Abstract: This invention provides a system for removing ammonia from landfill leachate. The system comprises: an economiser 22 for producing high pressure hot water in a hot water circuit from heat exchange with a hot gas stream carrying waste heat; a boiler 26 which is heated by the high pressure hot water to produce steam; and an ammonia stripper 32. The ammonia stripper 32 has a leachate inlet 56 connected to a leachate flow path, and an ammonia containing gas outlet 36, at an upper end thereof. A leachate discharge outlet 72 is provided which is connected to a leachate discharge flow path 74, and a steam inlet 70 is provided which is connected to the boiler 26 by a conduit. At a lower end of the ammonia stripper there is a forced air inlet 68. A randomly packed bed 60, 64 located between the upper end and the lower end. In use there is a flow of steam and air in one direction and of leachate in the opposite direction which releases ammonia from the leachate.

Abstract: Embodiments of apparatuses and methods for separating a paraffin isomerization-zone effluent are provided. In one example, an apparatus comprises a DIB column configured for fractionating the paraffin isomerization-zone effluent to form a branched C4 hydrocarbon-rich stream. The DIB column comprises a vessel. The vessel comprises a cylindrical wall that extends vertically and that encloses an internal cylindrical volume having a lower portion extending to an upper portion. An internal swage is disposed in the lower portion of the internal cylindrical volume. A plurality of fractionation trays includes an upper fractionation tray that is disposed in the internal cylindrical volume above the internal swage and a lower fractionation tray that is disposed in the internal swage. The lower fractionation tray has a smaller diameter than the upper fractionation tray.

Abstract: A system and a method for the production and provision of CO2 gas is disclosed. A sealable chamber is equipped with heating means and when sodium bicarbonate is placed in it and heated to its decomposition temperature CO2 gas is released. The released gas is conveyed into liquid within a container and when the pressure of the gas in the container raises more and more CO2 gas is dissolved. The heating may he done by conduction mechanism or by induction mechanism. The sodium bicarbonate or any other material including carbon dioxide may be disposed in powder or solid form. I may be disposed in thin envelope case.

Abstract: A method and apparatus for treating natural gas comprises a contactor having a manifold for spreading gas in the contactor vessel, a plurality of perforated plates above the manifold, a spray system for spraying a treating liquid into an upwardly rising column of gas and a liquid level controller for maintaining the treating liquid above the perforated plates. Gas and liquid from the contactor pass through a cooler and are then separated. A treating liquid regeneration system receives the treating liquid and flashes the liquid at low pressure to separate hydrocarbon gases, hydrocarbon liquid and treating liquid. The treating liquid is regenerated by heating and flashing off contaminant gases and is ultimately redelivered to the contactor.

Abstract: Methods and apparatuses for scrubbing diesel exhaust gases produced on a ship are provided. In an embodiment, a method for scrubbing diesel exhaust gases on a ship includes providing a scrubber vessel formed with a quench zone, a scrubbing zone, and a riser. Water is passed through the scrubbing zone and into the quench zone. The exhaust gases are delivered to the quench zone through the riser and enter the quench zone at a temperature of about 175° C. to about 340° C. The method includes cooling the exhaust gases to a temperature of about 60° C. to about 70° C. in the quench zone by contacting the exhaust gases with the water. The cooled exhaust gases are then scrubbed in the scrubbing zone.

Abstract: A hybrid cooling tower apparatus that extends along a vertical axis is provided. The cooling tower includes a first housing structure having an inlet and a first outlet located a first position along the vertical axis, wherein the housing structure includes a base and opposing side walls that extend along the vertical axis away from the base. The tower also includes a heat exchanger disposed in the housing structure, wherein the heat exchanger is positioned adjacent the first outlet and extends at least partially all the way across the first outlet. Finally the hybrid tower employs an air current generator positioned in a plane normal to the vertical axis and oriented to direct an air stream toward the base and through the heat exchanger and the first outlet.

Abstract: A cooling tower for evaporating water from a brine solution is provided and may include a housing having an air inlet and a brine inlet. The cooling tower may also include a heat-exchange assembly having a heat-exchange media that suspends the brine solution and at least one nozzle in fluid communication with the brine inlet. The at least one nozzle may receive the brine solution from the brine inlet and may transfer the brine solution from the brine inlet to the heat-exchange media to allow the heat-exchange media to transfer moisture from the brine solution to air received from the air inlet to reduce the moisture content of the brine solution.

Abstract: Systems and methods for circulating air in an enclosed environment are disclosed. An inlet can be provided to receive an outside air from outside of the enclosed environment and an air handling unit coupled to the inlet to receive the outside air through the inlet and configured to receive a circulated air from the enclosed environment. The air handling unit can be configured to affect a temperature of at least one of the received outside air and the received circulated air. Based on the received outside air and the received circulated air, the air handling unit can be further configured to generate air for supplying to the enclosed environment.

Abstract: A vaporizing apparatus for generating a process gas from a liquid material includes a vaporizing container defining a vaporizing space of the vaporizing apparatus; an injector connected to the vaporizing container to spray the liquid material in an atomized state into the vaporizing space; and a heater attached to the vaporizing container to heat the liquid material sprayed in the vaporizing space. The vaporizing apparatus further includes a gas delivery passage connected to the vaporizing container to output from the vaporizing space a generation gas generated from the liquid material; a filter disposed inside the gas delivery passage or between the gas delivery passage and the vaporizing space to trap mist contained in the generation gas; and an infrared irradiation mechanism configured to irradiate the filter with infrared rays.

Abstract: The invention relates to a method for creating transient cavitation comprising the steps of creating gas bubbles having a range of bubble sizes in a liquid, creating an acoustic field and subjecting the liquid to the acoustic field, characterized in that the range of bubble sizes and/or the characteristics of the acoustic field are selected to tune them to each other, thereby controlling transient cavitation in the selected range of bubble sizes. It also relates to an apparatus suitable for performing the method according to the invention.

Abstract: A humidifier and humidity sensor for use with a breathing assistance apparatus. The humidity sensor senses absolute humidity, relative humidity and/or temperature at both the patient end and humidifier end. The humidifier may also include provision to both control independently the humidity and temperature of the gases. Further, a chamber manifold facilitates easy connection of the humidifier to various outlets, inlets and sensors. A heated conduit provides a more effective temperature profile along its length.

Abstract: A method of exchanging heat is disclosed. Process fluid is passed through a dry indirect contact heat exchange section while a main air stream is also passed through that section. The process fluid is passed through a second indirect contact heat exchange section while a second air stream is passed through that section. A third air stream is passed through a direct contact heat exchange section and mixed with the second air stream to define the main air stream. Evaporative liquid is selectively distributed over the second indirect contact heat exchange section and over the direct heat exchange section. The distribution of evaporative liquid over one section is independent of the distribution of evaporative liquid over the other section.

Abstract: A method and apparatus for the humidification of gas streams, such as reactant gas streams for fuel cells, wherein the specific water evaporation rate, gas delivery temperature, and degree of gas humidity may be adjusted and maintained at predetermined levels. An ultrasonic device providing a water mist is used in the evaporation process. The amount of water vapor being introduced into the gas stream can be varied up to the saturation point of the reactant gas stream. As the water vapor leaves the evaporation chamber, it mixes with the gas stream in a gas humidification chamber or riser. The humidified reactant gas stream is then maintained at a set point temperature that is at least above the dew point temperature of the humidified reactant gas.

Abstract: The present invention provides a method and apparatus for the humidification of gas streams, such as reactant gas streams for fuel cells, wherein the specific water evaporation rate, gas delivery temperature, and degree of gas humidity may be adjusted and maintained at predetermined levels. The humidification apparatus is well suited for use in testing the operation of a fuel cell under various well-controlled conditions in order to evaluate the performance of the fuel cell. The amount of water vapor being introduced into the gas stream can be varied up to the saturation point of the reactant gas stream. As the water vapor leaves the evaporation chamber, it mixes with the gas stream in a gas humidification chamber or riser. The gas riser preferably has a baffle disposed therein to attract any water that may have condensed in the gas stream and direct the condensed liquid water toward the evaporation chamber so the water may be evaporated once again.

Abstract: In an air feeder for supplying air with a predetermined temperature and humidity into a cup in a resist coating unit provided in a coating and developing system, a cooling section, a by-pass, a heating section, a humidifying section, and a blower are provided. 55% of introduced air is cooled in the cooling section, 45% of the introduced air passes through the by-pass, and mixed air of the cooled air and the air from the by-pass is heated in the heating section and humidified in the humidifying section, thereby enabling energy-saving and space-saving temperature and humidity control.

Abstract: A system and method of exchanging heat are disclosed. Three heat exchange sections are used: a dry indirect contact heat exchange section, a second indirect contact heat exchange section that is operable in either a wet or dry mode, and a direct contact heat exchange section. The three sections are next to each other in an apparatus to reduce the overall height of the apparatus. The dry and second indirect contact heat exchange sections receive a process fluid in series or in parallel. Separate ambient air streams pass through the second indirect and direct contact heat exchange sections before mixing and entering the dry indirect contact heat exchange section. Another ambient air stream is mixed in upstream of the dry indirect contact heat exchange section when the system is operated in the dry mode. Two independent evaporative liquid distribution systems are included. One selectively distributes evaporative liquid over the second indirect contact heat exchange section.

Abstract: An apparatus for vaporizing a liquid material and supplying the material in a gas phase, in which a liquid material for CVD is introduced into a vaporizer at a controlled flow rate, atomized by an ultrasonic atomizing device disposed at the inside or the outside of the vaporizer, heated by a circular flow of a carrier gas and vaporized. When a liquid material for CVD is supplied to a CVD apparatus in the production of semiconductors, the concentration of the material is controlled easily in the vaporization, the concentration of the material in the gas can be changed quickly in response with the change in the flow rate of the material, decomposition of the material does not occur and the operating condition of a CVD apparatus is not restricted.

Abstract: Provided are a system and method for saturating a gas with a vapor from a liquid chemical. The system includes: (a) a saturation vessel connected to receive a liquid chemical and a carrier gas; (b) a gas sparger in the saturation vessel for sparging the carrier gas into the liquid chemical; (c) means for maintaining the liquid chemical in the saturation vessel at a substantially constant level; (d) means for controlling the temperature of the liquid chemical in the saturation vessel to a desired value, comprising (I) a system for cooling the liquid chemical, and (ii) a heater inside the saturation vessel extending vertically in the liquid a distance at least half of the height of the liquid chemical level for heating the liquid chemical; and (e) means for controlling the pressure of the saturated gas to a desired value. The invention also relates to novel methods and systems for controlled delivery of a vaporized liquid chemical.

Abstract: A hybrid cooling plant includes at least one sector with a dry cooling part connected to a feed pump and including at least two heat exchangers which are connected in parallel, and with a wet cooling part located underneath the dry cooling part, wherein the dry cooling part and the wet cooling part are connected to each other by a closed connection. The highest locations of the heat exchangers are connected through a deaerating line to a vacuum pump and the heat exchangers are provided with evacuating and ventilating valves and level limit switches. The deaerating lines of the heat exchangers of a sector which operationally form a unit are connected to a deaerating vessel or reservoir.

Abstract: A carburetor anti-icing apparatus and method for a marine drive is provided for heating a carburetor to a temperature above that at which ice may form in the idle and progression circuits of the carburetor. Several heaters, heat sources, and methods are disclosed for heating the carburetor. In one embodiment an electrical heating element is mounted to the carburetor body near the fuel orifices which make up the idle and progression circuits. In another embodiment, engine cooling water is circulated through a heater housing mounted to the carburetor body. In yet a further embodiment, engine exhaust from the marine drive is conveyed through the heater housing mounted to the carburetor body. A thermally conductive gasket is used to improve heat transfer. The carburetor anti-icing apparatus and method also improves low speed running performance due to the improved fuel vaporization resulting from the increased temperature in the progression circuit.

Abstract: A heat exchange apparatus which can be used as an evaporative condenser, fluid cooler or wet-air cooler, is provided with a direct evaporative heat exchange section overlying an indirect evaporative heat exchange section. An air entry zone common to both heat exchange sections receives an air stream blown into this zone by at least one fan, thereby pressurizing the plenum such that the air stream is forced to split and enter each section while inside the apparatus. This eliminates the need for separate air entries, thus condensing the size and cost of the apparatus, while increasing heat exchange capacity. A countercurrent air flow pattern through the direct section provides a uniformly cooled evaporative liquid for use in the indirect section. The evaporative liquid flow is parallel to the air stream provided in the indirect section.

Abstract: A carburetor anti-icing apparatus and method for a marine drive is provided for heating a carburetor to a temperature above that at which ice may form in the idle and progression circuits of the carburetor. Several heaters, heat sources, and methods are disclosed for heating the carburetor. In one embodiment an electrical heating element is mounted to the carburetor body near the fuel orifices which make up the idle and progression circuits. In another embodiment, engine cooling water is circulated through a heater housing mounted to the carburetor body. In yet a further embodiment, engine exhaust from the marine drive is conveyed through the heater housing mounted to the carburetor body. A thermally conductive gasket is used to improve heat transfer. The carburetor anti-icing apparatus and method also improves low speed running performance due to the improved fuel vaporization resulting from the increased temperature in the progression circuit.

Abstract: A solar dehumidifier which utilizes solar energy to evaporate the moisture in air absorbed by the liquid desiccant and then to make said liquid desiccant denser for reuse. In other words, the humid air is dried in order to be used in a specific area. In particular, the solar dehumidifier according to the present invention is provided with a heat-pipe heat exchanger to increase the evaporation rate of the moisture absorbed by the liquid desiccant.

Abstract: Exhaust gases from a process fired boiler are diverted from a stack prior to emission to the atmosphere through a duct system to a plurality of series connected heat exchangers. The exhaust gases are progressively reduced from an elevated temperature, for example in the range between about 350.degree.-525.degree. F., in stages to an ambient temperature of about 50.degree. F. At each stage heat from the exhaust gases is transferred from the gases to another medium, such as water, which is fed back to the boiler to reduce the energy cost of operating the boiler. At ambient temperature the exhaust gases are subjected to an atomized spray of a reagent solution that absorbs the contaminants in the exhaust gases. Absorption of the contaminants into solution with the atomized reagent spray is promoted by contact of the spray and exhaust gases on the surface of a fibrous batting.

Abstract: The solution-saturation (13,26) is produced in a countercurrent manner under low pressure of the gas (19) in a chlorofluorohydrocarbon (1) which is sprayed (12A,12B), previously compressed (3), and supercooled (5) to a temperature in the neighborhood of or lower than the temperature chosen for the chlorofluorohydrocarbon dissolved gas mixture at the outlet (30), the first gas-liquid chlorofluorohydrocarbon contact being effected by a bubbling (25) under pressure of the gas in the chlorofluorohydrocarbon (26) under conditions of temperature and pressure lower than the critical conditions, with a strict thermal regulation (31) throughout the dissolving stage so as to effect it below the critical conditions, thereafter the chlorofluorohydrocarbon mixture having a high content of dissolved gas is compressed (28A,28B) under high pressure. Application in the chlorofluorohydrocarbon solutions and in particular dichlorodifluoromethane having a high content of carbon dioxide.

Abstract: A process and an arrangement for the formation of an ignitable mixture from iquid fuel and combustion air, wherein preheated combustion air is conducted with a flow chamber along a surface which is moistened with fuel for take-up of fuel. In the process and arrangement, combustion air is conveyed into the flow chamber in the flow direction of the fuel which streams off the surface moistened by the fuel under the effect of gravity. Achieved hereby is an intensive contacting between the combustion air and the fuel. The fuel is dosed in excess so as to constantly afford a sufficient quantity of fuel for vaporization. During the through flow of the combustion air, there is formed, in the contact with the fuel, a saturated fuel-air mixture in conformance with the temperature of the preheated combustion air and the temperature of the fuel.