Method and apparatus for recovering a material by vaporization is disclosed. The method includes providing a heat transfer fluid to a liquid section of a vessel, injecting a material having a first component and a second component into the heat transfer fluid, the first component having a first volatility and the second component having a second volatility greater than the first volatility, circulating the heat transfer fluid from the liquid section to a heat exchanger, heating the heat transfer fluid to a temperature selected to vaporize at least a portion of the second component to a vapor section of the vessel, recovering the vaporized second component from the vapor section of the vessel, and circulating at least a portion of the heat transfer fluid from the from the heat exchanger through the vapor section of the vessel.

A desalination system includes a distillation unit to which a fluid to be desalinated is provided and through which a heat transfer fluid flows, and a solar concentration unit configured to heat the heat transfer fluid. The solar concentration unit includes an array of linear Fresnel reflectors, each linear Fresnel reflector of the array of linear Fresnel reflectors rotating about a respective axis, a receiver configured for absorption of light redirected by the array of linear Fresnel reflectors, the receiver comprising tubing through which the heat transfer fluid flows, and a frame supporting and positioning the receiver relative to the array of linear Fresnel reflectors. The frame defines a track along which the receiver is movable to adjust a relative position of the receiver along the respective axis of each linear Fresnel reflector of the array of linear Fresnel reflectors.

A humidification-dehumidification water purification system and method is disclosed. The system comprises a plurality of evaporator/condenser units and heat exchanger, preferably a solar collector. Contaminated water flows through successive condenser stages to the heat exchanger, and from there through successive evaporator stages. A flow of air is directed through successive evaporator stages in the direction opposite to the flow of water, where it is humidified by water vapor evaporating from the water. The humidified air passes through the successive condenser stages, where it is cooled, thereby condensing pure water and dehumidifying the air. The pure water is extracted from the system, and the dehumidified air can be recirculated through the system. In preferred embodiments of the invention, the evaporator/condenser units are stacked beneath the solar collector, and the system is fully portable and modular and can be either land- or water borne.

The present disclosure is drawn to an example evaporation panel, which can include an evaporation shelf that is laterally elongated and horizontally oriented and can include an upper surface and a lower surface. A second evaporation shelf can also be included that is laterally elongated and positioned in parallel beneath the evaporation shelf. The second evaporation shelf can have a second upper surface. The evaporation panel can further include a support column between the first evaporation shelf and the second evaporation shelf. The support column can include a plurality of stacked and spaced apart evaporation fins oriented in parallel with the evaporation shelf.

A wastewater evaporative separation system can include an evaporation panel assembly and a wastewater delivery system. The evaporative panel assembly can include at least 10 individual evaporation panels laterally joined together and fluidly coupled to a body of wastewater. The evaporation panel assembly can be configured for receiving wastewater from the body of wastewater and evaporating water therefrom as the wastewater cascades down the evaporation panel assembly and contaminants generally become more concentrated. The wastewater delivery system can be associated with the body of wastewater and can include a fluid directing assembly delivering wastewater from the body of wastewater to an upper portion of the evaporation panel assembly.

A method for controlling the temperature of the inner surface of a transfer line dryer, and thus controlling the temperature of a polymer product flowing through the transfer line dryer, is explained. Also provided is a transfer line dryer apparatus that is useful for implementing the disclosed method.

The present disclosure evaporation panel systems including a plurality of evaporation panels. The evaporation panels can include a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented; and a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves. The evaporation panels can also include a plurality of female-receiving openings which are individually bordered by two evaporation shelves and two support columns; and a plurality of male connectors positioned at lateral ends of both the first evaporation panel and the second evaporation panels. The first evaporation panel and the second evaporation panel can be orthogonally connectable via the male connectors of the first evaporation panel and the female-receiving openings of the second evaporation panel.

A new approach for desalination and purification of sea water using refrigeration units is suggested which seems promising to provide high quantities of drinkable water with reasonable cost. The apparatus uses compression refrigeration system to provide heat at the condenser to partially evaporate the intake sea water and uses evaporator at the other side to condense the produced water vapor back to clean drinkable water. A heat recovery heat exchanger captures the heat left in the returning sea water and delivers it to the fresh intake sea water to improve the efficiency and performance. The system can be designed using different refrigerants with some providing higher efficiencies and coefficients of performance. A typical desalination system using this approach shows in theory a production of about 3.6 trillion gallons of potable/drinkable water per year with only about 100 MW electric power installed. Equivalent electrical energy (kWh/m.sup.3) consumed by different methods has been reported about 13.5-25.5 kWh/m.sup.3 for Multi-stage Flash MSF, about 6.5-11 kWh/m.sup.3 for Multi-Effect Distillation MED, about 7-12 kWh/m.sup.3 for Mechanical Vapor Compression MVC, and about 3-5.5 kWh/m.sup.3 for Reverse Osmosis (RO). The suggested method here would take much less and only a fraction of kWh in theory to produce one cubic meter of potable/drinkable water.

Refrigeration unit can be designed to work under different pressures, different temperatures, different refrigerant flows, different capacities, and different powers. This purification system/apparatus can be utilized to purify sea/ocean water as well as any other type of water with dissolved and/or undissolved impurities. This purification system/apparatus can be designed to include optional processes, equipment and parts.

A hydro-thermal exchange unit (HTEU) for desalinating feed water in accordance with a humidification-dehumidification includes feed water, fresh water and gas conduit circuits for transporting feed water, fresh water, and gas, respectively. The unit also includes an evaporator through which a portion of the feed water conduit and the gas conduit pass. The evaporator causes evaporation of a portion of the feed water to produce vapor that is transported through the gas conduit. The unit also includes a condenser through which a portion of the gas conduit and the fresh water conduit pass. The condenser has input and output ports for coupling the gas and fresh water conduit circuits. The condenser extracts moisture from the vapor transported therethrough by the gas conduit. The extracted moisture is discharged through the fresh water conduit. The unit also includes a heat exchanger through which a portion of the fresh water conduit and the feed water conduit pass to thereby extract residual heat from the fresh water such that the residual heat heats the feed water.

A device housing having a hollow portion including a gas intake pipe projectingly provided to an outer periphery of an instrument body, having a heater built therein and attached to the instrument body. In the hollow portion, a heating wall formed by a bulge extending from the outer end side to the inner end side in the axial direction of the intake pipe and the heater for heating are internally provided. Between the heating wall and a gas intake pipe, and between the heating wall and an inner wall of the housing, inner and outer gas flow paths are formed a liquefied gas introduction side opening is provided at an outer end side of the outer gas flow path, and the outer end side of the inner gas flow path is communicated with a gas intake opening of the tip of the gas intake pipe.