Abstract: The present disclosure is drawn to evaporation panel assemblies, systems, and methods. For example, a modular evaporation panel system can include a plurality of evaporation panels with individual evaporation panels including evaporation shelves that are laterally elongated, vertically stacked, and spaced apart; vertical support columns positioned along the evaporation shelves to vertically support and separate the evaporation shelves; female-receiving openings defined by multiple evaporation shelves and multiple support columns; and male connectors positioned at lateral ends of the evaporation panels. The male connectors can be releasably receivable by the female-receiving openings of an adjacent evaporation panel, thereby providing modular assembly and disassembly of multiple evaporation panels relative to one another.

Abstract: The present disclosure evaporation panel systems including plurality of evaporation panels, wherein a first evaporation panel and a second evaporation panel of the plurality of evaporation panels each include evaporation shelves and support columns to support and separate to the evaporation shelves. At least a portion of the support columns include evaporation fins so that wastewater is loadable along the support column. The first evaporation panel and the second evaporation panel in this example are releasably connectable to one another to form a sub-assembly.

Abstract: A convector for air cooling of a fluid flowing in a pipe, comprising: a path for a cooling air flow comprising an inlet from and an outlet towards the environment, a heat exchange section comprising at least one tube bundle defining a heat exchange surface, said section being provided in said path for the air flow, fan means producing said air flow along said path, so that said air flow externally invests said tube bundle on said; heat exchange surface, a humidifying section arranged in said path, upstream of said heat exchange section, where water is atomized to be invested by the air flow, characterized by comprising a wetting device for wetting directly with water a portion of the heat exchange surface of said tube bundle to further cool said portion of tube bundle.

Abstract: An evaporation panel can include a first evaporation shelf including a first upper surface and a first lower surface, a second evaporation shelf positioned beneath the first evaporation shelf and having a second upper surface, and a support column disposed between the first evaporation shelf and the second evaporation shelf. In this example, the support column can include an evaporation fin.

Abstract: Embodiments for controlling condensate in a charge air cooler are provided. In one example, a charge air cooler comprises an inlet to admit charge air, a plurality of heat exchange passages to remove heat from the charge air, an outlet configured to discharge the charge air from the heat exchange passages to an intake passage upstream of an intake manifold of an engine, and a dispersion element extending at least partially across the outlet.

Abstract: A liquid distributor is used as an internal column component for a defined distribution of a liquid flowing downward within a column. The liquid distributor includes at least a bottom and side walls which constitute a container for the accommodation and defined distribution of the liquid. The bottom and at least one of the side walls are constructed from panels that are connected to each other. The panel or panels of the at least one side wall include a fiber composite material. A column and a method for separating substance mixtures are also provided.

Abstract: A filter module for the separation of overspray from overspray-laden cabin air of coating plants, in particular of painting plants, having a filter housing which delimits a filter chamber through which overspray-laden cabin air can be conducted in a main flow direction. A plurality of separation elements composed of a separation material which is permeable to the cabin air is arranged in the filter chamber such that a flow labyrinth is formed between the separation elements. A separation device and a plant for coating articles having such a filter module is also provided.

Abstract: Process and device for dispersing gas in a downward flow of liquid, according to which the liquid is distributed along at least one jet (A) directed downwards, preferably along a plurality of jets; gas is distributed radially (F) towards the liquid jet or jets in order to be entrained by the liquid; and the liquid-gas mixture is channeled into a downflow vertical tube (P).

Abstract: A screen-free, liquid-based lint collection system is disclosed. The system comprises an initial air-lint conduit. The air-lint conduit is coupled to a lint collection reservoir. The system further comprises a spray assembly and a sensor. The spray assembly is configured to spray a liquid into the lint-collection reservoir. The sensor monitors the level of the liquid collected in the lint-collection reservoir.

Abstract: The present disclosure evaporation panel systems including a plurality of evaporation panels. The evaporation panels can include a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented; and a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves. The evaporation panels can also include a plurality of female-receiving openings which are individually bordered by two evaporation shelves and two support columns; and a plurality of male connectors positioned at lateral ends of both the first evaporation panel and the second evaporation panels. The first evaporation panel and the second evaporation panel can be orthogonally connectable via the male connectors of the first evaporation panel and the female-receiving openings of the second evaporation panel.

Abstract: An arrangement of downcomers oriented at a 45-degree angle to a support that is either a wall within a divided wall column or a support beam that allows for reduced spacing of from 0.3 to 0.76 m spacing between trays within a distillation column. The advantages include the use of a single support beam to support two trays as well as more efficient operation and allowing for columns having diameters from 0.9 to 15.2 meters.

Abstract: The present disclosure relates to a modular heat exchange tower including a first module having a first basin disposed therein and a second module having a second basin disposed therein. The aforementioned modular heat exchange tower may also include heat exchange sections, which are disposed in the first module and the second module. The first module and the second module may be assembled prior to being transported to a job site and installed in the modular heat exchange tower.

Abstract: A packing structure obtained by assembling packing elements having a spiral helix shape, and the use of a structured packing composed of packing structure for an operation for bringing a gas into contact with a catalyst, and a process for manufacturing such a structured packing.

Abstract: Evaporation panel securing system can include first and second evaporation panels, and a security fastener to secure a male connector (first evaporation panel) within a female-receiving opening (second evaporation panel) in an orthogonally joined orientation, for example. The evaporation panels can include a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented; a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves; a plurality of female-receiving openings individually bordered by two evaporation shelves and two support columns; and a plurality of male connectors positioned laterally at ends of the plurality of evaporation panels, wherein the male connectors of the first evaporation panel are releasably joinable with female-receiving openings of the second evaporation panel.

Abstract: A splash bar for use in a cooling tower includes bottom, top, first side and second side portions. The bottom portion has first and second edges and is configured to be supported by horizontal hanger support members of a splash bar hanger grid along a width between the first and second edges. The top portion has first and second edges and is arranged substantially parallel with the bottom portion. The first side portion extends from the first edge of the bottom portion to the first edge of the top portion and the second side portion extends from the second edge of the bottom portion to the second edge of the top portion. The first and second edges of the top portion are closer to one another than the first and second edges of the bottom portion. A plurality of openings are formed through each portions.

Abstract: A ventilation and noise reduction system for centralized cooling towers includes a wind outlet sound-reduction structure, a wind inlet sound-reduction channel, a rainwater collection system, and an arrestor device; wherein the integrated sound-absorbing and sound-insulation shed includes a loading-bearing installation structure for a lifting ring, a concrete foundation, a bearing support structure, a ceiling installation structure, a sound-insulation structure and a lighting and sound-insulation structure.

Abstract: An integrated steam cycle power module (100) comprising a steam turbine (102) arranged to have steam supplied thereto; a steam manifold (104) arranged to have exhaust steam from the steam turbine supplied thereto; at least one heat exchanger (108) arranged to have exhaust steam supplied thereto from the manifold via risers which connect the manifold to headers (117) associated with the heat exchangers; and having the steam turbine situated below the steam manifold and arranged, in use, to vent exhaust steam to the manifold, which exhaust steam is passed to the heat exchanger in order to have heat extracted therefrom. Substantially all of the equipment required can be integrated into a compact module reducing plot space, overall costs and assembly time on site or allowing the module to be fabricated off site. The heat exchanger may be arranged to form substantially planar, substantially vertical walls along the side regions of the module.

Abstract: A fill support frame for an evaporative cooling tower includes a plurality of horizontal framing members, a plurality of columns, and a plurality of rails disposed on the horizontal framing members. The plurality of rails are configured to engage a plurality of slide members of a fill module.

Abstract: A support for a packing column having a support profile with a web section running in the vertical direction and having lower end and an upper end, and having a larger vertical extension than a horizontal extension. The support also has a foot section connected to the upper end of the web section and a head section connected to the lower end of the web section. The head section has an upper face and a sub-section, the width of the upper face being smaller than width of the sub-section and also smaller than the width of the foot section. The support enables a reduced support height and less coverage.

Abstract: A fill in a rectilinear evaporative cooling tower includes a grid, grid support, module radial support, module column and module girts. The grid is to support a plurality of splash bars. The grid support is configured to provide support for the grid. The module support is configured to provide support for the grid support. The module column is configured to provide support for the module support. The module girts is configured to rest on a fill support frame of the rectilinear evaporative cooling tower and configured to provide support for the module columns.

Abstract: A combined fluid collector and redistributor for a process engineering column, including a fluid collector for collecting a first fluid; a fluid redistributor arranged below the fluid collector to define a space between the fluid collector and the fluid redistributor; at least one pipe passing through the space to connect the fluid collector to the fluid redistributor; and at least one conduit extending through the fluid collector to permit a second fluid to flow through the fluid collector. There is at least one deflector in the space, wherein the at least one deflector is set at an angle relative to a central axis of the device whereby flow of the second fluid within the space is displaced angularly around the central axis.

Abstract: An apparatus includes a set of atomizers, a housing and a separator. Each atomizer includes an inlet portion that receives an inlet flow of a solution and an outlet portion that produces an atomized flow of the solution. The housing defines a flow path. Each atomizer is disposed at least partially within the housing such that the outlet portion of each atomizer is in fluid communication with the flow path. The housing is configured such that a gas flowing within the flow path can be sequentially mixed with the atomized flow of the solution produced by the outlet portion of each atomizer to produce a mixture of the gas and the solution. The separator produces a first outlet flow including a portion of the gas and a vaporized portion of a solvent, and a second outlet flow including a liquid portion of the solvent and a solute.

Abstract: The present disclosure relates to a modular heat exchange tower having a first module that includes a first basin disposed therein and a second module having a second basin disposed therein. The aforementioned modular heat exchange tower may also include heat exchange sections, which are disposed in the first module and the second module. The first module and the second module may be assembled prior to being transported to a job site and installed in the modular heat exchange tower.

Abstract: A separator apparatus is provided for a cutting machine which separates chips from coolant, wherein the separator includes a fluid chamber into which an airborne mixture of chips and coolant driven by an airflow enters via an entry port, the separator apparatus being configured to: sufficiently slow the speed of the airborne mixture once inside the chamber so that the chips and coolant separate out from the airflow; retain the chips and coolant released from the airborne mixture in the fluid chamber; and allow air from the airborne mixture to exit the fluid chamber via an air outlet; wherein the fluid chamber includes a chip collector which captures the chips and enables the chips to be separated and removed from the coolant in the chamber; and wherein the fluid chamber includes a coolant outlet through which coolant, from which the chips have been removed, is able to exit.

Abstract: Provided is a gas separation apparatus advantageous in suppression of increase in pressure loss and achievement of reduced size and weight, thereby reducing costs. The gas separation apparatus causes an absorbent to flow down along the surface of a packing arranged in a treatment chamber, and supplies to the treatment chamber a gas to be treated which contains a target gas component, and then causes the gas to be treated and the absorbent flowing down along the surface of the packing to come into gas-liquid contact. Thus the target gas component contained in the gas to be treated is absorbed into the absorbent and separated or recovered from the gas to be treated. The packing has at least one packing unit configured by a plurality of expanded metal plates standing vertically and being aligned.

Abstract: The invention relates to contactors suitable for use, for example, in manufacturing and chemical refinement processes. In an aspect is a hybrid indirect/direct contactor for thermal management of counter-current processes, the contactor comprising a vertical reactor column, an array of interconnected heat transfer tubes within the reactor column, and a plurality of stream path diverters, wherein the tubes and diverters are configured to block all straight-line paths from the top to bottom ends of the reactor column.

Abstract: A contact and separation column (1) encasing a stack of one or more contact and separation cells (3). Each cell comprises: —a tray (4) with gas flow openings (6) opening into contact and separation units (7); —a downcomer (16) defining a liquid discharge; and —a liquid supply (17). Each contact and separation unit (7) comprises an upstream contact zone (8, 9) with liquid inlets (12), and one or more downstream separation zones (10) provided with a swirler (13) and a top end with a gas outlet (14). The swirler (13) is located at a distance from the gas inlet of from 50 to 90 % of the total length of the contact and separation zone. Process for treating a gas with such a column.

Abstract: A liquid collection trough assembly for a cooling tower, condenser or dephlegmator includes a plurality of elongate troughs and associated inclined capture plates arranged to receive liquid on a front face thereof and direct the liquid into an associated elongate trough. Each capture plate has a generally upright deflection plate extending downwards from an upper region on its rear face so as to be capable of receiving liquid droplets contacting it and directing such liquid into or onto an adjacent trough or capture plate, in use. The deflection plate extends downwards to terminate in a bottom edge that is located downwards of the upper region of the capture plate and spaced rearwards of the rear face of an inclined portion of the capture plate.

Abstract: The invented system used in wet cooling tower, restore outlet fog of cooling tower into collection basin and consequently cooling water cycle. This invention consists of three main components; pump and its pertaining piping, waterfall and micron fog eliminator. In the first stage, the air containing fog is passed through a waterfall before exhausting. This action causes some portions of fog to condensate and fall down, remaining droplets of the fog grow and together with air cross the fog eliminator blades. Fog's droplets are entrapped between blades, leave the air, and restore to the tower. Therefore, humidity of exhausted air from tower will be effectively reduced.

Abstract: A vertical scrubber (1) for exhaust gas from a marine vessel is described. An exhaust gas tube (2) is substantially coaxially arranged through the bottom of a lower scrubbing chamber (3) and is released though an exhaust gas outlet (20) being coaxially arranged through the top of an upper scrubbing chamber (13). A lower scrubbing chamber deflection body (4) is arranged above the opening of the exhaust gas tube (2) for redirecting the exhaust gas towards the walls of the scrubber and create turbulent gas flow, where one or more lower chamber water injector(s) (6, 6?) is (are) arranged above the lower scrubbing chamber deflection body (4), to introduce scrubbing water, and where a lower chamber exhaust gas outlet (12) is arranged at the top of the lower scrubbing chamber (3) as a coaxial constriction, for withdrawing the partly scrubbed exhaust gas from the first scrubbing chamber and introducing the gas into the upper scrubbing chamber (13).

Abstract: The present disclosure relates to modules for heat exchange for use in cooling towers and methods of assembling cooling towers using such modules. The aforementioned modules for heat exchange may include fill packing and a structural system configured to provide support for at least the fill packing, in which the structural system includes a plurality of structural members configured to provide compression and tension support. The aforementioned modules for heat exchange may be assembled prior to being transported to a job site and installed in a cooling tower. A method for assembling a cooling tower using the aforementioned modules for heat exchange includes: constructing a cold water basin; assembling an air inlet structure on the cold water basin; and placing a heat exchange module on top of the air inlet structure.

Abstract: Disclosed herein is an assembly for selectively aerating a liquid including a base member a reservoir adapted to receive the liquid. The assembly also includes a support member non-rotatably coupled to the base member and a diverter member coupled to the support member and rotatable between a first diverter position and a second diverter position. The diverter member has at least one primary aperture and at least one secondary aperture. The assembly additionally includes an aerator member non-rotatably secured to the diverter member, the aerator member having an aeration aperture. In the first diverter position, a portion of the liquid in the reservoir flows through the primary aperture. In the second diverter position, a portion of the liquid in the reservoir flows through the secondary aperture, and though the aeration aperture.

Abstract: A cost-effective cooling tower splash fill bar support assembly that includes a plurality of perforated substantially planar components supporting a plurality of splash fill bars extending therethrough in a manner that distributes stress over a relatively large area, typically by using a splash fill bar support. Also, a method of forming a cooling tower splash fill bar support assembly including a splash fill bar support assembly having substantially planar components and splash fill bar supports.

Abstract: A fill assembly for evaporative cooling includes a plurality of splash bars, a grid to support the plurality of splash bars, and a pivot connection at an intersection between the grid and a splash bar of the plurality of splash bars. The fill assembly is configured to translate from an upright conformation to a compact conformation in response to the plurality of splash bars pivoting relative to the grid.

Abstract: A reactor for carrying out a three-phase reaction of a liquid phase, a gaseous phase, and a catalyst over a fixed catalyst bed is disclosed. The liquid and gaseous phases are passed through the reactor via a mixing and distribution device positioned over the fixed catalyst bed. The mixing and distribution device includes a trough distributor for the liquid phase, having trough-shaped channels, outlet tubes in the trough-shaped channels for the liquid phase, a distributor plate below the trough distributor, and vertical nozzles, having one or more openings for the gaseous phase and one or more openings, arranged below the openings for the gaseous phase. For entry of the liquid phase, the nozzles are installed so that, at a predetermined liquid feed rate, the surface of the liquid on the distributor plate is below the openings for the gaseous phase and above the openings for the liquid phase.

Abstract: A fill assembly for evaporative cooling includes a plurality of splash bars, a grid to support the plurality of splash bars, and a pivot connection at an intersection between the grid and a splash bar of the plurality of splash bars. The fill assembly is configured to translate from an upright conformation to a compact conformation in response to the plurality of splash bars pivoting relative to the grid.

Abstract: A cooling tower with a plurality of fill packs has a fire stop with openings disposed below the fill packs, a water distribution system for distributing water onto the fill packs, and a cold water basin disposed below the fire stop for collecting water which has past through said fill packs. The openings in the fire stop occupy at least 80% of the area over which the fire stop extends. The fire stop is made of an intumescent material with an expansion ratio sufficient to close said openings when said material intumesces.

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 splash grid is provided for installation in a rain zone of liquid gas contacting industrial equipment. The splash grid has a supporting frame assembly and multiple generally parallel elongate elements supported by the frame assembly. The elongate elements each has a transverse dimension, in plan view, not exceeding 3 mm, and a spacing in plan view not exceeding 10 mm. The elongate elements may be of a molded plastic material that is optionally integral with a surround that forms, or is attached to, the supporting frame assembly. Alternatively, the elongate elements may be separately manufactured flexible filament or cord supported by a surround that forms or is attached to the supporting frame assembly. The elongate elements may be staggered in the vertical direction and gaps may be provided for larger objects to pass through the splash grid. A liquid cooling installation having a rain zone fitted with a splash grid is also provided.

Abstract: A grid panel includes a generally elongated, rectangular main panel section having a plurality of main panel section corners: a pair of generally elongated, rectangular end panel sections extending from the main panel section beyond the main panel section corners, each of the end panel sections having a plurality of end panel section corners; a plurality of grid notches between the main panel section corners and the end panel section corners, respectively; and a plurality of grid openings in the main panel section and each of the end panel sections.

Abstract: Disclosed herein is an aerator for effectively aerating a liquid. The aerator comprises a body having a first opening and a spout defining a fluid flow path of the liquid. A spray head disposed in the fluid flow path having a plurality of spray openings mixes and aerates the liquid with the air from the air inlet as the liquid is sprayed out through the spray openings. The aerator may also contain an angled head portion to allow the aerator to be attached to a bottle.

Abstract: Disclosed herein is an aerator for effectively aerating a liquid. The aerator comprises a body having a first opening and a spout defining a fluid flow path of the liquid. A spray head disposed in the fluid flow path having a plurality of spray openings mixes and aerates the liquid with the air from the air inlet as the liquid is sprayed out through the spray openings. The aerator may also contain an angled head portion to allow the aerator to be attached to a bottle.

Abstract: The present invention provides a method and apparatus for the treat en of process gas from an anaerobic digestion system or a landfill gas system. In one embodiment, the system comprises a caustic scrubber including a vertical column having a top and a bottom and including a counter current flow system, wherein a process gas stream flows up vertically through the column in counter current flow to a caustic liquid solution that flows downward through the column.

Abstract: There is disclosed a non-electric portable manually operated misting fan assembly which is formed by a handle for allowing the user to grasp and manipulate the fan assembly, the handle formed by a container adapted to function as a reservoir for a supply of fluid and having an upper end which includes a pump assembly including a pump head extending upwardly therefrom for pumping fluid from the handle container through a fluid nozzle located in the pump head. The fan means are fixedly mounted on the handle and positioned above the pump head, the fan means bounded by an upper end and a lower end, the lower end being accurately formed over the pump head in order to allow the user to position his finger on the pump head to manipulate the pump in order to eject a fluid from the fluid reservoir incident to the fanning procedure.

Abstract: There is disclosed a non-electric portable manually operated misting fan assembly which is formed by a handle for allowing the user to grasp and manipulate the fan assembly, the handle formed by a container adapted to function as a reservoir for a supply of fluid and having an upper end which includes a pump assembly including a pump head extending upwardly therefrom for pumping fluid from the handle container through a fluid nozzle located in the pump head. The fan means are fixedly mounted on the handle and positioned above the pump head, the fan means bounded by an upper end and a lower end, the lower end being accurately formed over the pump head in order to allow the user to position his finger on the pump head to manipulate the pump in order to eject a fluid from the fluid reservoir incident to the fanning procedure.

Abstract: A mist generating system for a cleaning implement is adapted to generate a finely atomized liquid mist for suppressing dust, allergens, and other airborne particulates. The mist generating system can be adapted to fit many cleaning implements such as vacuum cleaners, wet extraction cleaners, floor mops, and dusters to suppress airborne dust and particulates generated during operation and the cleaning process.

Abstract: The invention is a fluid distribution device for coupling with a fluid distribution conduit or chimney for improving the distribution of downwardly flowing poly-phase mixture including at least one gas phase and at least one liquid phase, above at least one catalyst bed of granular solid catalytic material. The fluid distribution device for receiving the liquid and gas phases has one or more openings in the top and/or upper portion of its height through which a gas phase can enter and has a gas conduit that opens to a mixing cavity within the device. The fluid distribution device further comprises one or more lateral openings for liquid ingress. The lateral opening or openings allow the liquid to enter a liquid conduit that opens to the internal mixing cavity. The mixing cavity allows intimate contact between the liquid and gas phases. Therefore the flow distribution device of the invention provides improved tolerance for tray out of levelness.

Abstract: Apparatuses, methods and systems directed to reducing mineral buildup on drift eliminators of a cooling tower. Some embodiments of the invention allow irrigation of the drift eliminators of the cooling tower with fluid in the basin of the cooling tower to reduce mineral buildup. In other embodiments, the systems disclosed can be integrated with the drift eliminators to provide constant irrigation of to reduce mineral buildup. In some other embodiments, a control unit is used to selectively irrigate the drift eliminators based on the fluid temperature in the basin and the temperature inside and outside of the cooling tower.

Abstract: A cooling tower or, in alternate operation an evaporative condenser, is provided having a dry sensible or indirect heat exchange section and an evaporative heat exchange section. The dry sensible section includes a coil circuit through which a liquid to be cooled passes. The evaporative section is below the dry sensible section and may include a coil circuit or fill sheets. Modulating louvers are provided to allow the air flow and accordingly the evaporative loading to be varied between the dry sensible section and the evaporative section.

Abstract: An apparatus for mixing a liquid with a large gas stream flowing in a gas duct, especially for introducing reducing agent into flue gas containing nitrogen oxides. At least one metering lance having at least two atomizer nozzles supplies liquid to the gas stream, with the nozzles being inclined relative to the direction of flow of the gas stream and being inclined in opposite directions relative to one another. At least one disk-shaped mixer element is associated with and spaced from the nozzles, and is inclined relative to the direction of flow of the gas stream. Flow eddies form at the mixer element, and at least a portion of the liquid enters the flow eddies. Atomization is effected in such a way by the mixer element that volatilized gaseous portions in the nozzle streams exiting the nozzles enter the flow eddies, while non-volatized droplet portions, due to their inertia and an atomizer angle, do not enter the flow eddies in the vicinity of the mixer element.