A submerged offshore reverse osmosis desalination apparatus and method uses product water from the apparatus and an onshore cooler or heat exchanger provide or improve the cooling of a Sea Water Air Conditioning (SWAC) system, power plant, data center, Ocean Thermal Energy Conversion (OTEC) system, or Rankine Cycle heat engine.

A reverse osmosis system includes a first pretreatment system and a fluid source located below a reservoir. A first membrane housing has a reverse osmosis membrane therein. A first turbocharger includes a first pump portion and a first turbine portion. The first pump portion receives feed fluid from the first pretreatment system, pressurizing the feed fluid and communicates the feed fluid to the feed fluid inlet. The first turbine portion receives brine fluid from the brine outlet. The system further includes a second and third turbocharger. A second turbine portion and the third turbine portion receive brine fluid from the first turbine portion. Second feed fluid is communicated through a booster pump, a second pretreatment system, and second pump portion to increase a pressure of the second feed fluid. The second feed fluid is communicated to the third pump portion which communicates the pressurized second feed fluid to the first pump portion.

A submerged offshore reverse osmosis desalination apparatus and method uses product water from the apparatus and an onshore cooler or heat exchanger to provide or improve the cooling of a Sea Water Air Conditioning (SWAC) system, power plant, data center, Ocean Thermal Energy Conversion (OTEC) system, or Rankine Cycle heat engine.

A submerged offshore reverse osmosis desalination apparatus and method uses desalinated product water from the apparatus and an onshore cooler or heat exchanger to provide or improve the cooling of an onshore Rankine Cycle heat engine.

The subject disclosure provides systems for electric power generation and water desalination. In certain aspects, the systems include a power generation unit such as a reciprocating generator or fuel cell having a water cooling subsystem configured to receive cool water and output warm water and a water desalination plant co-located with the power generation unit and configured to receive and desalinate the warm water. Aspects of the invention also include methods for cooling a power generation unit using a water cooling subsystem and desalinating water with a desalination plant that is co-located with the power generation unit.

A reverse osmosis system includes a first pretreatment system and a fluid source located below a reservoir. A first membrane housing has a reverse osmosis membrane therein. A first turbocharger includes a first pump portion and a first turbine portion. The first pump portion receives feed fluid from the first pretreatment system, pressurizing the feed fluid and communicates the feed fluid to the feed fluid inlet. The first turbine portion receives brine fluid from the brine outlet. The system further includes a second and third turbocharger. A second turbine portion and the third turbine portion receive brine fluid from the first turbine portion. Second feed fluid is communicated through a booster pump, a second pretreatment system, and second pump portion to increase a pressure of the second feed fluid. The second feed fluid is communicated to the third pump portion which communicates the pressurized second feed fluid to the first pump portion.

A reverse osmosis system includes a membrane housing comprising a reverse osmosis membrane therein. The membrane housing comprising a feed fluid inlet, a brine outlet and a permeate outlet. A first turbocharger has a first pump portion and a first turbine portion. The brine outlet is coupled to a first pipe directing a first portion of brine to the first pump portion. The first pump portion is in fluid communication with the feed fluid inlet. A feed pump communicates feed fluid to the feed fluid inlet through the first turbine portion. The brine outlet is coupled to a second pipe directing a second portion of brine toward a drain through a brine control valve.

A reverse osmosis system includes a membrane housing comprising a reverse osmosis membrane therein. The membrane housing comprising a feed fluid inlet, a brine outlet and a permeate outlet. A first turbocharger has a first pump portion and a first turbine portion. The brine outlet is coupled to a first pipe directing a first portion of brine to the first pump portion. The first pump portion is in fluid communication with the feed fluid inlet. A feed pump communicates feed fluid to the feed fluid inlet through the first turbine portion. The brine outlet is coupled to a second pipe directing a second portion of brine toward a drain through a brine control valve.

A control method is provided for a filter system, which includes at least one filter element (2). The method includes continuously recording a total energy consumption (E.sub.G) during a filtration cycle (22) of the filter system. The total energy consumption (E.sub.G) includes at least of the energy consumption (E.sub.B) for a physical cleaning (24) and the energy consumption (E.sub.P) for the subsequent production cycle (23) up to a predefined, in particular current point in time. The method further includes computing a relative energy consumption (E.sub.rel) by way of division of the recorded total energy consumption (E.sub.G) by a net permeate volume (Q.sub.N) which has been produced during the filtration cycle (22) up to the predefined point in time and starting a physical cleaning (24) in dependence on the relative energy consumption or of a characteristic value derived from this.

Device for water disinfection by ultrafiltration. The device comprises a filtering assembly with at least one ultrafiltration membrane (6) inside a casing (10); a pump (5, 15), powered with electrical energy, configured for driving water to be filtered to said at least one ultrafiltration membrane (6); and an electric supply connection (2) for powering said pump (5) from a power supply. Said at least one ultrafiltration membrane is located in said casing (10) in a position in which it receives the feed flow of the water to be filtered by gravity or pressure; the electric power supply is provided by a battery included in a portable communication device (4); and the intensity of the current consumed by the pump (5, 15) is below 1.2 A, with a supply voltage of up to 24 V.