Abstract: A method and apparatus are provided for the non-recirculating self-sanitization of a carbon filter (14) in a water pretreatment system (12). The apparatus includes a heat exchanger (50) that can maintain an activated carbon bed (44) of the carbon filter (14) at a desired sanitization temperature during service operation of the pretreatment system (12) where the pretreatment system (12) is providing a pretreated water stream (32H) for final treatment.

Abstract: A vapor compression distillation system (10) is provided and includes a fluid inlet (12) for receiving a fluid, a fluid outlet (14) for a distillate that has been distilled from the fluid, a heat exchanger (16) connected to the fluid inlet (12) and the fluid outlet (14) to transfer heat from the distillate to the fluid; and an integrated motor/compressor unit (18) connected to the heat exchanger (16) to receive vaporized distillate therefrom and to supply pressurized distillate thereto. The system 10 may further include a coolant system (20) connected to the integrated motor/compressor (18) to supply a coolant flow thereto. The system (10) may also include an air oil mist system (22) that is connected to the integrated motor/compressor unit (18) to supply an air oil mist thereto for bearing lubrication and cooling.

Abstract: A method is provided for manufacturing pharmaceutical water by means of distillation and sanitizing the equipment used in said manufacturing. The method comprises the removal of suspended solids from chlorine-containing water by means of a multimedia filter, followed by a water-softening step and a dechlorination step. Ammonia is then removed from the dechlorinated water before subjecting the water to distillation in a mechanical vapor compression distillation unit. A portion of the generated low-pressure-steam is used to sanitize the manufacturing equipment at certain prescribed locations, and the distilled water, exhibiting United States Pharmacopoeia purified water quality, is withdrawn from the still and stored as pharmaceutical water product. No reverse osmosis operation is required. A system for carrying out the process is also provided. Sanitization is carried out while the system is in a standby mode.

Abstract: An improved water purification system for production of USP purified water and/or USP water for injection include backwashable, chlorine tolerant microfilter or ultrafilter for initial filtration of the feed water (10). The filtrate from the filter (18) is provided to a dechlorinator (18) prior to being subjected to an optional, reverse osmosis membrane unit (60) and then to a still (66) which discharges purified water at USP standards for purified water or water for injection.

Abstract: An improved water purification system for production of USP purified water and/or USP water for injection include backwashable, chlorine tolerant microfilter or ultrafilter for initial filtration of the feed water (10). The filtrate from the filter (18) is provided to a dechlorinator (18) prior to being subjected to an optional, reverse osmosis membrane unit (60) and then to a still (66) which discharges purified water at USP standards for purified water or water for injection.

Abstract: An improved water purification system for production of USP purified water and/or USP water for injection include backwashable, chlorine tolerant microfilter or ultrafilter for initial filtration of the feed water (10). The filtrate from the filter (18) is provided to a dechlorinator (18) prior to being subjected to an optional, reverse osmosis membrane unit (60) and then to a still (66) which discharges purified water at USP standards for purified water or water for injection.

Abstract: An improved portable reverse osmosis water purification plant includes a frame 10 with a storage area 20 thereon adapted to receive a feedwater pump 76 and a product water pump 78. A diesel engine 44 is located on the frame 10 along with a high pressure pump 52 which is driven thereby. A primary filter 70 is located on the frame 10 and is connected to the feedwater pump 76 to receive water to be purified therefrom. A secondary filter 72 is also located on the frame 10 and is of the cartridge type. The same delivers water to be purified to the high pressure pump 52, which in turn provides the water to be purified to membrane/pressure vessels 60 located on the frame.

Abstract: A compact and energy efficient water distillation unit is disclosed including a housing divided by shared interior walls into deaerator, heater and evaporator chambers. A deaerator is mounted in the deaerator chamber. An evaporator is mounted in the evaporator chamber and a vapor compressor is provided for drawing water vapor produced by the evaporator through a demister and outputting the vapor into a duct open to the evaporator. The duct is at least partially located above the heater chamber and open thereto. A heater is mounted in the heater chamber. A duct interconnects the evaporator with the deaerator chamber and a vertical standpipe connects the deaerator and evaporator chambers.

Abstract: Formation of alkaline scale on cooling tower and associated heat transfer surfaces contacted by circulating water is reduced or substantially eliminated while minimizing equipment corrosion by introducing an effective amount of carbon dioxide and a threshold effect chemical scale control additive to the circulating water.

Abstract: Formation of alkaline scale in water distillation equipment is reduced or substantially eliminated without a significant increase in equipment corrosion rate by dissolving an effective amount of carbon dioxide in brine which is boiling or flashed or which has been boiled or flashed and which contains an effective amount of a high temperature threshold effect chemical scale control additive.