Abstract: A device for intercepting liquid obtained from a stream of mixed fluids contains an enclosure having an upper opening and a lower opening. The upper opening is connectible to a source of suction while the lower opening is connectible to a source of the mixed fluids. A partition between the openings divides the enclosure into a liquid collecting section which includes the upper opening and a liquid discharging section which includes the lower opening. The partition has a liquid flow passage at the lower end thereof and an orifice at the upper end thereof, and the orifice provides a pressure drop between the two openings. A liquid collecting basin is formed at the bottom of the enclosure, and the lower opening is provided with an overflow for the basin. In operation, the suction source draws a stream of mixed fluids from the mixed fluid source. Liquid is derived from the stream in or above the liquid collecting section and forms a pool in the liquid collecting basin.

Abstract: An improved ocean thermal energy conversion (OTEC) system which includes a novel combined evaporator/condenser. The combined evaporator/condenser further includes a plurality of evaporator spouts and a mist eliminator, wherein the pressure is maintained across the plurality of evaporator spouts. The OTEC system also generates fresh water as a primary product and generates only enough electricity, as a secondary product, to operate the OTEC system itself.

Abstract: In a plate heat exchanger for evaporation of a liquid by means of a heat emitting vapor every second plate interspace forms an evaporation passage (28) and the rest of the plate interspaces form condensation passages (30). Aligned openings (16) in the plates form an inlet channel through the plate heat exchanger for introduction of evaporation liquid into the evaporation passages (28). For enabling use of a large inlet area of each condensation passage (30) and a large outlet area of each evaporation passage (28) the plate heat exchanger is arranged in a container (1), the interior of which is divided in two chambers (6, 7) by the plate heat exchanger itself and a partition (5).

Abstract: An orbital evaporator has a vertical heat transfer tube or tubes mounted in a container driven in an orbital motion. A stiff whip rod is freely movable within the tube. Its lower end rests on a horizontal plate. The orbital motion causes the rod to roll over the interior surface of the tube to distribute the liquid in a thin film and to control fouling. A set of fins is mounted on the exterior of the tube to collect and channel the condensate to improve heat transfer through the tube. The fins are preferably longitudinal and the whip rod is preferably hydrophobic. Operating the evaporator with boiling temperatures substantially below 100.degree. C. in combination with the fins and a rolling whip rod allows operation as a desalinization unit for an indefinite period of time with a high total heat transfer coefficient. The evaporator preferably also includes a degasser to control the formation of a gas barrier at the exterior surface of the tube.

Abstract: A method and apparatus for deaerating a suspension of solids in a liquid such as, for instance, papermaking stock. The suspension is flashed in a vacuum tank connected to a condenser. The vapor released when the suspension is flash cooled in the tank is condensed into an absorption liquid having a higher temperature but a lower vapor pressure than that of the released vapor on a heat exchange surface of the condenser. The flash cooled suspension is used as the cooling medium in the condenser. The diluted absorption liquid is regenerated in an evaporator and recirculated to the condenser. The vapor released in the evaporator can be condensed to heat the suspension further or for other suitable heating purposes.

Abstract: Distilling equipment comprising evaporation apparatus (2) including a boiling chamber (6) and equipment and conduits (46-59, 62, 63, 65-71) for supplying raw liquid to the boiling chamber at a predetermined level (43), a plurality of serial condensation stages (10, 20, 30), the first stage (10) connected to the top (7) of the boiling chamber (6) to receive gas therefrom and condense the gas by contact with cold recycled distillate from the final condensation stage (30), each stage having vertical vacuum producing bubble tubes (15, 25, 35) through which distillate and gas bubble (17) pass downward to a collection vessel (16, 26), gas carrier tubes (19, 29) which carry gas from each collection vessel (16, 26) to the condensation chamber (21, 31) of the following stage, and pump (41, 42) in cooperating conduits (18, 22, 28, 32) for pumping distillate free of gas from each collection chamber (16, 26) to the condensation chamber (21, 31) of the following stage.

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: This document describes an improved method and apparatus for recycling energy in counterflow heat exchange and distillation. The basis of the invention is transferring heat with thin sheets of material having extensive surface area relative to the flow rate through the system. A distillation apparatus (11 and 12), a counterflow heat exchanger (11), a clothes dryer (FIG. 9), a power generator (FIG. 12), and other embodiments of the invention are described.

Abstract: Apparatus and a method for upgrading low pressure steam or brine, such as from a geothermal well, to prepare the steam or brine for any one of a number of uses, such as for conversion to pure, high pressure, high temperature steam for driving turbines. The system operates in a degasification phase in which a small amount of superheated steam is applied to the brine to scrub the same to cause the removal of concentrated gases therefrom. The degasified product is then pumped to a high pressure, heated countercurrently, and directed through a demineralized phase to remove the salts and solids in a liquid phase and convert the bulk of the water into pure, high pressure saturated steam. The steam output from the demineralizing phase can then be used to produce useful work, such as driving a turbine. In addition to forming saturated steam from geothermal brine, the system can be used to form pure saturated steam from impure water from any suitable source.