Omniphilic and superomniphilic surfaces for simultaneous vapor condensation and airborne liquid droplet collection are provided. Also provided are methods for using the surfaces to condense liquid vapor and/or capture airborne liquid droplets, such as water droplets found in mist and fog. The surfaces provide enhanced capture and transport efficiency based on preferential capillary condensation on high surface energy surfaces, thin film dynamics, and force convection.

The present invention relates to a heat exchanger enabling the reduction of the number of components constituting the heat exchanger, the simplification of the coupling structure thereof, and also, the decrease of combustion gas flow resistance and the minimization of noise and vibration generation, the heat exchanger being provided with a heat exchange unit having heating medium flow channels through which a heating medium flows and combustion gas flow channels through which combustion gas combusted in the burner flows to be alternately formed and adjacent to each other in spaces between a plurality of plates, wherein the heat exchange unit comprises: a sensible heat unit which surrounds the outer side of a combustion chamber, is formed of one side area of the plates, and heats the heating medium by using sensible heat of combustion gas generated by the combustion of the burner; and a latent heat unit which is formed of the other side area of the plates, and heats the heating medium by using latent heat of water vapor included in combustion gas that has finished undergoing heat exchange in the sensible heat unit, wherein bent flange units are formed on the edges of the plurality of plates, and in a state where the flange units of neighboring plates overlap, certain areas among the edges of the plurality of plates have formed thereon combustion gas pass-through units having combustion gas flowing through the combustion gas flow channels pass therethrough.

A heat exchanger 100, including: an inner cylinder 10 through which a first fluid can flow, the inner cylinder 10 being configured to house a heat recovery member 30; and an outer cylinder 20 disposed so as to be spaced on a radially outer side of the inner cylinder 10 such that a second fluid can flow between the outer cylinder 20 and the inner cylinder 10. In the heat exchanger 100, at least a part of the outer cylinder 20 and/or the inner cylinder 10 has at least one continuous irregular structure 40.

A heat exchanger (10) of heat pipe configuration for transferring heat between a first and second process streams via a heat transfer fluid comprises: at least one first process stream passage (19); at least one second process stream passage (29); and a shell (11) enclosing the first and second process stream passages (19, 29) within a volume (55). The volume (55), as a result of a heat transfer process, is fully filled with both vapour and liquid phases of the heat transfer fluid. The first and second process stream passages (19, 29) are spaced by a disengagement zone (50) enabling gravitational separation of said vapour and liquid phases and limiting accumulation of liquid phase heat transfer fluid about the first process stream passage(s) (19). Such heat exchangers can be used, among other applications, to replace a flash cooling stage in a Bayer process plant.

A cathode gas cooling system provided with a heat exchanger having first internal channels into which cathode gas flows and second internal channels to which water discharged from a fuel cell is supplied and cooling cathode gas flowing through the first internal channels by latent heat of vaporization of water flowing through the second internal channels. The first internal channels and second internal channel are are respectively made independent channels inside the heat exchanger so that steam produced inside the second internal channels by heat exchange with cathode gas flowing through the first internal channels does not flow into the first internal channels.

A heat exchanger includes a plurality of fins arranged in parallel, and a plurality of heat exchanger tubes penetrating the fins. The heat transfer tubes define a plurality of refrigerant passages through which refrigerant is passed inside the heat exchanger. Each of the refrigerant passages is formed as a single independent passage from the refrigerant inlet to the refrigerant outlet.

At least one of a heat-driven power generation system, an HVAC system, a system requiring heat rejection from its working fluid, and any object where cooling is advantageous where the portion of at least one of the exterior working fluid containment tubing and the exterior surface area exposed to air that is used for heat rejection is coated with a special coating designed to enhance heat rejection to the exterior air and/or space with minimal interference from air molecules in the earth's atmosphere.

Provided is a heat exchanger comprising a flat perforated heat transfer pipe having multiple refrigerant flow paths substantially parallel to each other, a fin provided with an insertion hole into which the flat perforated heat transfer pipe is to be inserted, and headers connected to ones of the refrigerant flow paths at both end portions in a width direction of the flat perforated heat transfer pipe, wherein the refrigerant flow paths are separated by at least four partition walls in the flat perforated heat transfer pipe, and are arranged in the width direction, the flat perforated heat transfer pipe is expanded and joined to the insertion hole, and ones of the refrigerant flow paths arranged at both end portions in the width direction have a greater width than those of other refrigerant flow paths.

A heat exchanger module including: a hollow chamber having an inner volume configured through which flows a first fluid in fluidic communication with a source of the first fluid, and a fluid outlet; a hollow enclosure extending outwardly from a surface of the hollow chamber wherein the hollow enclosure includes an inner volume through which flows a second fluid that undergoes a phase change in an operative mode of the heat exchanger module, wherein the hollow enclosure is in fluidic communication with a source of the second fluid, and an enclosure root of the hollow enclosure is inserted in the hollow chamber extending into the inner volume such that in an operative mode a second fluid flowing through the hollow chamber from the inlet to the outlet bathes the outer surface of said enclosure root.

An auxiliary multi-pass tube bundle heat exchanger for improving the melting efficiency of melter kettles used to melt thermoplastic pavement marking materials. The auxiliary multi-pass tube bundle heat exchanger includes a heat transfer tube bundle having a plurality of heat transfer tubes in which the flow of molten thermoplastic material reverses directions at least once. Hot heat transfer oils flows around the plurality of heat transfer tubes. Molten thermoplastic material is pumped from the bottom of a melter kettle, through the auxiliary multi-pass tube bundle heat exchanger and to the top of the melter kettle. A drainage system is provided to drain molten thermoplastic material and any settled glass beads form the auxiliary multi-pass tube bundle heat exchanger and a purging system is provided to purge molten thermoplastic material form the auxiliary multi-pass tube bundle heat exchanger using compressed air.