Abstract: Equipment, systems, processes and techniques for conducting processing of solutions are described. The techniques can be applied to provide diluted solution (i.e. purified solvent), concentrate solution or each. A variety of specific equipment, example systems and processes are depicted and described.

Abstract: Equipment, systems, processes and techniques for conducting processing of solutions are described. The techniques can be applied to provide diluted solution (i.e. purified solvent), concentrate solution or each. A variety of specific equipment, example systems and processes are depicted and described.

Abstract: Equipment, systems, processes and techniques for conducting processing of solutions are described. The techniques can be applied to provide diluted solution (i.e. purified solvent), concentrate solution or each. A variety of specific equipment, example systems and processes are depicted and described.

Abstract: Equipment, systems, processes and techniques for conducting reverse osmosis processing of solutions are described. The techniques can be applied to provide diluted solution (i.e. purified solvent), concentrate solution or each. A variety of specific equipment, example systems and processes are depicted and described.

Abstract: A moisture control system for pressurized air comprises a first and a second chamber which alternate between drying and regenerating phases. Only one of the chambers is at the drying phase at any given point in time. An input provides compressed air to the chamber at the drying phase. The moisture control system includes a bypass line passing air that does not go through the chamber at the drying phase. The air exiting the chamber at the drying phase is combined with the air from the bypass line to obtain air with a controlled moisture content for outputting.

Abstract: Regenerative air dryers are disclosed for feeding pressurized air with a controlled moisture content to a header. In one embodiment, a dryer comprises first and second chambers alternating between drying and regenerating phases. One of the chambers is at the drying phase while the other is at the regenerating phase. A controller is programmed to switch the phase of the chambers between drying and regenerating when the desiccant in the chamber at the drying phase has retained water to a predetermined capacity. A bypass line bypasses both chambers. An input provides air to the chamber at the drying phase and to the bypass line. A dew point feedback system controls a volume of air passing through the bypass line. Means are included for combining air from the bypass line with air exiting the chamber at the drying phase to provide air with a controlled dew point to the header.

Abstract: Equipment, systems, processes and techniques for conducting reverse osmosis processing of solutions are described. The techniques can be applied to provide diluted solution (i.e. purified solvent), concentrate solution or each. A variety of specific equipment, example systems and processes are depicted and described.

Abstract: An improved method and apparatus for cooling the under-car channel of a tunnel kiln while minimizing migration of air between the above-car and under-car channels involves controlling or equalizing the mass flow of cooling air directed through the under-car channel and in particular through individual undercarriage cooling zones which can match individual heating zones of the tunnel kiln.

Abstract: A method and apparatus for reducing fuel consumption in conveyor ovens by creating a barrier to the infiltration of heated air from a heating section of the oven into a cooling section of the oven thereby reducing the loss of heated air and reducing consumption of fuel otherwise required to maintain the selected oven temperature. The barrier is formed by directing a stream of pressurized air into a transition section between the heating and cooling sections of the oven.