Abstract: A device for converting a liquid into vapor includes an enclosure, a heating surface with a downward slope arranged in the enclosure, and a liquid inlet port connected to an upper portion of the heating surface so that a liquid introduced from the liquid inlet port flows on the heating surface. The device also includes a vapor outlet port formed through a wall of the enclosure. The heating surface includes a heat transfer pipe configured to allow the flowing of a heat transfer fluid to heat the heating surface, and a corner piece including a U-shaped cross-section with a semi-circular portion arranged around the heat transfer pipe and an upper portion forming an opening on the enclosure.

Abstract: Provided is a method of manufacturing a server room cooling apparatus, the method including: providing a housing; providing at least one frame in the housing; providing, on the at least one frame, a barrier wall configured to divide a space inside the housing into at least two spaces; forming a mist ejection unit configured to eject mist to an outer air supplied from outside the server room cooling apparatus, at a side of a supply unit that is formed by the barrier wall and supplies outer air to a server room; forming a filter unit configured to filter outer air supplied from outside the server room cooling apparatus, at a side of the mist ejection unit; and forming an outer air inflow unit into which outer air flows, at one side of the filter unit.

Abstract: A cartridge-based vaporizer is disclosed. The vaporizer has a body with a control panel and a chamber for receiving a cartridge. A cartridge including a vaporizable product container and an atomizer may be placed in the chamber and selectively secured within the chamber. The body may include a variable air intake in fluid communication with the atomizer when the atomizer is received in chamber. The body may include a cartridge identification sensor configured to identify a cartridge type of the cartridge based on a cartridge identifier of the cartridge.

Abstract: An indirect heat exchanger has two airflow paths and an airflow generator to draw air through the airflow paths. A fluid conduit passes through the heat exchanger such that a cooling region is positioned within each of the flow paths. A dispenser is positioned to dispense evaporative liquid on one of the cooling regions. The dispenser operates in a wet mode and a dry mode. A controller regulates airflow through the first flow path and the second flow path, and also controls the operation of the dispenser. In this way, the controller may operate the airflow paths independently such that the airflow through a flow path operating in the dry mode is greater than that of the flow path operating in the wet mode.

Abstract: A low-temperature distillation facility for distilling a mixed fluid into a pure fluid. An aggregation device has an inlet connected to the vapour space of a supercooling chamber, wherein captured mixed fluid from an evaporator enters the supercooling chamber. The aggregation device's outlet is connected to the vapour space of a superheating chamber, wherein captured pure fluid from a condenser can be sprayed into the superheating chamber. An energy source cools the temperature in the supercooling chamber and heats the temperature in the superheating chamber. A heat exchanger is arranged between the exits of the supercooling chamber and of the superheating chamber. During the process, vapour flows from the supercooling chamber via the aggregation device to the superheating chamber.

Abstract: A method for cryogenic cooling without fouling is disclosed. The method comprises providing a first cryogenic liquid saturated with a dissolved gas; expanding the first cryogenic liquid into a separation vessel, separating into a vapor, a second cryogenic liquid, and a first solid; drawing the vapor into a heat exchanger and the second cryogenic liquid and the first solid out of the separation vessel; cooling the vapor against a coolant through the heat exchanger, causing the vapor to form a third cryogenic liquid and a second solid, the second solid dissolving in the third cryogenic liquid; and combining the second cryogenic liquid and the first solid with the third cryogenic liquid, producing a final cooled slurry. In this manner, the cryogenic cooling is accomplished without fouling.

Abstract: A steam dispersion system includes a header defining a first end and a second end, a plurality of steam dispersion tubes extending upwardly from the header, a condensate drain outlet located at the first end, a hollow pipe positioned within the header, the pipe defining a length extending in a direction generally from the first end to the second end, the pipe defining a main humidification steam inlet located at the first end and a main steam outlet that is within the header. The hollow pipe is configured to receive steam flowing in from the main steam inlet toward the main steam outlet. The pipe may define a plurality of orifices along the length thereof for allowing steam flowing through the pipe to enter the header for distribution through the dispersion tubes. A steam re-direction structure directs steam flow leaving through the main steam outlet back toward the first end of the header.

Abstract: To recover water from a cooling tower exhaust an air entry is provided adjacent thereto which feeds into a cooling heat exchanger. The cooling heat exchanger reduces a temperature of the wet air entering the air entry, causing condensation of water. This condensed water is captured and discharged from the system separate from dry air. A pre-cooler loop can be provided with a pre-cooler heat exchanger upstream of the cooling heat exchanger and fed by a cool line with a cold working fluid drawing heat out of the wet air. The pre-cooler heat exchanger can have its working fluid re-cooled in a second heat exchanger which exchanges heat with the cooler dry air downstream of the cooling heat exchanger. The cooling heat exchanger has a cold fluid passing therethrough which is cooled by a refrigeration system or some other cold fluid source.

Abstract: Methods, apparatus and processes for three phase contacting and reactions in a cross flow reactor with reduced feed vaporization, low pressure operation, higher liquid holdup, lower reactor pressure drop, low severity operation, and reduced product inhibitory effects. A cross flow reactor for three phase catalytic hydroprocessing, having at least one reactor stage is disclosed. The reactor stage has a central gas distributor with perforated lateral surface for distributing gas, a middle region accommodating a packed catalyst bed, and an outer gas space for removal of effluent gases from the middle region. The middle region receives a liquid reactant and gas from central gas distributor to carry out three phase catalytic hydroprocessing reaction.

Abstract: Methods, systems, and devices for humidifying are described herein. One method includes determining a temperature in a space associated with a humidifying unit, determining a relative humidity in the space, determining an air speed associated with the humidifying unit, and adjusting an amount of water sprayed by the humidifying unit based, at least in part, on the temperature, the relative humidity, and the air speed.

Abstract: In one embodiment of a method for vaporizing liquids such as fuels, the liquid is sprayed into a chamber such that the spray does not impinge on any surface. The energy for vaporization is supplied through the injection of a hot diluent such as nitrogen or oxygen depleted air. Additional heat is added through the surface. In another embodiment, the liquid is sprayed onto a hot surface using a geometry such that the entire spray is intercepted by the surface. Heat is added through the surface to maintain an internal surface temperature above the boiling point of the least volatile component of the liquid. The liquid droplets impinging on the surface are thus flash vaporized. A carrier gas may also be flowed through the vaporizer to control the dew point of the resultant vapor phase mixture.

Abstract: A gas generator for health use is provided. The gas generator for health use includes an electrolysis device for electrolyzing water and producing a gas mixture that includes hydrogen and oxygen. The gas generator for health use further includes a gas mixing system coupled to the electrolysis device to receive the gas mixture. The gas mixing system is adapted to mix the gas mixture with water vapor, an atomized medicinal liquid, a volatile essential oil or a combination thereof to produce a health gas for being inhaled by a user.

Abstract: In an anesthesia vaporizer for vaporizing an anesthetic agent liquid and a method of vaporizing an anesthetic agent liquid in an vaporizer, an evaporation unit evaporates the anesthetic agent, a delivery unit intermittently adds a volume of said liquid to the evaporation unit in order to evaporate at least a portion of the volume of the liquid from the evaporation unit. A heat energy storage unit includes a phase change material (PCM) and is thermally coupled to at least a portion of the evaporation unit. The PCM has a phase shift temperature that is higher than the evaporation temperature of the anesthetic agent. The PCM in the heat energy storage unit is preferably at least partly liquid at an operative temperature of the vaporizer.

Abstract: A gas hood for a gas regulator comprises a housing for covering a gas regulator, an opening for receiving the gas regulator and semi-sealing the space between the housing and the gas regulator, and a gas inlet for constantly introducing gas into the space, wherein parts of the gas escapes from the opening so that the space can maintain a micro-positive pressure.

Abstract: A system for supplying vaporized precursor includes an enclosure including an output. A plurality of trays is arranged in a stacked, spaced configuration inside the enclosure. The plurality of trays is configured to hold liquid precursor. A first conduit fluidly connects a carrier gas supply to the enclosure and includes a plurality of openings. A first valve is arranged along the first conduit and is configured to selectively control delivery of the carrier gas from the carrier gas supply through the first conduit to the plurality of openings in the first conduit. The plurality of openings is configured to direct the carrier gas across the liquid precursor in the plurality of trays, respectively. The output of the enclosure provides a mixture of the carrier gas and the vaporized precursor.

Abstract: The present invention provides a humidifying unit, a humidification method, and a humidification system, whereby the efficiency of diffusing water vapor into the air, the absorption amount (absolute humidity), and the water supply utilization can be enhanced.

Abstract: A system for removing gray water from a lavatory or galley area has a container positioned in a floor of the lavatory or the galley. A conduit is provided in flow communication with the container. The conduit is coupled to a ventilation device configured to generate an air flow in the conduit to evaporate the gray water collected in the container.

Abstract: The electrical connections of a chamber or enclosure for a water tub can be protected through the use of spill element sensors. The spill element sensors can help to disable the delivery of power to the heater of a water tub in the event that the electrical connections become wet.

Abstract: Provided is a vaporizer that can efficiently cool a carrier gas, improve the effect of preventing a material from being clogged near the outlet port of a gas passage, contribute to prolonging the timing of maintenance and improving operating efficiency, and exert more uniform dispersing effect. A vaporizer includes: a center rod inserted into a carrier gas introduction hole formed in a disperser to form the gas passage in cooperation with the inner wall of the carrier gas introduction hole; a cooling part disposed on the outer circumferential side of the carrier gas introduction hole in the disperser to cool the inside of the gas passage; a cooling member insertion hole formed across almost the entire length of the center rod along the axial direction of the center rod; and a cooling member disposed in the inside of the cooling member insertion hole to cool the center rod.

Abstract: The invention relates to a method producing a portioned column by forming a first segment and a third segment into arcuate segments, and attaching these arcuate segments to a second z-shaped segment to from two contiguous volumes with approximately semi-circular cross-sections that combine to form a partitioned, approximately cylindrical segment.

Abstract: A system for mixing ortho-xylene with an oxygen-containing gas such as air comprises an evaporator vessel fed with the gas and having a lance projecting into the gas. The lance is provided with a metal spray nozzle for injecting droplets of hot liquid ortho-xylene into the gas stream, concurrently with the direction of flow of the gas. The metal at the surface of the spray nozzle, that in use is in contact with the liquid ortho-xylene, has a high surface hardness to resist erosion, particularly by cavitation. The system is useful in the production of phthalic anhydride by the oxidation of ortho-xylene with air, whereby the risk for deflagrations is reduced. A soft metal seal is the preferred gasket between the spray nozzle and the lance.

Abstract: The Process of Dissolving Air through Pressure/cooling, Into a Fuel Containment (Fuel Tank) Device.

Abstract: Method and apparatus for separating a liquid reaction product from a gaseous stream in a catalytic reactor by means of a metallic sheet being indirectly cooled by a cooling surface and having a plurality of percolations in form of geometric-shaped protrusions on both sides of the sheet each with an open base, the open base is on the side of the sheet facing a catalyst bed are arranged upwards and on the side facing the cooling surface the open base faces downwards.

Abstract: Methods, systems, and devices for humidifying are described herein. One method includes determining a temperature in a space associated with a humidifying unit, determining a relative humidity in the space, determining an air speed associated with the humidifying unit, and adjusting an amount of water sprayed by the humidifying unit based, at least in part, on the temperature, the relative humidity, and the air speed.

Abstract: The present disclosure pertains to a pressure support system configured to provide pressure support therapy to a subject, wherein the pressure support system is configured to determine a volume of liquid held by a humidifier. The liquid volume determination is based on the temperature of the liquid in the humidifier, the temperature of the heater in the humidifier, and/or the temperature of a component of the heater (e.g., a heating element), subsequent to modulation of the rate at which energy is dissipated into the liquid by a heater. Applying a known amount of energy for a known amount of time (power) increases the temperature of the liquid in the humidifier. The amount of liquid in the humidifier can be determined from the applied power and the rise in liquid temperature, heater temperature, and/or heater component temperature over time because the rise in liquid temperature over time is proportional the volume of liquid in the humidifier.

Abstract: A feed liquid flows into a second-stage humidifier chamber to form a second-stage humidifier bath. A first remnant of the feed liquid from the second-stage humidifier chamber then flows into a first-stage humidifier chamber to form a first-stage humidifier bath having a temperature lower than that of the second-stage bath. A second remnant of the feed liquid is then removed from the first-stage humidifier. Meanwhile, a carrier gas is injected into and bubbled through the first-stage humidifier bath, collecting a vaporizable component in vapor form from the first remnant of the feed liquid to partially humidify the carrier gas. The partially humidified carrier gas is then bubbled through the second-stage humidifier bath, where the carrier gas collects more of the vaporizable component in vapor form from the feed liquid to further humidify the carrier gas before the humidified carrier gas is removed from the second-stage humidifier chamber.

Abstract: A cooling tower including a hot-water basin comprising a first cooling cell and a second cooling cell; and at least one means for controlling fluid communication between the first and second cooling cells is provided. A method of maintaining the efficiency of a cooling tower and a method of servicing a cooling tower are also provided.

Abstract: There is provided an aerosol generating system configured to heat an aerosol-forming substrate, the system including an aerosol generating device and a cartridge, a vaporizer configured to heat the aerosol-forming substrate to form an aerosol, at least one air inlet and at least one air outlet. The air inlet and the air outlet are arranged so as to define an air flow route between the air inlet and the air outlet. The aerosol generating system further includes a flow control configured to adjust a size of the at least one air inlet, so as to control an air flow speed in the air flow route.

Abstract: A system for removing gray water from a lavatory or galley area has a container positioned in a floor of the lavatory or the galley. A conduit is provided in flow communication with the container. The conduit is coupled to a ventilation device configured to generate an air flow in the conduit to evaporate the gray water collected in the container.

Abstract: The present invention relates to an apparatus and method for an air bypass system for a natural draft cooling tower that employs a wet heat exchanger, a direct dry heat exchanger or an indirect dry heat exchanger to extract heat from a heated fluid, which is usually liquid or steam.

Abstract: The present invention relates to a humidifier and a method of monitoring the water level in the humidifier, the method comprising the steps of: detecting the temperature at the air outlet of the humidifier and generating temperature signals indicating the temperature thereof (310, 410); determining the water level in the humidifier according to the generated temperature signals (330, 430). The water level in the humidifier can be monitored using a rather simple structure yielding a high accuracy.

Abstract: The present invention relates to an apparatus and method for an air bypass system for a natural draft cooling tower that employs a wet heat exchanger, a direct dry heat exchanger or an indirect dry heat exchanger to extract heat from a heated fluid, which is usually liquid or steam.

Abstract: A system, apparatus and method for concentrating a solution. The system includes a humidification device and a solution flow path for flow of a solution to be concentrated to the humidification device. The humidification device includes humidification media to facilitate evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution. The method includes flowing a solution to be concentrated along a flow path to a humidification device including humidification media, flowing a gas through the humidification media, and flowing the solution to be concentrated through the humidification media. There is evaporation of liquid from the solution to the gas as the solution passes through the humidification media thereby concentrating the solution and producing a humidified gas. The solution to be concentrated may be salt water and the gas may be air.

Abstract: A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section is comprised of a series of serpentine tubes, and an evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section. An improved heat exchange apparatus is provided with an indirect evaporative heat exchange section consisting of a series of serpentine tubes comprised of tube runs both of normal and increased height between tube runs A direct heat exchange section may be provided in the increased vertical spacing between tube runs A secondary spray distribution may also be provided in the increased vertical spacing between tube runs.

Abstract: A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section is comprised of a series of serpentine tubes, and an evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section. An improved heat exchange apparatus is provided with an indirect evaporative heat exchange section consisting of a series of serpentine tubes comprised of run sections return bend sections of both normal and increased height. A direct heat exchange section may be provided in the vertical spacing between run sections formed by the increased height return bends.

Abstract: A steam dispersion apparatus includes a steam chamber communicating in an open-loop arrangement with a first steam source for supplying steam to the steam chamber. The steam chamber includes a steam dispersion location at which steam exits therefrom at generally atmospheric pressure. A heat exchanger communicates in a closed-loop arrangement with a second steam source for supplying steam to the heat exchanger at a pressure generally higher than atmospheric pressure. The heat exchanger is located at a location that is not directly exposed to the air to be humidified, the heat exchanger being in fluid communication with the steam chamber so as to contact condensate from the steam chamber. The heat exchanger converts condensate formed by the steam chamber back to steam when the condensate contacts the heat exchanger.

Abstract: A humidity generator and method for setting operating parameters of the humidity generator to controllably generate humidity levels below 100% and greater than 100%.

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: A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.

Abstract: A steam distribution apparatus having a heat exchanger header defining a chamber; steam distribution apparatus communicating with the heat exchanger chamber; a source of steam at a pressure higher than atmospheric; a heat exchanger having one end communicating with the source of steam and another end for communicating with the chamber and steam dispersion apparatus; and a valve. The valve operates the heat exchanger in an open-loop configuration which supplies humidification steam to the steam distribution apparatus at atmospheric pressure and operates the heat exchanger in a closed-loop at the steam pressure higher than atmospheric for heating the heat exchanger chamber wherein condensate within the chamber or steam distribution apparatus can be converted back to humidification steam.

Abstract: A portable appliance includes a humidifier and a heated scent mechanism. The heated scent mechanism includes a scent generator that harvests excess heat produced by a liquid heating chamber, or heat produced as a byproduct of motor operation. The humidifier may be controllable such that the appliance can serve as either a humidifier or air-freshener, individually or simultaneously.

Abstract: An indirect evaporative cooler wherein the exhaust air from the wet passages is drawn directly from the wet passages by a first fan (66) while a second fan (64 or 42) powers the movement of air to be cooled through dry passages of the cooler.

Abstract: A method directed to reducing mineral buildup on drift eliminators of a cooling tower by allowing irrigation of the drift eliminators of the cooling tower with fluid in the basin of the cooling tower to reduce mineral buildup.

Abstract: A cooling tower with a hot water distribution system includes a distribution lateral disposed above a hot water basin. The distribution lateral discharges fluid into the hot water basin, which in turn, releases the fluid through a plurality of orifices. As the fluid is released, it falls on heat-exchanging fill material that assists in increasing the cooling rate of the fluid. The distribution lateral is configured structurally to discharge the fluid through a plurality of outlets at one or more angles (as compared to the horizontal) into the hot water basins. In one embodiment, the outlets are arranged into one or more rows that extend along a substantial length of the distribution lateral. Discharging the fluid in this manner enhances and promotes a more even fluid flow within the hot water basin, which results in a more even fluid flow over and onto the fill material, thereby increasing thermal efficiency.

Abstract: A system and method for separating a fluid mixture is provided which employ vacuum distillation apparatus, and optionally, gas-handling apparatus operable to introduce a gas into the liquid mixture prior to being dispersed within the vacuum distillation apparatus. The liquid mixture is dispersed within the vacuum distillation apparatus as micro-sized droplets. When used, the gas that has been introduced into the liquid mixture is rapidly liberated from the micro-sized droplets thereby causing the droplets to break into still smaller droplets thereby maximizing the vaporization of the more volatile components in the liquid mixture.

Abstract: An aircraft humidifier is engineered as a stand-alone, fully integrated aircraft humidifier that is suitable for providing uniform, non-wetting humidified air disbursed by the aircraft humidifier into ambient air to increase the relative humidity in low humidity environments such as aircraft interiors, including cockpits, cabins, crew rests, cargo holds, and lavatories as well as any other enclosed areas.

Abstract: A system for providing positive pressure to an interior of a positive pressure facility can include an enclosure for securing to an exterior of the positive pressure facility, an evaporator motor compartment with a motor, a compressor compartment with a compressor, a fresh air intake section for bringing air in from outside, a condenser compartment with air venture, a heater compartment with a heater, and an enclosure extension for attaching to the interior of the positive pressure facility. An electrical compartment can be connected with a return air compartment of the enclosure extension. A human machine interface with a display can present controls for controlling the system and various portions of real-time information related to the system.

Abstract: An air cooled condenser apparatus has a tubular shell having an open upper end and an open lower end, a ring of tube bundle panels disposed generally vertically and at an angle to each other, with each of the tube bundles comprising a primary condenser region and a secondary condenser region, and adapted for air flow therethrough to condense fluid in the panels, and configured so that air flow through the panels passes through and exits the open upper end of the shell, and a duct disposed at the ground level of the shell, and a non-condensable extraction system with active or passive devices to control the local rate of the evacuated mixture of non-condensables and attached steam.

Abstract: Contemplated configurations and methods are drawn to systems in which gas assisted spray nozzles are used to distribute a liquid phase in micron-sized droplets in a device effluent at a position upstream of a second device having multiple parallel flow paths for the effluent. Most preferably, the assist gas is a high-pressure gas phase that is generated in a process upstream of the device effluent, the first device is a hydrotreating or hydrocracking reactor or distillation column, and the second device is an air cooler or heat exchanger.

Abstract: Device (10, 110) for evaporating a liquid, includes: a reservoir (14) containing the liquid; an organ for absorbing the liquid (16); and an organ for producing a gas flow (18), which is directed towards the absorption organ (16); characterized in that the absorption organ (16) includes a plurality of absorbent strips (24) suited to retain the liquid.