positioned to siphon air from the evaporative cooler when a continuous water supply is suspended.

Abstract: In one embodiment, a plate for an evaporative cooler is disclosed. The plate may comprise a wicking material with an exposed surface and a sealed surface opposite the exposed surface. An impermeable barrier may be coupled to the sealed surface. One or more masks may line a portion of the exposed surface, wherein the masks may comprise an impermeable material. In some embodiments, the mask may be a strip of impermeable material and may be coupled to a flat area of the top surface. In further embodiments, the one or more masks may align with a liquid wick path of the wicking material. In further embodiments, the one or more masks may line the edge of perforations that pass at least partially through the plate.

Abstract: Heat exchanger plates for indirect evaporative coolers, of the type having a dry side having low permeability to an evaporative liquid and formed to allow a product fluid to flow over a heat transfer area of its surface, a wet side designed to have its surface wet by an evaporative liquid, and formed to allow a working gas to flow over its surface to evaporate the evaporative liquid, further include edge extensions formed beyond the heat exchange area of the plates to facilitate removal of excess evaporative liquid. The edge extensions may slant or curve away from the wet side of the plates to assist in liquid removal. The plates may be used in a variety of configurations.

Abstract: The present invention relates to methods for indirect evaporative air-cooling with the use of plates, heat exchangers and feeder wicks—of the indirect evaporative type. Several components for an indirect evaporative heat exchanger described as follows: A plate for an indirect evaporative heat exchanger where the plate is made of laminate material having one sheet of wicking material for wet zone(s) and the other of a water proof plastic material for the dry zone(s). An evaporative heat exchanger is created by assembling the plates forming spacing for wet channels, (they are created by the wet zone of the plates,) and dry channels, (they are created by the dry zone of the plates,) with channel guides or corrugated plates. The spacing between the plates is defined to reduce pressure drop for increased airflow. A feeder wick system creates the wetting of the wet channels without excess water.

Abstract: An indirect evaporative cooler includes a number of heat transfer plates. Each plate has a wet side and a dry side, and the dry sides of adjacent plates face each other. The plate dry sides have low permeability to an evaporative liquid. Input air flows over the dry sides from an input end to an output end. Part of the input air becomes product air and exits at the output end. The rest of the input air passes through perforations in the plates to the other side of the plates to become working air. The other side of each plate is a wet side, which is wet by an evaporative liquid. Working gas flows over the wet side, evaporating the evaporative liquid and cooling the evaporative liquid, the plate, and finally the product gas by heat transfer. The perforations are formed both toward the input end of the plate and toward the output end of the plate.

Abstract: A duplex exchanger includes first and second heat exchangers each including a main flow channel and a cooperating counterheat channel. The first counterheat channel is joined to the first main flow channel for receiving a cooled primary stream therefrom. The second counterheat channel is also joined to the first main channel splitting the primary stream therefrom. An evaporative coolant is injected into the first counterheat channel, and an evaporative saturant is injected into the second counterheat channel. Heat from the initially hot primary stream in the first exchanger evaporates the coolant in the first counterheat channel for self-cooling the primary stream in the first main channel. Heat from a hot secondary stream channeled through the second main channel evaporates the saturant in the second counterheat channel for adding mass to the primary stream channeled therethrough.