Abstract: In one aspect, a heat exchange apparatus is provided that includes an evaporative heat exchanger assembly including an evaporative heat exchanger and an evaporative liquid distribution assembly configured to distribute evaporative liquid onto the evaporative heat exchanger. The heat exchange apparatus includes a plume abatement assembly downstream of the evaporative heat exchanger. The plume abatement assembly includes at least one heating element configured to increase the temperature of the airflow from the evaporative heat exchanger before the airflow leaves the heat exchange apparatus. The plume abatement assembly has an operative configuration wherein the airflow travels through the at least one heating element to permit the at least one heating element to raise the temperature of the airflow and a bypass configuration wherein less of the airflow travels through the at least one heating element of the plume abatement assembly.

Abstract: An exhaust heat recovery apparatus is installed proximate an engine and at a front side of a warm-up catalytic converter in an exhaust system, where the exhaust system includes an exhaust line connected with the engine, and the warm-up catalytic converter is installed at the exhaust line. The exhaust heat recovery apparatus includes a bellows unit which is of a dual-pipe type and exchanges heat between exhaust gas emitted through the exhaust line and coolant circulating from a cooling system to the engine.

Abstract: A dual pipe includes an outer pipe having a valley/ridge portion on an outer circumferential surface thereof, and an inner pipe having a valley/ridge portion formed on an inner circumferential surface thereof and inserted into the outer pipe. In the dual pipe, the inner pipe and the outer pipe are threadedly engaged with each other. A low pressure refrigerant passes through the inner pipe. In order to secure a passage of a high pressure refrigerant in a space between the outer circumferential surface of the inner pipe and the inner circumferential surface of the outer pipe, a part of the helical valley/ridge portion formed on the outer circumferential surface of the inner pipe is composed of a multiple-helix helical valley/ridge portion.

Abstract: Embodiments of the present disclosure provide cooling systems for turbomachinery and methods of installation. In an embodiment, an apparatus of the present disclosure can include a ventilation conduit for routing a cooling air from a compressor of a power generation system to a turbine component of the power generation system; and a nozzle in fluid communication with the ventilation conduit, wherein the nozzle delivers water from a water supply into the ventilation conduit.

Abstract: The present application provides a gasifier for creating a flow of a syngas. The gasifier may include a reaction chamber and a quench chamber. The quench chamber may include a number of integrated scrubber trays therein such that the syngas first enters a quench pool via a dip tube and then passes through the scrubber trays before leaving the quench chamber.

Abstract: A system and a method for promoting improved air flow through a cooling tower and reduced inner air pressure losses caused by rain in the rain zone of a cooling tower. Aerodynamic modules are mounted on the lower edge of the cooling tower shell in order to deflect the downward-flowing air about the lower edge of the tower shell and into the rain zone. The aerodynamic modules can be modularly mounted, can be replaced, and do not affect the statics of the tower shell. Aerodynamic modules can also be built on the base area to deflect the incoming air over any obstacles. Troughs or dripping elements can also promote flow by reducing the rain falling in an outer area.

Abstract: A carrier-gas mixture is directed through a fluid flow path in a combined heat and mass transfer device operating at a sub-atmospheric pressure. Heat and mass are transferred from or to the carrier-gas mixture via interaction with a liquid composition that includes a vaporizable component in a liquid state to substantially change the content of the vaporizable component in the carrier-gas mixture via evaporation or condensation of the vaporizable component. The mass flow rate of the carrier-gas mixture is varied by extracting or injecting the carrier-gas mixture from at least one intermediate location in the fluid flow path, and/or the mass flow rate of the liquid composition is varied by extracting or injecting the liquid composition from at least one intermediate location in the fluid flow path; and the flow of the carrier-gas mixture or the liquid composition is regulated to reduce the average local enthalpy pinch in the device.

Abstract: An improved structure of cooling tower includes a fan housing with a fan disposed therein, induction openings distributed on the fan housing and located below the fan, and a diffuser stack disposed at one end surface of the fan housing. In operation, cold air is drawn into the cooling tower by the fan through inlet openings of the cooling tower so as to exchange heat with the condensing water within a water chiller. When warm and wet air is drawn out of the cooling tower and the warm and wet air outside the cooling tower is induced in through the induction openings and then is drawn out, circulation reflux of warm and wet air, which tends to occur in conventional cooling towers, can be avoided and therefore increase the efficiency of the water chiller.

Abstract: An atmospheric cooling tower apparatus includes a housing structure having an air inlet and an air outlet, a first evaporative heat transfer media disposed in the housing, and a closed coil heat transfer media disposed in the housing. A water distribution assembly is disposed above the evaporative heat transfer media and configured to distribute water onto the evaporative fill heat transfer fill media. A collection basin is disposed beneath the evaporative heat transfer media configured to collect water that has passed through the evaporative heat transfer media. A first control valve controls an inflow of water to supply water to one or both of the evaporative heat transfer media and the closed coil heat transfer media. The closed coil heat transfer media and the evaporative heat transfer media are disposed laterally next to each other.

Abstract: An improved structure of cooling tower includes a fan housing with a fan disposed therein, induction openings distributed on the fan housing and located below the fan, and a diffuser stack disposed at one end surface of the fan housing. In operation, cold air is drawn into the cooling tower by the fan through inlet openings of the cooling tower so as to exchange heat with the condensing water within a water chiller. When warm and wet air is drawn out of the cooling tower and the warm and wet air outside the cooling tower is induced in through the induction openings and then is drawn out, circulation reflux of warm and wet air, which tends to occur in conventional cooling towers, can be avoided and therefore increase the efficiency of the water chiller.

Abstract: This invention relates to a counter flow type of cooling tower generating low grade of noise, which includes: a body wherein an external air inhalation hole is formed in the lower portion and a discharge hole is formed in the upper portion; a fan that is provided in the body and absorbs external air into the body through an inhalation hole and discharges the external air to the discharge hole; an spraying nozzle that sprays coolant; an eliminator that is provided above the spraying nozzle and prevents air and water from scattering; a filler that is provided below the spraying nozzle; and a collection tank collecting the coolant that passes the filler and drops, wherein a space portion is formed between the filler and the collection tank, and the space portion formed between the filler and the collection tank further includes a noise generation restraining portion consisting of at least one noise generation restraining unit.

Abstract: The convector comprises at least one finned tube bundle (7) in the tubes of which said fluid to be cooled is made to circulate and at least one fan (11) producing an air flow that strikes the outside of said finned tubes. The convector comprises an adiabatic chamber (13) through which said air flow (F1) passes, positioned upstream of the tube bundle (7), inside which water is nebulized and vaporized. The adiabatic chamber (13) is defined by side walls (5) and by at least two evaporation honeycomb fill packs (15, 17).

Abstract: An integrated cooling apparatus and process which includes a source of compressed gas; a cooling unit for cooling the compressed gas to form cooled compressed gas by heat exchange with water having a first purity, thereby producing a stream of cooled compressed gas and a stream of warmed water having the first purity; a first heat exchanger for warming a stream of water having a second purity, the second purity being lower than the first purity, by indirect heat exchange with a stream of water having the first purity; and a conduit for sending cooled water having the first purity to the cooling unit.

Abstract: A method of forming a jacketed steam distribution tube assembly includes simultaneously extruding an inner tube, an outer tube, and a plurality of connecting members for connecting the inner tube to the outer tube, thereby forming a jacketed steam distribution tube assembly.

Abstract: A system is disclosed that incorporates a generator for generating a liquid coolant. This invention provides a self-contained water (or similar liquid coolant) chilling system of suitable capacity to cool small to medium size structures, such as private residences and manufactured homes. The system utilizes an arrangement of heat-exchanging panels to pre-condition an ambient temperature air-stream, prior to passage through a pump-driven coolant spray. The system also provides several sub-systems for automatic coolant monitoring, chemical addition and periodic coolant replacement.

Abstract: A combination mass transfer and pump apparatus, which in a single step actively mixes a first mass and a second mass and simultaneously pumps one of the first mass and the second mass through the apparatus. The combination mass transfer and pump apparatus substantially comprises a housing and at least one distributor element having a plurality of selectively fluid-permeable membrane elements wherein the at least one distributor element is agitated within the second mass such that the first mass diffuses across the selectively fluid-permeable membrane elements, mixing with the second mass, and in the same step the second mass is pumped through the housing.

Abstract: A steam distribution device for a steam humidification system includes a source of steam, a horizontally mounted steam dispersion element for receiving steam from the source of steam and for dispersing a portion of the steam into an air stream, a horizontally mounted jacket partially surrounding the steam dispersion element and unconnected to the source of steam for maintaining the temperature of the steam dispersion element at about the temperature of the steam, the jacket being in flow communication with the dispersion element and receiving steam from the dispersion element, and a condensate collection element separate from the source of steam and connected to the jacket for collecting condensation from the jacket. In a second embodiment, the jacket substantially surrounds the steam dispersion element and is spaced from the dispersion element creating a chamber therebetween. Aligned orifices in the dispersion element and the jacket disperse steam into the air stream.

Abstract: A steam distribution device for a steam humidification system is a source of steam, a horizontally mounted steam dispersion element for receiving steam from the source of steam and for dispersing a portion of the steam into an air stream, a horizontally mounted jacket partially surrounding the steam dispersion element and unconnected to the source of steam for maintaining the temperature of the steam dispersion element at about the temperature of the steam, the jacket being in flow communication with the dispersion element and receiving steam from the dispersion element, and a condensate collection element separate from the source of steam and connected to the jacket for collecting condensation from the jacket.

Abstract: A quench cooler for cooling a hot flowing gas essentially comprises a cylindrical shell (10) which is connected to a hot-gas line (7) and to a cold-gas line (9) and which has means (30) for injecting water. The water injection means (30) are pressure-atomization nozzles to which water and steam are admitted. The steam is generated in an evaporator (17) which is arranged in the hot-air line (7).

Abstract: The invention relates to a heat exchanger wherein the heating vapor is fed onto heat exchange surfaces of membrane material from a vapor distributor, the vapor distributor having parallel conduits for directing vapor over the entire width of the surfaces. According to the invention the vapor distributor is made up of two opposing wall elements which are fastened to each other by means of projections in one element and corresponding recesses in the other element. The upper end of the membrane constituting the heat exchange surface is locked between the projections and recesses that are fastened to each other. Thus, pleats are produced in the membrane as an expansion leeway for the vapor space delimited by the membrane.

Abstract: Leakage in a heat exchanger between two liquids which are in indirect heat exchange relationship is detected by marking one of the two liquids with a colorless chemical marker and detecting it in the second liquid by extraction and conversion to a colored material. The heat exchanger liquids are preferably organic liquids which are immiscible with water. The marker is detected in a heat exchanger liquid by extraction of the marker followed by chemical conversion of the marker to a colored material that can be detected visually. Aminoalkylnaphthalenes are suitable markers which can be extracted by an acidic aqueous solution and converted to a colored material by reaction with a diazotized aromatic amine. Phenylazoalkylphenol derivatives are also suitable markers which can be extracted and simultaneously converted to a colored material with a detection reagent which is comprised of water and a water-soluble amine.

Abstract: A device for monitoring the amount of butane that can be safely added into a fuel gas before condensation occurs includes a dry-bulb thermocouple for measuring the temperature of the gas and a wet-bulb thermocouple for measuring the temperature of a wick soaked in the butane in the gaseous environment of the fuel gas. For a continuous flowing process the difference in the two measured temperatures indicates the proportion of butane that can be added before saturation, and is used to regulate the flow rate of the butane. The wick is periodically flushed with butane, in order to prevent heavy hydrocarbon components in the butane from accumulating.

Abstract: A combined direct and indirect media is disclosed which is formed from a plurality of plate-like structures. The plates are generally sheet-like elements having an indirect portion and a direct portion. The indirect portion includes a first indirect section, a second indirect section, and a hinge disposed between the first and second indirect sections. The first indirect section can be folded about the hinge to place the first and second sections in an opposed relation. The direct and indirect portions are configured to form the direct and indirect evaporative cooling media when a plurality of plates are arranged in an ordered array.

Abstract: Apparatus for the mixing of different streams of air and particularly dry and moist streams of air, in a cooling tower. In order to obtain an effective low-loss mixing over a short flow path by simple means, eddy fields are produced by at least one cylindrical flow body arranged transversely to the direction of flow of one of the streams of air (the main air stream) in the cooling tower as a result of the burbling or separation of the flow on the sides of the body. The transverse components of the eddy fields produce an intensive mixing of the different streams of air.

Abstract: Device for mixing dry and humid air streams of a combined atmospheric cooler employing parallel air streams. The device comprises a wet exchange unit and a dry heat exchange unit which are disposed in parallel in the air stream. The device for mixing the dry and humid air streams comprises surfaces for deflecting the air streams disposed upstream of the wet heat exchange unit and is characterized in that the deflecting surfaces are constituted by at least one channel which is open in the direction of the air outlet of the cooler and which extends in the space located upstream of the wet heat exchange unit. The at least one channel extends from the region in which the humid air stream arrives adjacent the part of the dry heat exchange unit which is the nearest of said region and toward the center of the cooler.

Abstract: Plume formation by exhaust air from wet cooling towers during periods when ambient air conditions are conducive to the formation of such plumes is prevented by preheating inlet air and/or precooling influent hot water to reduce the temperature difference between the air and water and consequently the water content of exhaust air to that which can be absorbed by the ambient atmosphere thus avoiding plume formation.

Abstract: Product gas resulting from the partial oxidation of finely divided fuel in a reactor is discharged as a stream into a tube leading downwardly into a vessel containing a water bath in which the lower end of the tube is immersed. Liquid slag produced during the partial oxidation is also discharged as a solid stream within and surrounded by the stream of product gas. The tube is cooled by circulating cooling water upwardly through an annular clearance in the tube which is discharged from the annular clearance at the upper end of the tube for gravity descent as a liquid film along the inside of the tube. The slag becomes cooled and granulated on contact with the water bath and is discharged from the vessel in granulated condition. The gas escapes from the lower open tube end, travels upwardly through the water bath to become cooled thereby, and is then discharged from the vessel in cooled condition.

Abstract: A method for removing dust and noxious materials from flue gases within a tall chimney through which the dust can be collected efficiently without increasing the operating cost of the boiler. A spraying device assembly is adapted to be mounted in a vertical portion of a chimney so as to save space.

Abstract: A vapor-air humidifier for air climatizing or conditioning installations is disclosed which comprises a double-wall vapor distributor pipe defining vapor exhaust pipe means. By means of a jacket chamber or space, heated by the vapor or steam, the internal space or chamber of the vapor-air humidifier remains free of condensate due to cooling of the air current. The vapor transfered to the air current is thus removed from the internal space which is free of condensate and there is prevented any spraying of water of condensation. Since vapor exhaust elements are arranged along the exhaust pipe means and are distributed over the entire channel cross-section of the humidifier, there is avoided the formation of vapor layers.

Abstract: A generally rectangular, bottom-vented, mechanical draft combination wet-dry water cooling tower is provided which has excellent water conservation properties and resistance to recirculation of heated discharge air, and which is designed for minimizing undue low level deflection and spreading of hot moist discharge air with essentially complete elimination of visible fog plumes above the tower.

Abstract: An installation for changing the temperature of fluid media has a gas-liquid contacting arrangement and an indirect heat-exchange arrangement. The gas-liquid contacting arrangement is made up of a chamber and a device inside the chamber through which liquid may flow to be converted into the form of a spray. A collecting vessel at the bottom of the chamber collects the liquid which passes through the spray device. The wall of the chamber is provided with openings for the admission of a gas into the chamber and louvers may be provided for regulating the flow of gas into the chamber. The indirect heat-exchange arrangement is made up of two portions which are located at a level above that of the spray device and which extend upwardly and outwardly from the vicinity of the wall of the chamber. Each of the heat-exchange portions is constituted by a plurality of parallel conduits provided with fins. Where the installation is used for cooling purposes, the heat-exchange portions may serve as condensers.

Abstract: An adjustably operable heat transfer system for cooling tower installations, the heat transfer units consisting of a section of only "wet" operating evaporative heat exchanger units and a section of dual-purpose heat exchanger units which are adapted for alternative or simultaneous wet evaporative heat transfer and "dry" convective heat transfer. All units are operated in the wet mode, when the air temperatures are highest, for maximum heat transfer output, but a mixed mode is used, when the air temperature is lowest, dry warm air obtained through convective heat transfer being admixed to the moist warm air obtained through evaporative heat transfer, in order to prevent cloud formation by the latter.

Abstract: A wet-dry cooling tower with an upper tubular heat exchange section superposed over a lower sloped film fill section. The film fill comprises a number of spaced sheets, preferably of the corrugated type. Also, splash-type fill may be disposed on either side of the film fill for increased gas-liquid contact. After partial cooling in the upper tubular section, liquid is either directed to the lower film fill section or bypasses it depending on cooling requirements.

Abstract: A cooling tower has circumferentially distributed inlet openings at the lower end for the entrance of cooling air and a central upper outlet opening. Cooling air flows through the tower, on the one hand, counter-currently to a medium to be cooled which flows in downward direction over a trickling unit (wet cooling section), and on the other hand, parallel thereto about heat-exchanger elements, flown through by a medium to be cooled (dry cooling section). The trickling unit and the heat-exchanger elements are separated from each other.