Provided herein are new aluminum alloy materials which are useful in replacing copper in a heat exchanger. The aluminum alloy materials are also useful in manufacturing components of heating, ventilating, air-conditioning, and refrigeration (HVAC&R) systems for indoor and outdoor units. The alloys are well-suited for tubing in a heat exchanger. The alloys display high strength and good corrosion resistance. Also provided herein are methods for making the aluminum alloy materials.

Provided herein are new aluminum alloy materials which are useful in replacing copper in a heat exchanger. The aluminum alloy materials are also useful in manufacturing components of heating, ventilating, air-conditioning, and refrigeration (HVAC&R) systems for indoor and outdoor units. The alloys are well-suited for tubing in a heat exchanger. The alloys display high strength and good corrosion resistance. Also provided herein are methods for making the aluminum alloy materials.

A controller performs a first operation in which a heat source device directly or indirectly heats water in a first channel of a heat exchanger and a second operation in which the heat source device directly or indirectly cools the water in the first channel of the heat exchanger after the first operation ends.

The following provides a system and method to predict an indicator of tube fouling in a fired apparatus such as a boiler. Historical data can be collected when the tubing is still considered to be clean, and used to build a first model between an indicator of fouling, such as tube skin temperature, and boiler load. The actual measurement of that indicator of fouling can then be compared against the model output, such that the error between the model and measurement is considered an indication of the tube fouling. Moreover, the rate of change of the model error can be used to measure the fouling rate. Next, historical data on the fluid feed quality can be collected and together with the historical error rate change data can be combined to develop a second model. This second model reflects how fluid feed quality variables may affect the fouling rate over time.

A system for reducing evaporative cooling water losses using an electric and magnetic field inducing device is disclosed. The device influences a liquid's properties including evaporation rate, diffusion, vapor, heat transfer rate, and/or fluid properties. The device comprises a malleable core with notches and electrically conductive windings wrapped around the flexible core around the notches. An insulative coating isolates the windings from the core. The device is pliable and is wrapped and/or attached around a conduit (e.g., a makeup line or pipe or a recirculating line or pipe of an evaporative cooling tower) with flowing fluid and current is passed through the windings to treat the fluid.

A system for reducing evaporative cooling water losses using an electric and magnetic field inducing device is disclosed. The device influences a liquid's properties including evaporation rate, diffusion, vapor, heat transfer rate, and/or fluid properties. The device comprises a malleable core with notches and electrically conductive windings wrapped around the flexible core around the notches. An insulative coating isolates the windings from the core. The device is pliable and is wrapped and/or attached around a conduit (e.g., a makeup line or pipe or a recirculating line or pipe of an evaporative cooling tower) with flowing fluid and current is passed through the windings to treat the fluid.

A reversible flow heat exchange system includes a heat exchanger system that includes a canister configured to receive a first fluid from a machine and a heat exchanger disposed within the canister. The reversible flow heat exchange system also includes a cooling system coupled to the heat exchanger and configured to circulate a second fluid between the heat exchanger system and the cooling system and a reversing valve coupled to the heat exchanger and configured to selectively direct a flow of the first fluid in a first direction through the canister and in a second direction through the canister that is opposite the first direction.

A tubular heat exchanger includes tubes, each having a plurality of cells inside, stacked in multiple stages and zigzag-bent heat-radiating fins brazed and integrated among the tubes. The gaps among the tubes become progressively wider toward the rear to enable foreign substance to be discharged without being caught by the heat-radiating fins. The upper and lower surfaces are formed of an inclined surface progressively and symmetrically reduced and inclined rearwardly with respect to a tube center line to have the front cell thicker than the end cell. The upper and lower surfaces of the heat-radiating fins are formed of an inclined surface progressively and symmetrically enlarged and inclined rearwardly with respect to a fin center line. A wind direction guiding ribs, tilted toward the upper and lower surfaces of the tubes, protrude from the heat-radiating fins to blow the wind along the upper and lower surfaces of the tubes.

A tubular heat exchanger includes tubes, each having a plurality of cells inside, stacked in multiple stages and zigzag-bent heat-radiating fins brazed and integrated among the tubes. The gaps among the tubes become progressively wider toward the rear to enable foreign substance to be discharged without being caught by the heat-radiating fins. The upper and lower surfaces are formed of an inclined surface progressively and symmetrically reduced and inclined rearwardly with respect to a tube center line to have the front cell thicker than the end cell. The upper and lower surfaces of the heat-radiating fins are formed of an inclined surface progressively and symmetrically enlarged and inclined rearwardly with respect to a fin center line. A wind direction guiding ribs, tilted toward the upper and lower surfaces of the tubes, protrude from the heat-radiating fins to blow the wind along the upper and lower surfaces of the tubes.

Implementations described herein generally relate to substrate processing equipment and more particularly to methods and compositions for temperature control of substrate processing equipment. In one implementation, a method of cooling a processing chamber component is provided. The method comprises introducing an inert purge gas into a supply reservoir containing a coolant and flowing the treated coolant to a processing chamber component to cool the processing chamber component. The coolant initially comprises deionized water and a water-soluble base.