US20130000329A1 - Method of wetting evaporative cooler media through a permeable layer - Google Patents
Method of wetting evaporative cooler media through a permeable layer Download PDFInfo
- Publication number
- US20130000329A1 US20130000329A1 US13/173,072 US201113173072A US2013000329A1 US 20130000329 A1 US20130000329 A1 US 20130000329A1 US 201113173072 A US201113173072 A US 201113173072A US 2013000329 A1 US2013000329 A1 US 2013000329A1
- Authority
- US
- United States
- Prior art keywords
- liquid coolant
- evaporative
- pad
- air
- evaporative pad
- 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
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/0035—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning using evaporation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F1/00—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
- F24F1/0007—Indoor units, e.g. fan coil units
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F1/00—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
- F24F1/0007—Indoor units, e.g. fan coil units
- F24F1/0071—Indoor units, e.g. fan coil units with means for purifying supplied air
-
- 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
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C1/04—Direct-contact trickle coolers, e.g. cooling towers with cross-current only
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/04—Distributing or accumulator troughs
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2220/00—Application
- F05D2220/70—Application in combination with
- F05D2220/76—Application in combination with an electrical generator
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F6/00—Air-humidification, e.g. cooling by humidification
- F24F6/02—Air-humidification, e.g. cooling by humidification by evaporation of water in the air
- F24F6/04—Air-humidification, e.g. cooling by humidification by evaporation of water in the air using stationary unheated wet elements
- F24F6/043—Air-humidification, e.g. cooling by humidification by evaporation of water in the air using stationary unheated wet elements with self-sucking action, e.g. wicks
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/54—Free-cooling systems
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
Definitions
- the present invention relates generally to a method and apparatus concerning the operation of evaporative cooling systems and, in particular, to a method and apparatus concerning the effective wetting by a liquid coolant of an evaporative pad of an evaporative cooling system that cools air supplied to a gas turbine system.
- Evaporative cooling systems or evaporative coolers as such systems are typically referred to, are employed in various ways in residential, commercial and industrial contexts.
- the evaporative coolers cool air that is directed through the evaporative coolers.
- the evaporative coolers cool the air through the evaporation of a coolant, typically water, which is brought into contact with the air at the evaporative coolers.
- an evaporative cooler typically includes an evaporative pad at which the air directed to the evaporative cooler is cooled.
- a coolant such as water for example, is caused to flow through the evaporative pad and air is brought into contact with the coolant at the pad, usually by means of a fan, blower or turbine drawing or forcing the air through the pad.
- the evaporative pad typically is constructed of a material that has a large surface area over which the coolant is dispersed so that the coolant assumes a large surface area at the evaporative pad, thereby facilitating the evaporation of the coolant at the pad.
- Heat transfer takes place between the air and the dispersed coolant, as the air comes into contact with the coolant at the evaporative pad, and the coolant thereby evaporated, causing the air to cool and the density of the air to increase. Coolant is continuously delivered to the evaporative pad to replace the coolant that evaporates.
- Evaporative coolers are known to be employed for the purpose of cooling the living spaces of residential structures and the working environments of commercial and industrial buildings for thermal comfort for example.
- evaporative coolers are known to be applied in industrial processes in which a supply of cooler and denser air can be used to advantage.
- an evaporative cooler can be employed in conjunction with a gas turbine system wherein the cooled air from the evaporative cooler is compressed and the compressed air mixed with a fuel such as natural gas for example. The mixture of air and fuel is combusted and the resulting expanding gases are directed to a turbine so as to drive the turbine that, in turn, drives an electrical generator for producing electrical power for example.
- the cooled air because of its increased density, provides a higher mass flow rate and pressure ratio at the gas turbine equipment, resulting in an increase in turbine output and efficiency.
- the foregoing benefit may not be fully realized in those instances in which the evaporative pad is not completely wetted by the coolant so that the air passing through the pad is cooled to a lesser extent than would be the case in which the pad is essentially entirely wetted by the coolant.
- the areas of the evaporative pad that are not wetted by the coolant can result in the establishment of temperatures in the air that passes through these non-wetted areas that are warmer than the temperatures in the air that has come into contact with the coolant in areas of the evaporative pad that have been wetted by the liquid coolant.
- These temperature differences in the respective air masses that are then directed to the turbine compressor can cause air turbulence that can result in damage to the turbine equipment. Even in the absence such damage, the vibration of the turbine blades can result in the deteriorated performance of the turbine equipment.
- the present invention provides an evaporative cooler that includes an evaporative pad including a liquid coolant-receiving surface at which a liquid coolant distributed to the evaporative pad is received and thereafter passes into the evaporative pad.
- the evaporative cooler also includes a liquid coolant distribution container that includes an upper portion configured to hold liquid coolant and a lower portion contiguous with the upper portion.
- the lower portion includes an opening and a permeable bed in place over the opening through which the liquid coolant held in the upper portion of the liquid coolant distribution container passes and is distributed to the liquid coolant-receiving surface of the evaporative pad.
- the present invention provides a method of cooling air.
- the method includes passing a liquid coolant into an evaporative pad.
- the pad includes a liquid coolant-receiving surface at which a liquid coolant distributed to the evaporative pad is received and thereafter passes into the evaporative pad.
- the evaporative pad is of an evaporative cooler and the passage of liquid coolant is from a liquid coolant distribution container.
- the liquid coolant distribution container includes an upper portion configured to hold liquid coolant and a lower portion contiguous with the upper portion.
- the lower portion includes an opening and a permeable bed in place over the opening through which the liquid coolant held in the upper portion of the liquid coolant distribution container passes and is distributed to the liquid coolant-receiving surface of the evaporative pad.
- the method includes wetting essentially the entirety of the evaporative pad with the liquid coolant passing into the evaporative pad.
- the method includes passing the air through the essentially entirely wetted evaporative pad.
- the method includes contacting essentially the entirety of the air with the coolant at the essentially entirely wetted evaporative pad, whereby essentially the entirety of the air passing through the essentially entirely wetted evaporative pad is cooled.
- FIG. 1 is a schematic side elevational view of an example of an evaporative cooling system, or evaporative cooler, incorporated in an air-conditioning system that supplies cooled air to a gas turbine system;
- FIG. 2 is a schematic perspective view of an example of a liquid coolant distribution container for distributing liquid coolant to an evaporative pad of an evaporative cooler such as the evaporative cooler referred to with respect to FIG. 1 ;
- FIG. 3 is a schematic cross-sectional view of the liquid coolant distribution container of FIG. 2 .
- FIG. 1 schematically illustrates an example embodiment of the invention wherein an evaporative cooling system, or evaporative cooler, indicated generally at 10 , is included as a component of an air-conditioning system, indicated generally at 40 .
- the air-conditioning system including the evaporative cooler 10 , is operably associated with a gas turbine system, indicated generally at 50 , to which air exiting the evaporative cooler 10 is directed to the gas turbine system.
- a compressor 52 at the gas turbine system 50 functions to draw ambient air into the air inlet 41 of the air-conditioning system 40 and through the air-conditioning system. After being suitably conditioned at the air-conditioning system 40 , the air streams through the adapter duct 44 (sometimes referred to as a transition duct or bellmouth) to the compressor 52 . The conditioned air, upon entering the compressor 52 , is compressed to relatively high pressures. Thereafter, the compressed air enters a combustion area 54 where the compressed air is mixed with a fuel such as natural gas, for example, and the mixture is burned to produce high-pressure, high-velocity gases that are the product of the combustion that takes place in the combustion area 54 .
- a fuel such as natural gas
- the high-pressure, high-velocity gases proceed to a turbine 55 possessed with considerable energy and drive the blades of the turbine that are attached to an output shaft 56 .
- the rotation of the turbine blades causes the output shaft 56 which is attached to rotate as well, and the energy of the output shaft 56 as it rotates is delivered to a generator 58 and electrical energy thereby produced at the generator as will be understood by those having ordinary skill in the art.
- the use of gas turbine systems is not limited to electrical power generation, however, and the turbine systems also can be applied, for example, to driving pumps and compressors.
- air from the ambient environment is used at the gas turbine system 50 .
- the ambient air may first be conditioned and that is accomplished at the air-conditioning system 40 .
- ambient air under the influence of the compressor 52 , is drawn into the air-conditioning system at air inlet 41 .
- the ambient air first enters a filter chamber 42 where particulate matter, including in some cases water droplets, is removed from the ambient air. Thereafter, the filtered air passes through the evaporative cooler 10 , the operation of which is discussed in greater detail below.
- the evaporative cooler functions to cool the filtered air and increases its density; and, as noted above, the denser air provides a higher mass flow rate and pressure ratio at the gas turbine system 50 , resulting in an increase in turbine output and efficiency.
- the filtered and cooled air that exits the evaporative cooler 10 flows to demisters 43 which remove unwanted water from the air. From the demisters, the air flows into the adapter duct 44 and from the adapter duct the conditioned air flows to the gas turbine system 50 where the conditioned air after being compressed is mixed with fuel and burned as described above.
- the arrows in FIG. 1 are all indicative of the flow of the air from its entry into the air-conditioning system 40 at the air inlet 41 to the delivery of the air at the compressor 52 of the gas turbine system 50 .
- the evaporative cooler 10 itself includes an evaporative pad, indicated generally at 12 in FIG. 2 , that includes an air-entry surface 14 at which air delivered to the evaporative pad from the filter chamber 42 enters and passes through the evaporative pad.
- the evaporative pad 12 also includes an air-exiting surface 16 at which air passing through the evaporative pad, and cooled at the pad, exits from the evaporative pad.
- the evaporative pad 12 further includes a liquid coolant-receiving surface 18 at which a liquid coolant distributed to the evaporator pad is received and thereafter passes into the evaporative pad.
- liquid coolants can be employed with evaporative coolers, in the example illustrated in the drawings water, either treated or untreated, or an aqueous solution can be used as the liquid coolant.
- Untreated water can include raw water taken from the environment or water that has been treated only for the purpose of making it potable.
- Treated water would include water that has been treated in order to render it more suitable for application to evaporative coolers.
- Water that has been demineralized and/or treated with surfactants and/or fungicides and bactericides are examples of treated water.
- Aqueous solutions would include homogeneous mixtures in which water is the solvent.
- a reservoir 20 is provided at the air-conditioning unit adjacent the bottom of the evaporative pad 12 as an adjunct to the evaporative cooler 10 .
- Water is added to the reservoir 20 through water inlet 21 in order to maintain sufficient water in the reservoir for the purpose of delivering the water in adequate amounts to the liquid coolant-receiving surface 18 of the evaporator pad.
- the delivery of the water is accomplished, for example, by means of a pump 24 that pumps water from the reservoir 20 through a conduit 25 to a water-delivery header 26 .
- the water-delivery header 26 delivers water to a liquid coolant distribution container, indicated generally at 28 , and, from the container, the water flows to the liquid coolant-receiving surface 18 of the evaporative pad 12 .
- the water-delivery header 26 can be configured so as to deliver the water in relatively equal amounts along the length and across the width of the liquid coolant distribution container 28 . From the liquid coolant-receiving surface 18 , the water flows downwardly towards the bottom of the evaporative pad 12 .
- the reservoir 20 also includes a drain 23 for removing sludge from the bottom portion of the reservoir that may accumulate over time.
- the water distributed to the liquid coolant-receiving surface 18 and passing into the evaporative pad 12 wets the evaporator pad as the water flows downwardly through the pad and, thereby, the water tends to be retained, at least in part, at the evaporator pad. To the extent that the water is not retained at the evaporative pad 12 , the water will flow from the evaporator pad at a liquid coolant-exiting surface 19 that is included as a part of the evaporator pad. Thus, the liquid coolant, water in the illustrated embodiment, which passes entirely through the evaporative pad 12 exits the evaporative pad at the liquid coolant-exiting surface 19 .
- the air-entry surface 14 , the air-exiting surface 16 , the liquid coolant-receiving surface 18 and the liquid coolant-exiting surface 19 of the evaporative pad 12 are arranged so that air flowing from the air-entry surface 14 to the air-exiting surface 16 through the evaporative pad 12 and liquid flowing from the liquid coolant-receiving surface 18 towards the liquid coolant-exiting surface 19 through the evaporative pad come into contact with one another.
- the liquid coolant evaporates so that the air flowing from the air-entry surface 14 to the air-exiting surface 16 through the evaporative pad is cooled.
- the evaporative pad 12 can be made of any one of a number of evaporative cooling media.
- a medium that can be employed is excelsior that is held in place by netting.
- Another example of a medium that can be used is plastic fibers.
- Corrugated structures, including structures made of corrugated cellulose or plastics also can be used. It can be important that, whatever medium is used, a large surface area be presented to the coolant and the air flowing through the evaporative pad so that cooling of the air upon contact with the liquid coolant is carried out efficiently. It also can be important that the evaporative cooling medium employed have the properties of providing for the relatively even distribution and good retention of the coolant at the medium.
- the liquid coolant distribution container 28 can take the form of a trough including sloping sides 29 that are inclined toward one another in the direction of the bottom of the trough.
- the liquid coolant distribution container 28 includes an upper portion 32 and a lower portion 34 .
- the upper portion 32 of the liquid coolant distribution container can be constructed of sheet material such as stainless steel or plastic sheeting for example and be configured to hold the liquid coolant so that the coolant cannot flow outwardly at the first portion of the liquid coolant distribution container and can flow only downwardly in the trough.
- the lower portion 34 of the liquid coolant distribution container is contiguous with the upper portion 32 and includes an opening 36 at the base of the lower portion.
- the lower portion 34 also includes a permeable bed 37 that is supported in place over the opening 36 , and the liquid coolant held in the upper portion 32 of the liquid coolant distribution container passes through the opening 36 and the permeable bed 37 and is distributed to the liquid coolant-receiving surface 18 of the evaporative pad 12 .
- the liquid coolant distribution container 28 is shown as supported somewhat above the liquid coolant-receiving surface 18 . However, the liquid coolant distribution container can be supported on and in contact with the liquid coolant-receiving surface 18 .
- the permeable bed 37 is sufficiently permeable to allow water held in the upper portion 32 of the liquid coolant distribution container to pass through the permeable bed and distributed to the liquid coolant-receiving surface 18 of the evaporative pad 12 at a selected rate that is sufficient to adequately keep essentially the entirety of the evaporative pad wetted with the coolant so that essentially the entirety of the air flowing through the pad comes into contact with the coolant and is cooled.
- An example of a material from which the permeable bed can be made is fiberglass padding. When fiberglass padding is employed, the padding can be placed over the opening 36 in the lower portion 34 of the liquid coolant distribution container 28 and held in place by the sloping sides 29 , 29 of the container.
- a material that can be used to form the permeable bed is relatively finely divided plastic material that can be contained within suitable netting and the finely divided plastic-filled netting placed over the opening 36 .
- suitable netting and the finely divided plastic-filled netting placed over the opening 36 .
- the sides of the trough need not be sloping as shown in the drawings but can be arranged so as to be positioned substantially vertically. In that case, it can be necessary to provide retainers of a suitable sort to hold the permeable bed in place over the opening 36 .
- the perimeter of the outer boundary of the evaporative pad 12 , the perimeter of the liquid coolant-receiving surface 18 and the perimeter of the opening 36 in the lower portion 34 of the liquid coolant distribution container 28 can be substantially co-extensive with one another. That is, these elements can have substantially the same outer dimensions or limits.
- coolant flowing through the opening 36 in the liquid coolant distribution container 28 will flow to essentially the entirety of the liquid coolant-receiving surface 18 of the evaporative pad 12 ; and the liquid coolant passing through the liquid coolant-receiving surface 18 and into the evaporative pad 12 will flow downwardly and wet essentially the entirety of the evaporative pad 12 so that essentially the entirety of the air flowing through the evaporative pad will come into contact with the liquid coolant and essentially the entirety of the flowing air cooled.
- Essentially the entirety of the evaporative pad can be considered to have been wetted and essentially the entirety of the air can be considered to have been contacted by the coolant so that essentially the entirety of the air is cooled whenever the properties of the air passing through the evaporative pad are only negligibly different from the properties of air that has passed through the evaporator pad when it has been wetted in its entirety.
- Another aspect of the invention that can be included in the construct of the liquid coolant distribution container 28 concerns features of the liquid coolant distribution container that result in the liquid coolant being distributed to the liquid coolant-receiving surface 18 of the evaporative pad 12 at a selected rate.
- the selected rate would be sufficient to cause essentially the entirety of the evaporative pad to be wetted by the liquid coolant flowing from the liquid coolant-receiving surface 18 of the evaporator pad towards the liquid coolant-exiting surface 19 of the evaporator pad.
- the selected rate would not be substantially greater than is required for that purpose and would be insufficient to cause an excessive amount of the liquid coolant to exit the liquid coolant-exiting surface 19 of the evaporative pad 12 .
- the excessive recirculation of the water from the reservoir 20 to the water-delivery header 26 is avoided.
- the rate at which liquid coolant will flow through the opening 36 in the liquid coolant distribution container 28 is essentially dependent on the depth of the liquid coolant in the container, or the magnitude of the head of the liquid coolant in the container, and the permeability characteristic of the permeable bed 37 .
- the upper portion 32 of the liquid coolant distribution container 28 is configured to maintain the liquid coolant at a selected depth in the upper portion 32 of the liquid coolant distribution container 28 above the permeable bed 37 and the permeable bed has a permeability characteristic, such that the liquid coolant is distributed to the liquid coolant-receiving surface 18 of the evaporative pad 12 through the permeable bed 37 at a rate that is sufficient to cause essentially the entirety of the evaporative pad 12 to be wetted by the liquid coolant flowing from the liquid coolant-receiving surface 18 of the evaporator pad towards the liquid coolant-exiting surface 19 of the evaporator pad but insufficient to cause an excessive amount of liquid coolant to exit the liquid coolant-exiting surface of the evaporative pad.
- the depth of the liquid coolant in the liquid coolant distribution container can be controlled, simply, by controlling the height to which the top of the container extends. In that case, coolant delivered to the container would be delivered at a rate such that coolant would continually flow to outside the container over the top of the container. In the embodiment shown in the drawings, however, an alternate technique is employed to control the depth of the liquid coolant. Thus, as best seen in FIGS. 2 and 3 , a notch 31 is provided in the rear panel 33 of the liquid coolant distribution container 28 .
- the bottom of the notch establishes the height to which coolant in the container can be maintained, with the coolant being delivered to the container from the water-delivery header 26 at a sufficient rate to cause coolant to continually, but somewhat slowly, flow through the notch in order to maintain that height.
- the coolant flowing from the liquid coolant distribution container through the notch 31 can be collected and routed through a conduit, for example, to the reservoir 20 .
- water can be delivered to the liquid coolant distribution container 28 using other than the water-delivery header 26 illustrated in FIG. 1 .
- a simple water delivery line can be hung over the top of one of the sloping sides 29 of the liquid coolant distribution container.
- an opening can be made in a side of the upper portion 32 of the container and the water line secured to the opening at the water line's discharge point.
- the permeability characteristic of the permeable bed 37 can be established in any one or more of a number of ways.
- the medium selected to make up the permeable bed can influence the permeability characteristic of the bed.
- a permeable bed of a fiberglass material can have a permeability characteristic that is different than the permeability characteristic of granulated material such as finely divided plastic spheres.
- the permeability characteristic of the fiberglass material itself can be influenced by the density of the fiberglass material.
- the permeability characteristic of the granulated material can be influenced by how tightly the granules are packed together for example.
- the invention can include a method of cooling air including passing a liquid coolant through an evaporative pad of an evaporative cooler and wetting essentially the entirety of the evaporative pad with the liquid coolant as the liquid coolant passes through the evaporative pad.
- the method can also include passing the air to be cooled through the essentially entirely wetted evaporative pad and contacting essentially the entirety of the air with the essentially entirely wetted evaporative pad, whereby essentially the entirety of the air passing through the essentially entirely wetted evaporative pad is cooled.
- the method can include distributing the liquid coolant to a liquid coolant-receiving surface at the evaporative pad by passing the liquid coolant through a permeable bed before passing the liquid coolant into the evaporative pad.
- the method can include maintaining the depth of the liquid coolant in the upper portion of a liquid coolant distribution container at a level and the permeability characteristic of the permeable bed at a value such that the liquid coolant is distributed to the liquid coolant-receiving surface of the evaporative pad through an opening in the liquid coolant distribution container and the permeable bed that overlies the opening at a rate that is sufficient to cause essentially the entirety of the evaporative pad to be wetted by the liquid coolant flowing from the liquid coolant-receiving surface of the evaporator pad towards a liquid coolant-exiting surface of the evaporator pad but insufficient to cause an excessive amount of liquid coolant to exit from the liquid coolant-exiting surface of the evaporative pad.
- the present invention has been described above and illustrated with reference to certain embodiments thereof, it is to be understood that the invention is not so limited.
- the present invention has applications to evaporative cooler systems, or evaporative coolers of essentially any type. These include, but are not limited to, evaporative coolers for cooling air for thermal comfort and evaporative coolers for controlling the temperature of the air in structures such as greenhouses and buildings containing livestock.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Air Humidification (AREA)
Abstract
Description
- 1. Field of the Invention
- The present invention relates generally to a method and apparatus concerning the operation of evaporative cooling systems and, in particular, to a method and apparatus concerning the effective wetting by a liquid coolant of an evaporative pad of an evaporative cooling system that cools air supplied to a gas turbine system.
- 2. Discussion of the Prior Art
- Evaporative cooling systems, or evaporative coolers as such systems are typically referred to, are employed in various ways in residential, commercial and industrial contexts. In one example, the evaporative coolers cool air that is directed through the evaporative coolers. The evaporative coolers cool the air through the evaporation of a coolant, typically water, which is brought into contact with the air at the evaporative coolers.
- Typically, an evaporative cooler includes an evaporative pad at which the air directed to the evaporative cooler is cooled. A coolant, such as water for example, is caused to flow through the evaporative pad and air is brought into contact with the coolant at the pad, usually by means of a fan, blower or turbine drawing or forcing the air through the pad. The evaporative pad typically is constructed of a material that has a large surface area over which the coolant is dispersed so that the coolant assumes a large surface area at the evaporative pad, thereby facilitating the evaporation of the coolant at the pad. Heat transfer takes place between the air and the dispersed coolant, as the air comes into contact with the coolant at the evaporative pad, and the coolant thereby evaporated, causing the air to cool and the density of the air to increase. Coolant is continuously delivered to the evaporative pad to replace the coolant that evaporates.
- Evaporative coolers are known to be employed for the purpose of cooling the living spaces of residential structures and the working environments of commercial and industrial buildings for thermal comfort for example. In addition, evaporative coolers are known to be applied in industrial processes in which a supply of cooler and denser air can be used to advantage. For example, an evaporative cooler can be employed in conjunction with a gas turbine system wherein the cooled air from the evaporative cooler is compressed and the compressed air mixed with a fuel such as natural gas for example. The mixture of air and fuel is combusted and the resulting expanding gases are directed to a turbine so as to drive the turbine that, in turn, drives an electrical generator for producing electrical power for example. The cooled air, because of its increased density, provides a higher mass flow rate and pressure ratio at the gas turbine equipment, resulting in an increase in turbine output and efficiency.
- The foregoing benefit, however, may not be fully realized in those instances in which the evaporative pad is not completely wetted by the coolant so that the air passing through the pad is cooled to a lesser extent than would be the case in which the pad is essentially entirely wetted by the coolant. Additionally, the areas of the evaporative pad that are not wetted by the coolant can result in the establishment of temperatures in the air that passes through these non-wetted areas that are warmer than the temperatures in the air that has come into contact with the coolant in areas of the evaporative pad that have been wetted by the liquid coolant. These temperature differences in the respective air masses that are then directed to the turbine compressor can cause air turbulence that can result in damage to the turbine equipment. Even in the absence such damage, the vibration of the turbine blades can result in the deteriorated performance of the turbine equipment.
- The following sets forth a simplified summary of examples of the present invention for the purpose of providing a basic understanding of selected aspects of the invention. The summary does not constitute an extensive overview of all the aspects or embodiments of the invention. Neither is the summary intended to identify critical aspects or delineate the scope of the invention. The sole purpose of the summary is to present selected aspects of the invention in a simplified form as an introduction to the more detailed description of the embodiments of the invention that follows the summary.
- In accordance with one aspect, the present invention provides an evaporative cooler that includes an evaporative pad including a liquid coolant-receiving surface at which a liquid coolant distributed to the evaporative pad is received and thereafter passes into the evaporative pad. The evaporative cooler also includes a liquid coolant distribution container that includes an upper portion configured to hold liquid coolant and a lower portion contiguous with the upper portion. The lower portion includes an opening and a permeable bed in place over the opening through which the liquid coolant held in the upper portion of the liquid coolant distribution container passes and is distributed to the liquid coolant-receiving surface of the evaporative pad.
- In accordance with another aspect, the present invention provides a method of cooling air. The method includes passing a liquid coolant into an evaporative pad. The pad includes a liquid coolant-receiving surface at which a liquid coolant distributed to the evaporative pad is received and thereafter passes into the evaporative pad. The evaporative pad is of an evaporative cooler and the passage of liquid coolant is from a liquid coolant distribution container. The liquid coolant distribution container includes an upper portion configured to hold liquid coolant and a lower portion contiguous with the upper portion. The lower portion includes an opening and a permeable bed in place over the opening through which the liquid coolant held in the upper portion of the liquid coolant distribution container passes and is distributed to the liquid coolant-receiving surface of the evaporative pad. The method includes wetting essentially the entirety of the evaporative pad with the liquid coolant passing into the evaporative pad. The method includes passing the air through the essentially entirely wetted evaporative pad. The method includes contacting essentially the entirety of the air with the coolant at the essentially entirely wetted evaporative pad, whereby essentially the entirety of the air passing through the essentially entirely wetted evaporative pad is cooled.
- The foregoing and other aspects of the present invention will be apparent to those skilled in the art to which the present invention relates from the detailed descriptions of examples of aspects and embodiments of the invention that follow with reference to the accompanying drawings, wherein the same reference numerals are used in the several figures to refer to the same parts or elements and in which:
-
FIG. 1 is a schematic side elevational view of an example of an evaporative cooling system, or evaporative cooler, incorporated in an air-conditioning system that supplies cooled air to a gas turbine system; -
FIG. 2 is a schematic perspective view of an example of a liquid coolant distribution container for distributing liquid coolant to an evaporative pad of an evaporative cooler such as the evaporative cooler referred to with respect toFIG. 1 ; and -
FIG. 3 is a schematic cross-sectional view of the liquid coolant distribution container ofFIG. 2 . - Examples of embodiments that incorporate one or more aspects of the present invention are described below with references, in certain respects, to the accompanying drawings. These examples are not intended to be limitations on the present invention. Thus, for example, in some instances, one or more examples of the present invention described with reference to one aspect or embodiment can be utilized in other aspects and embodiments. In addition, certain terminology is used herein for convenience only and is not to be taken as limiting the present invention.
-
FIG. 1 schematically illustrates an example embodiment of the invention wherein an evaporative cooling system, or evaporative cooler, indicated generally at 10, is included as a component of an air-conditioning system, indicated generally at 40. The air-conditioning system, including theevaporative cooler 10, is operably associated with a gas turbine system, indicated generally at 50, to which air exiting theevaporative cooler 10 is directed to the gas turbine system. - A
compressor 52 at thegas turbine system 50 functions to draw ambient air into theair inlet 41 of the air-conditioning system 40 and through the air-conditioning system. After being suitably conditioned at the air-conditioning system 40, the air streams through the adapter duct 44 (sometimes referred to as a transition duct or bellmouth) to thecompressor 52. The conditioned air, upon entering thecompressor 52, is compressed to relatively high pressures. Thereafter, the compressed air enters acombustion area 54 where the compressed air is mixed with a fuel such as natural gas, for example, and the mixture is burned to produce high-pressure, high-velocity gases that are the product of the combustion that takes place in thecombustion area 54. The high-pressure, high-velocity gases proceed to aturbine 55 possessed with considerable energy and drive the blades of the turbine that are attached to anoutput shaft 56. The rotation of the turbine blades causes theoutput shaft 56 which is attached to rotate as well, and the energy of theoutput shaft 56 as it rotates is delivered to agenerator 58 and electrical energy thereby produced at the generator as will be understood by those having ordinary skill in the art. The use of gas turbine systems is not limited to electrical power generation, however, and the turbine systems also can be applied, for example, to driving pumps and compressors. - For optimum plant operation, air from the ambient environment is used at the
gas turbine system 50. The ambient air may first be conditioned and that is accomplished at the air-conditioning system 40. Again referring toFIG. 1 , as noted above, ambient air, under the influence of thecompressor 52, is drawn into the air-conditioning system atair inlet 41. The ambient air first enters afilter chamber 42 where particulate matter, including in some cases water droplets, is removed from the ambient air. Thereafter, the filtered air passes through theevaporative cooler 10, the operation of which is discussed in greater detail below. However, it is noted here that the evaporative cooler functions to cool the filtered air and increases its density; and, as noted above, the denser air provides a higher mass flow rate and pressure ratio at thegas turbine system 50, resulting in an increase in turbine output and efficiency. - The filtered and cooled air that exits the
evaporative cooler 10 flows to demisters 43 which remove unwanted water from the air. From the demisters, the air flows into theadapter duct 44 and from the adapter duct the conditioned air flows to thegas turbine system 50 where the conditioned air after being compressed is mixed with fuel and burned as described above. The arrows inFIG. 1 are all indicative of the flow of the air from its entry into the air-conditioning system 40 at theair inlet 41 to the delivery of the air at thecompressor 52 of thegas turbine system 50. - The
evaporative cooler 10 itself includes an evaporative pad, indicated generally at 12 inFIG. 2 , that includes an air-entry surface 14 at which air delivered to the evaporative pad from thefilter chamber 42 enters and passes through the evaporative pad. Theevaporative pad 12 also includes an air-exitingsurface 16 at which air passing through the evaporative pad, and cooled at the pad, exits from the evaporative pad. Theevaporative pad 12 further includes a liquid coolant-receivingsurface 18 at which a liquid coolant distributed to the evaporator pad is received and thereafter passes into the evaporative pad. Although various types of liquid coolants can be employed with evaporative coolers, in the example illustrated in the drawings water, either treated or untreated, or an aqueous solution can be used as the liquid coolant. Untreated water can include raw water taken from the environment or water that has been treated only for the purpose of making it potable. Treated water would include water that has been treated in order to render it more suitable for application to evaporative coolers. Water that has been demineralized and/or treated with surfactants and/or fungicides and bactericides are examples of treated water. Aqueous solutions would include homogeneous mixtures in which water is the solvent. - A
reservoir 20 is provided at the air-conditioning unit adjacent the bottom of theevaporative pad 12 as an adjunct to theevaporative cooler 10. Water is added to thereservoir 20 throughwater inlet 21 in order to maintain sufficient water in the reservoir for the purpose of delivering the water in adequate amounts to the liquid coolant-receivingsurface 18 of the evaporator pad. The delivery of the water is accomplished, for example, by means of apump 24 that pumps water from thereservoir 20 through aconduit 25 to a water-delivery header 26. The water-delivery header 26 delivers water to a liquid coolant distribution container, indicated generally at 28, and, from the container, the water flows to the liquid coolant-receivingsurface 18 of theevaporative pad 12. The water-delivery header 26 can be configured so as to deliver the water in relatively equal amounts along the length and across the width of the liquidcoolant distribution container 28. From the liquid coolant-receivingsurface 18, the water flows downwardly towards the bottom of theevaporative pad 12. Thereservoir 20 also includes adrain 23 for removing sludge from the bottom portion of the reservoir that may accumulate over time. - The water distributed to the liquid coolant-receiving
surface 18 and passing into theevaporative pad 12 wets the evaporator pad as the water flows downwardly through the pad and, thereby, the water tends to be retained, at least in part, at the evaporator pad. To the extent that the water is not retained at theevaporative pad 12, the water will flow from the evaporator pad at a liquid coolant-exitingsurface 19 that is included as a part of the evaporator pad. Thus, the liquid coolant, water in the illustrated embodiment, which passes entirely through theevaporative pad 12 exits the evaporative pad at the liquid coolant-exitingsurface 19. - Based on the foregoing description, it will be understood that the air-
entry surface 14, the air-exitingsurface 16, the liquid coolant-receivingsurface 18 and the liquid coolant-exitingsurface 19 of theevaporative pad 12 are arranged so that air flowing from the air-entry surface 14 to the air-exitingsurface 16 through theevaporative pad 12 and liquid flowing from the liquid coolant-receivingsurface 18 towards the liquid coolant-exitingsurface 19 through the evaporative pad come into contact with one another. As a result of this contact of the air and the liquid coolant, the liquid coolant evaporates so that the air flowing from the air-entry surface 14 to the air-exitingsurface 16 through the evaporative pad is cooled. - The
evaporative pad 12 can be made of any one of a number of evaporative cooling media. One example of a medium that can be employed is excelsior that is held in place by netting. Another example of a medium that can be used is plastic fibers. Corrugated structures, including structures made of corrugated cellulose or plastics also can be used. It can be important that, whatever medium is used, a large surface area be presented to the coolant and the air flowing through the evaporative pad so that cooling of the air upon contact with the liquid coolant is carried out efficiently. It also can be important that the evaporative cooling medium employed have the properties of providing for the relatively even distribution and good retention of the coolant at the medium. - Turning to a discussion of the construction of the liquid
coolant distribution container 28, as best illustrated inFIGS. 2 and 3 , the liquid coolant distribution container can take the form of a trough including slopingsides 29 that are inclined toward one another in the direction of the bottom of the trough. The liquidcoolant distribution container 28 includes anupper portion 32 and alower portion 34. Theupper portion 32 of the liquid coolant distribution container can be constructed of sheet material such as stainless steel or plastic sheeting for example and be configured to hold the liquid coolant so that the coolant cannot flow outwardly at the first portion of the liquid coolant distribution container and can flow only downwardly in the trough. Thelower portion 34 of the liquid coolant distribution container is contiguous with theupper portion 32 and includes anopening 36 at the base of the lower portion. Thelower portion 34 also includes apermeable bed 37 that is supported in place over theopening 36, and the liquid coolant held in theupper portion 32 of the liquid coolant distribution container passes through theopening 36 and thepermeable bed 37 and is distributed to the liquid coolant-receivingsurface 18 of theevaporative pad 12. In the example illustrated inFIGS. 1 and 2 , the liquidcoolant distribution container 28 is shown as supported somewhat above the liquid coolant-receivingsurface 18. However, the liquid coolant distribution container can be supported on and in contact with the liquid coolant-receivingsurface 18. - The
permeable bed 37 is sufficiently permeable to allow water held in theupper portion 32 of the liquid coolant distribution container to pass through the permeable bed and distributed to the liquid coolant-receivingsurface 18 of theevaporative pad 12 at a selected rate that is sufficient to adequately keep essentially the entirety of the evaporative pad wetted with the coolant so that essentially the entirety of the air flowing through the pad comes into contact with the coolant and is cooled. An example of a material from which the permeable bed can be made is fiberglass padding. When fiberglass padding is employed, the padding can be placed over theopening 36 in thelower portion 34 of the liquidcoolant distribution container 28 and held in place by the slopingsides opening 36. It will be understood to those skilled in the art that the sides of the trough need not be sloping as shown in the drawings but can be arranged so as to be positioned substantially vertically. In that case, it can be necessary to provide retainers of a suitable sort to hold the permeable bed in place over theopening 36. - In order to be most assured that the liquid
coolant distribution container 28 will function to wet essentially the entirety of theevaporative pad 12, as best seen inFIG. 2 , the perimeter of the outer boundary of theevaporative pad 12, the perimeter of the liquid coolant-receivingsurface 18 and the perimeter of theopening 36 in thelower portion 34 of the liquidcoolant distribution container 28 can be substantially co-extensive with one another. That is, these elements can have substantially the same outer dimensions or limits. Consequently, coolant flowing through theopening 36 in the liquidcoolant distribution container 28 will flow to essentially the entirety of the liquid coolant-receivingsurface 18 of theevaporative pad 12; and the liquid coolant passing through the liquid coolant-receivingsurface 18 and into theevaporative pad 12 will flow downwardly and wet essentially the entirety of theevaporative pad 12 so that essentially the entirety of the air flowing through the evaporative pad will come into contact with the liquid coolant and essentially the entirety of the flowing air cooled. Thereby, the development of hot spots in theevaporative pad 12 that can be the cause of damage to the blades of the compressor and the consequent operational failure of the gas turbine system can be avoided. - Essentially the entirety of the evaporative pad can be considered to have been wetted and essentially the entirety of the air can be considered to have been contacted by the coolant so that essentially the entirety of the air is cooled whenever the properties of the air passing through the evaporative pad are only negligibly different from the properties of air that has passed through the evaporator pad when it has been wetted in its entirety.
- Another aspect of the invention that can be included in the construct of the liquid
coolant distribution container 28 concerns features of the liquid coolant distribution container that result in the liquid coolant being distributed to the liquid coolant-receivingsurface 18 of theevaporative pad 12 at a selected rate. The selected rate would be sufficient to cause essentially the entirety of the evaporative pad to be wetted by the liquid coolant flowing from the liquid coolant-receivingsurface 18 of the evaporator pad towards the liquid coolant-exitingsurface 19 of the evaporator pad. However, the selected rate would not be substantially greater than is required for that purpose and would be insufficient to cause an excessive amount of the liquid coolant to exit the liquid coolant-exitingsurface 19 of theevaporative pad 12. In this aspect, the excessive recirculation of the water from thereservoir 20 to the water-delivery header 26 is avoided. - The rate at which liquid coolant will flow through the
opening 36 in the liquidcoolant distribution container 28, aside from the physical properties of the liquid coolant itself such as its viscosity for example, is essentially dependent on the depth of the liquid coolant in the container, or the magnitude of the head of the liquid coolant in the container, and the permeability characteristic of thepermeable bed 37. Consequently, in the example of the invention shown in the drawings, theupper portion 32 of the liquidcoolant distribution container 28 is configured to maintain the liquid coolant at a selected depth in theupper portion 32 of the liquidcoolant distribution container 28 above thepermeable bed 37 and the permeable bed has a permeability characteristic, such that the liquid coolant is distributed to the liquid coolant-receivingsurface 18 of theevaporative pad 12 through thepermeable bed 37 at a rate that is sufficient to cause essentially the entirety of theevaporative pad 12 to be wetted by the liquid coolant flowing from the liquid coolant-receivingsurface 18 of the evaporator pad towards the liquid coolant-exitingsurface 19 of the evaporator pad but insufficient to cause an excessive amount of liquid coolant to exit the liquid coolant-exiting surface of the evaporative pad. - The depth of the liquid coolant in the liquid coolant distribution container can be controlled, simply, by controlling the height to which the top of the container extends. In that case, coolant delivered to the container would be delivered at a rate such that coolant would continually flow to outside the container over the top of the container. In the embodiment shown in the drawings, however, an alternate technique is employed to control the depth of the liquid coolant. Thus, as best seen in
FIGS. 2 and 3 , anotch 31 is provided in therear panel 33 of the liquidcoolant distribution container 28. The bottom of the notch establishes the height to which coolant in the container can be maintained, with the coolant being delivered to the container from the water-delivery header 26 at a sufficient rate to cause coolant to continually, but somewhat slowly, flow through the notch in order to maintain that height. The coolant flowing from the liquid coolant distribution container through thenotch 31 can be collected and routed through a conduit, for example, to thereservoir 20. It will be understood to those skilled in the art that water can be delivered to the liquidcoolant distribution container 28 using other than the water-delivery header 26 illustrated inFIG. 1 . For example, a simple water delivery line can be hung over the top of one of the slopingsides 29 of the liquid coolant distribution container. Alternately, an opening can be made in a side of theupper portion 32 of the container and the water line secured to the opening at the water line's discharge point. - The permeability characteristic of the
permeable bed 37 can be established in any one or more of a number of ways. For example, the medium selected to make up the permeable bed can influence the permeability characteristic of the bed. Thus, a permeable bed of a fiberglass material can have a permeability characteristic that is different than the permeability characteristic of granulated material such as finely divided plastic spheres. Also, the permeability characteristic of the fiberglass material itself can be influenced by the density of the fiberglass material. As well, the permeability characteristic of the granulated material can be influenced by how tightly the granules are packed together for example. - It will be understood from the foregoing description that in one aspect, the invention can include a method of cooling air including passing a liquid coolant through an evaporative pad of an evaporative cooler and wetting essentially the entirety of the evaporative pad with the liquid coolant as the liquid coolant passes through the evaporative pad. The method can also include passing the air to be cooled through the essentially entirely wetted evaporative pad and contacting essentially the entirety of the air with the essentially entirely wetted evaporative pad, whereby essentially the entirety of the air passing through the essentially entirely wetted evaporative pad is cooled. In another aspect, the method can include distributing the liquid coolant to a liquid coolant-receiving surface at the evaporative pad by passing the liquid coolant through a permeable bed before passing the liquid coolant into the evaporative pad. In still another aspect, the method can include maintaining the depth of the liquid coolant in the upper portion of a liquid coolant distribution container at a level and the permeability characteristic of the permeable bed at a value such that the liquid coolant is distributed to the liquid coolant-receiving surface of the evaporative pad through an opening in the liquid coolant distribution container and the permeable bed that overlies the opening at a rate that is sufficient to cause essentially the entirety of the evaporative pad to be wetted by the liquid coolant flowing from the liquid coolant-receiving surface of the evaporator pad towards a liquid coolant-exiting surface of the evaporator pad but insufficient to cause an excessive amount of liquid coolant to exit from the liquid coolant-exiting surface of the evaporative pad. In yet further aspects, the invention can include the foregoing methods wherein liquid coolant distribution containers and evaporative pads of the types described above can be employed and the methods are employed to provide cooled air to a gas turbine system.
- While the present invention has been described above and illustrated with reference to certain embodiments thereof, it is to be understood that the invention is not so limited. Thus, the present invention has applications to evaporative cooler systems, or evaporative coolers of essentially any type. These include, but are not limited to, evaporative coolers for cooling air for thermal comfort and evaporative coolers for controlling the temperature of the air in structures such as greenhouses and buildings containing livestock.
- Modifications and alterations will occur to those skilled in the art upon reading and understanding the specification, including the drawings. In any event, the present invention covers and includes any and all modifications and variations to the described embodiments that are encompassed by the following claims.
Claims (20)
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/173,072 US20130000329A1 (en) | 2011-06-30 | 2011-06-30 | Method of wetting evaporative cooler media through a permeable layer |
GB1211508.5A GB2492479A (en) | 2011-06-30 | 2012-06-28 | Wetting of an evaporative cooler media through a permeable layer |
DE102012105753A DE102012105753A1 (en) | 2011-06-30 | 2012-06-29 | Method for moistening evaporative cooling media by a permeable layer |
CN2012103008576A CN102853685A (en) | 2011-06-30 | 2012-06-30 | Method of wetting evaporative cooler media through a permeable layer |
US14/167,072 US20140144171A1 (en) | 2011-06-30 | 2014-01-29 | Method of Wetting Evaporative Cooler Media Through a Fabric Distribution Layer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/173,072 US20130000329A1 (en) | 2011-06-30 | 2011-06-30 | Method of wetting evaporative cooler media through a permeable layer |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US14/167,072 Continuation-In-Part US20140144171A1 (en) | 2011-06-30 | 2014-01-29 | Method of Wetting Evaporative Cooler Media Through a Fabric Distribution Layer |
Publications (1)
Publication Number | Publication Date |
---|---|
US20130000329A1 true US20130000329A1 (en) | 2013-01-03 |
Family
ID=46704379
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US13/173,072 Abandoned US20130000329A1 (en) | 2011-06-30 | 2011-06-30 | Method of wetting evaporative cooler media through a permeable layer |
Country Status (4)
Country | Link |
---|---|
US (1) | US20130000329A1 (en) |
CN (1) | CN102853685A (en) |
DE (1) | DE102012105753A1 (en) |
GB (1) | GB2492479A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8979291B2 (en) | 2013-05-07 | 2015-03-17 | Universal Display Corporation | Lighting devices including transparent organic light emitting device light panels and having independent control of direct to indirect light |
US9018660B2 (en) | 2013-03-25 | 2015-04-28 | Universal Display Corporation | Lighting devices |
US20150253046A1 (en) * | 2014-03-07 | 2015-09-10 | University Of Central Florida Research Foundation, Inc. | Evaporatively cooled mini-split air conditioning system |
US9358488B2 (en) | 2013-11-15 | 2016-06-07 | Bha Altair, Llc | Gas turbine filtration system with inlet filter orientation assembly |
US10260421B2 (en) * | 2017-03-20 | 2019-04-16 | General Electric Company | Fibrous media drift eliminator |
US10514136B2 (en) | 2013-03-25 | 2019-12-24 | Universal Display Corporation | Lighting devices |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104234838B (en) * | 2013-06-18 | 2019-02-15 | 通用电气公司 | Detection system and method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4236537A (en) * | 1978-05-03 | 1980-12-02 | Industrial Sheet Metal & Mechanical Corp. | Ordering system for tobacco bulk curing barn |
US5606868A (en) * | 1995-03-06 | 1997-03-04 | General Shelters Of Texas S.B., Inc. | Reticulated foam sleeve for evaporative cooling unit spray conduit |
US20010032477A1 (en) * | 2000-02-23 | 2001-10-25 | Leslie Schlom | Heat exchanger for cooling and for a pre-cooler for turbine intake air conditioning |
US6367277B1 (en) * | 2001-04-10 | 2002-04-09 | Stephen W. Kinkel | Evaporative cooling apparatus |
US6468389B1 (en) * | 1999-11-09 | 2002-10-22 | James Jeffrey Harris | Undulating membrane surface for evaporative processes |
US20030150234A1 (en) * | 2002-01-09 | 2003-08-14 | Tadahiro Ohmi | Air cooling device and air cooling method |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4080410A (en) * | 1975-06-09 | 1978-03-21 | Goettl Adam D | Evaporative cooler construction |
US4045523A (en) * | 1975-06-09 | 1977-08-30 | Goettl Adam D | Evaporative cooler with superimposed disposable pad assemblies |
-
2011
- 2011-06-30 US US13/173,072 patent/US20130000329A1/en not_active Abandoned
-
2012
- 2012-06-28 GB GB1211508.5A patent/GB2492479A/en not_active Withdrawn
- 2012-06-29 DE DE102012105753A patent/DE102012105753A1/en not_active Withdrawn
- 2012-06-30 CN CN2012103008576A patent/CN102853685A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4236537A (en) * | 1978-05-03 | 1980-12-02 | Industrial Sheet Metal & Mechanical Corp. | Ordering system for tobacco bulk curing barn |
US5606868A (en) * | 1995-03-06 | 1997-03-04 | General Shelters Of Texas S.B., Inc. | Reticulated foam sleeve for evaporative cooling unit spray conduit |
US6468389B1 (en) * | 1999-11-09 | 2002-10-22 | James Jeffrey Harris | Undulating membrane surface for evaporative processes |
US20010032477A1 (en) * | 2000-02-23 | 2001-10-25 | Leslie Schlom | Heat exchanger for cooling and for a pre-cooler for turbine intake air conditioning |
US6367277B1 (en) * | 2001-04-10 | 2002-04-09 | Stephen W. Kinkel | Evaporative cooling apparatus |
US20030150234A1 (en) * | 2002-01-09 | 2003-08-14 | Tadahiro Ohmi | Air cooling device and air cooling method |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9018660B2 (en) | 2013-03-25 | 2015-04-28 | Universal Display Corporation | Lighting devices |
US10514136B2 (en) | 2013-03-25 | 2019-12-24 | Universal Display Corporation | Lighting devices |
US8979291B2 (en) | 2013-05-07 | 2015-03-17 | Universal Display Corporation | Lighting devices including transparent organic light emitting device light panels and having independent control of direct to indirect light |
US9358488B2 (en) | 2013-11-15 | 2016-06-07 | Bha Altair, Llc | Gas turbine filtration system with inlet filter orientation assembly |
US10323572B2 (en) | 2013-11-15 | 2019-06-18 | Bha Altair, Llc | Gas turbine filtration system with inlet filter orientation assembly |
US20150253046A1 (en) * | 2014-03-07 | 2015-09-10 | University Of Central Florida Research Foundation, Inc. | Evaporatively cooled mini-split air conditioning system |
US10260421B2 (en) * | 2017-03-20 | 2019-04-16 | General Electric Company | Fibrous media drift eliminator |
Also Published As
Publication number | Publication date |
---|---|
GB2492479A (en) | 2013-01-02 |
CN102853685A (en) | 2013-01-02 |
GB201211508D0 (en) | 2012-08-08 |
DE102012105753A1 (en) | 2013-01-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20130000329A1 (en) | Method of wetting evaporative cooler media through a permeable layer | |
US20140144171A1 (en) | Method of Wetting Evaporative Cooler Media Through a Fabric Distribution Layer | |
US8966924B2 (en) | Pre-cooling chamber for a cooling tower | |
CN1128966C (en) | Heat pump/engine system, and method for utilizing same | |
AU2001269912B2 (en) | Direct turbine air chiller/scrubber system | |
US8662150B2 (en) | Heat exchanger media pad for a gas turbine | |
JP6910289B2 (en) | Combination type convector | |
JP6599140B2 (en) | Media pad for gas turbine | |
RU98122426A (en) | METHOD AND DEVICE FOR INCREASING POWER IN GAS TURBINES BY WET COMPRESSION | |
AU2001269912A1 (en) | Direct turbine air chiller/scrubber system | |
JP2009503431A (en) | Convector for cooling pipe circulating fluid | |
US9551282B2 (en) | Media pads with mist elimination features | |
IL144119A (en) | Air conditioning system | |
CN1711448A (en) | Air conditioning system and methods | |
CN101907020A (en) | Be used to regulate the system of the air-flow that enters turbo machine | |
EP2774478A1 (en) | System and method for dehumidifying greenhouse air | |
JP2006505401A (en) | Biological filter device provided with a plurality of filter units | |
US8517355B2 (en) | Evaporative cooling tower and method | |
US20120273171A1 (en) | Earthen evaporative heat exchanger | |
CN1201516A (en) | Method and apparatus for cooling fluid and dehumidifying and cooling gas | |
JP2015218931A (en) | Auxiliary cooling device of heat exchanger | |
KR100320726B1 (en) | Water direct contact air conditioning | |
CN105928106A (en) | Capillary tube closed type evaporative cooling water chilling unit | |
CN207715240U (en) | A kind of gas turbine inlet spray cooling device and gas turbine engine systems | |
JP6587587B2 (en) | Auxiliary cooling device for condenser |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: GENERAL ELECTRIC COMPANY, NEW YORK Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SMITH, PETER JOHN DUNCAN;KULKARNI, ABHIJEET MADHUKAR;SIGNING DATES FROM 20110628 TO 20110629;REEL/FRAME:026527/0602 |
|
AS | Assignment |
Owner name: BHA ALTAIR, LLC, TENNESSEE Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:GENERAL ELECTRIC COMPANY;BHA GROUP, INC.;ALTAIR FILTER TECHNOLOGY LIMITED;REEL/FRAME:031911/0797 Effective date: 20131216 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |