15 results about "Coalescer" patented technology

Aircraft air cycle machines include a first stage turbine, a second stage turbine that receives air from the first stage turbine, and a duct arranged between the first stage turbine and the second stage turbine. A circular finned coalescer is arranged within the duct and includes a central body, a first fin layer wrapped about the central body, a first parting sheet wrapped about the first fin layer, and a second fin layer wrapped about the first parting sheet. Each of the fin layers include a plurality of fin elements and channels are defined between circumferentially adjacent fin elements of each of the first and second fin layers. The channels are tortuous channels such that moisture carried on a flow through the channels will impinge upon surfaces of the fin elements and coalesce into water droplets.

This invention belongs to the field of wastewater treatment technology, specifically relating to a multi-stage cyclone flotation separator for emulsified wastewater. The multi-stage cyclone flotation separator for emulsified wastewater includes: a coalescer for preliminary separation treatment of the emulsified wastewater; a sludge-water separation chamber connected to the outlet of the coalescer for settling the sludge phase in the emulsified wastewater; a cyclone flotation unit disposed above the sludge-water separation chamber, the inlet of which is connected to the sludge-water separation chamber; an oil-water separation chamber disposed above the cyclone flotation unit, with coalescing packing material disposed between the oil-water separation chamber and the cyclone flotation unit; and an oil collection tank and a water collection chamber connected to the oil-water separation chamber, the oil collection tank being located above the water collection chamber.

Aircraft air cycle machines include a first stage turbine, a second stage turbine, and a duct arranged between the first stage turbine and the second stage turbine. A plate-fin coalescer is arranged along the duct. The plate-fin coalescer includes a housing, a first fin layer arranged within the housing, a second fin layer arranged within the housing, and a first parting sheet arranged between the first fin layer and the second fin layer. Each of the first fin layer and the second fin layer include a plurality of fin elements arranged in substantially parallel orientation relative an axis through the housing, and channels are defined between adjacent fin elements of the plurality of fin elements of each of the first fin layer and the second fin layer. Moisture carried on a flow through the channels will impinge upon surfaces of the fin elements and coalesce into water droplets for removal.

The utility model provides a gas-liquid separation device capable of reducing the gas content in a water electrolysis hydrogen production electrolyte, which comprises a shell, a gas-liquid separation device, a gas-liquid separation device and a liquid storage tank, the shell is provided with an inlet pipeline through which a gas-liquid mixture flows into the shell, and the lower part of the interior of the shell is a liquid collection area; the first separation area is mounted in the shell, and the first separation area comprises a flow dividing assembly used for conducting circumferential flow dividing on the inflowing gas-liquid mixture along the inlet pipeline and a baffle assembly used for converting the flowing direction of the inflowing gas-liquid mixture from the horizontal direction to the vertical direction; the second separation area is arranged in the shell, a rectification coalescer is arranged in the second separation area, and the second separation area is used for rectifying the gas-liquid mixture passing through the first separation area, slowing down the flow speed of the gas-liquid mixture and enabling water vapor and small liquid drops in the gas flowing through the second separation area to be condensed and settled on the rectification coalescer to be removed from the gas; according to the separation device provided by the utility model, liquid flow, liquid drops and water vapor can be separated as much as possible, and the separation efficiency of a gas-liquid mixture is greatly improved.

The utility model relates to an air cooling tower, including the tower body, the first filler layer, cooling water delivery pipe, the second filler layer, refrigerated water delivery pipe and silk screen coalescer are sequentially arranged from below to above in the tower body, and the cooling water delivery pipe and refrigerated water delivery pipe all are provided with the shower head respectively, and the baffle is arranged between refrigerated water delivery pipe and silk screen coalescer, and the return liquid connector is arranged on the tower body of baffle and silk screen coalescer, the first elbow and the second elbow are arranged on the baffle, the included angle of the central axis of first elbow outlet end and the central axis of tower body and the included angle of the central axis of second elbow outlet end and the central axis of tower body all adopt 80 degrees to 90 degrees, and the included angle between the central axis of first elbow outlet end and the central axis of second elbow outlet end adopts 150 degrees to 210 degrees. Realize the use of relatively simpler component structure to convert compressed air into the rotating ascending airflow to realize the water in the airflow preliminary separation. The utility model is convenient to use, and has wide market prospect.

The present disclosure provides a filter-coalescer arrangement, a filter-coalescer device and a coalescer arrangement and a coalescer device for removing solid and liquid contaminants from a gas stream, respectively comprising in sequential series arrangement a pre-filter, an inertial separator comprising a vortex generator and a axial flow separator, and a coalescer; and in sequential series arrangement an inertial separator comprising a vortex generator and a axial flow separator, and a coalescer. Further disclosed are a filter-coalescer system and a coalescer system comprising said arrangement and said device arranged in a pressure vessel, a method of using said device and said system and a method of servicing said system.

This disclosure provides a filter-coalescing arrangement, filter-coalescing device, and coalescing arrangement and coalescing device for removing solid and liquid contaminants from a gas stream, each comprising a pre-filter, an inertial separator including a vortex generator and an axial flow separator, and a coalescing device arranged in series in sequence; and an inertial separator including a vortex generator and an axial flow separator, and a coalescing device arranged in series in sequence. A filter-coalescing system and a coalescing system comprising the arrangement and device arranged in a pressure vessel are also disclosed, as well as methods of using the device and the system and methods of maintaining the system.

The utility model relates to acid jujube saponin depth extraction equipment with foam intercepting device technical field discloses acid jujube saponin depth extraction equipment with foam intercepting device, including the bottom plate, the top of bottom plate is provided with the extraction kettle cylinder, the top of extraction kettle cylinder is provided with the foam intercepting assembly, the foam intercepting assembly includes intercepting frame, inclined coalescer and wire mesh board, through the foam intercepting assembly that sets up, the staff starts motor after, its drive defoaming blade high -speed rotation, utilizes shearing force to break big foam, and the inclined coalescer is designed through the inclination and the flow guide groove, and the middle foam is broken by the collision, and the liquid drop after breaking is backflowed to the extraction kettle cylinder along the flow guide groove, and the top wire mesh board can intercept tiny liquid drop, and through the three -level structure cooperation operation, compared with traditional single intercepting mode, can effectively promote the foam treatment efficiency, significantly reduce the loss caused by saponin overflow with foam.

Filter media are generally described. In some embodiments, a filter media has one or more properties that enhance its suitability for use in coalescer filters. For instance, the filter media may have a particularly low pressure drop and / or may have a particularly high efficiency. In some instances, such properties may be obtained without the inclusion of fluorinated materials, government-regulated substances, and / or toxic substances (e.g., PFAS) in the filter media or with the inclusion of no more than de minimis amounts of such substances.

This invention provides a system and method for extracting coalescing exhaust from an engine. In one embodiment, the system includes an engine, a muffler, and a coalescing exhaust passage, the engine including a crankcase in fluid communication with a coalescing agent, the muffler for receiving combustion exhaust from the engine, and the coalescing exhaust passage fluidly connecting the coalescing agent to the muffler. The coalescing exhaust passage includes an inlet disposed upstream of the muffler, the inlet being adapted to allow kinetic fluid to flow into the coalescing exhaust passage to increase the flow rate of the coalescing exhaust through the coalescing exhaust passage.

The utility model discloses a combined gas purification coalescer, including the casing, be provided with the cylinder in the casing, be provided with centrifugal unit between cylinder and casing, the inside of cylinder is provided with the filler unit and microfiltration unit from below to top, and the gas of entering the casing is purified in proper order through centrifugal unit, filler unit and microfiltration unit, finally discharges through the export of cylinder top, in the application, through setting centrifugal unit to drive the gas movement of entering the casing through the realization gas -liquid spin -off of centrifugal effect, and centrifugal unit is located between cylinder and casing, and the gas of being handled through centrifugation is convenient to contact casing bottom wall after upward movement and enter the cylinder, and realize repeated filtration through filler unit and microfiltration unit in proper order, and gradually filter separation of liquid and other impurities in the gas, thereby improve the gas -liquid separation efficiency of coalescer through combined structure, reach the purpose of energy -conserving, reducing consumption, increasing yield, increasing efficiency.

This invention belongs to the field of synthetic rubber and discloses a method and system for treating exhaust gas from a synthetic rubber production plant. The system includes: a post-treatment unit of the synthetic rubber production plant, a water washing tower, a first booster fan, a first adsorption device, a coalescer, a circulating preheater, a second booster fan, a second adsorption device, a regeneration device, a regeneration condenser, and an oil-water separator. This invention provides a simple, catalyst-free, fuel-free, green, low-carbon, and environmentally friendly method and system suitable for treating the characteristics of exhaust gas from synthetic rubber plants, which can further reduce the energy consumption of synthetic rubber plants.

The utility model relates to filter equipment technical field discloses a coalescence dehydrator, including the filter core and the baffle in the barrel, the baffle includes the upper baffle and lower baffle and is located the upper portion and lower portion in the barrel respectively, and the coalescence cavity between baffle, and the oil outlet chamber between lower baffle and barrel bottom, the filter core includes coalescence filter core and separation filter core, and coalescence filter core top is connected with the barrel through sealing structure, and separation filter core bottom is connected with the barrel bottom through oil outlet pipeline. Through the import sealing end and coalescence filter core joint, when water hydrocarbon mixture enters the upper baffle upper portion in the barrel from the feed pipe, sealing structure can effectively prevent water hydrocarbon mixture from entering the coalescence cavity, can only enter from the import end of coalescence filter core, carries out sufficient filtration to water hydrocarbon mixture, effectively improves water and hydrocarbon separation effect of water hydrocarbon mixture, separates water and hydrocarbon, separates thoroughly, and discharges respectively, removes water in water hydrocarbon mixture, and is convenient for the use of hydrocarbon in the subsequent process.