Abstract: A processing apparatus (1) for the processing of process or industrial wastewaters is provided. The processing apparatus (1) has an evaporator (4) in which a tube bundle heat exchanger is provided, whose pure distillate side is connected to a separating apparatus for separating the distillate from floating organic phase or similar free liquid constituents. This separating apparatus is intended to collect the floating organic phase from the condensate, in order that this phase can be sucked back into the evaporator (4). In addition, the vapor mixture is conducted from the separating apparatus (8) to a recuperator (3) and cooled to such an extent that the water, the volatile solvents and the organic material dissolved in the vapor can be condensed and discharged separately or can be sucked back into the evaporator (4). This allows significantly better distillate qualities to be achieved.

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: An objective of the present invention is to suppress bumping in the distillation still so as to collect a high purity solvent containing no impurities. A solvent vapor valve 21 is disposed in a solvent vapor withdrawal conduit 20 through which solvent vapor is transferred from inside the distillation still 10 to an inner pipe 31 of a double-tube structure 30 which is a heat exchange section. Also, a thermistor 14 is disposed in an upper space in the distillation still 10. After a heating chamber 11 starts heating the solvent, the start of boiling is determined by a sudden rise in temperature detected by the thermistor 14, and shortly thereafter, the solvent vapor valve 21 is closed to fill the distillation still 10 with the solvent vapor.

Abstract: Methods and systems for producing electrical power, desalinated water, and/or salt are provided. The system can include one or more first turbines in fluid communication with a body of salt water; one or more boilers for heating the salt water to provide steam and brine; and one or more second turbines in fluid communication with the steam for producing the electrical power.

Abstract: Vaporization chambers (distillation “pots”) are disclosed in which the liquid contained in such a pot is heated and circulated to establish thermal uniformity of the liquid and to route the circulated liquid past a thermally conductive member that contacts the liquid. The thermally conductive member extends from a location on a wall of the pot in a portion of the pot that holds the liquid as the liquid is being heated in the pot and conducts thermal energy directly from the liquid to a location outside the pot corresponding to the location on the wall. The pot desirably is divided into an upper portion and lower portion, wherein the liquid circulates from the lower portion to the upper portion and from the upper portion to the lower portion during heating. During this circulation, bubbles formed in the liquid can be routed into the upper portion in a manner resulting in fracture of the bubbles and recovery of liquid entrained in the bubbles, thereby preventing foam accumulation in the pot.

Abstract: An low concentration dope is fed through a nozzle into a concentrating apparatus, and flash evaporation of the low concentration dope is performed at an end of the nozzle. The low concentration dope is concentrated thereby to an concentrating dope which is contained and heated in the concentrating apparatus. Thus part of solvents of the low concentration dope and the concentrating dope is evaporated to a solvent gas. The solvent gas is cooled and condensed in a condensing section of the concentrating apparatus, and thereafter drawn through a first exit from the concentrating apparatus. The concentrating dope is concentrated to a high concentration dope, which is drawn through a second exit from the concentrating apparatus.

Abstract: A desalination apparatus capable of obtaining fresh water stably at low cost by utilizing low-temperature waste, wherein the desalination apparatus including a heat exchanger 92 cooperating with an evaporation can 60 so as to subject a low-temperature waste heat 11 and raw water 62 in the evaporation can 60 to heat exchange and generate water vapor 63 in the evaporation can 60; a condenser 98 cooperating with a raw water tank 72 so as to receive the water vapor 63 from the evaporation can 60, cool the water vapor 63 by subjecting the water vapor 63 and raw water 71 in the raw water tank 72 to heat exchange and obtain distilled water 76; a distilled water tank for storing the distilled water 76; vacuum means for evacuating the evaporation can 60 and depressurizing the inside thereof so as to promote generation of water vapor 63 in the evaporation can 60; and raw water supply means for supplying raw water to the evaporation can.

Abstract: A liquid sample 3 held in an open container 2 and including a volatile solvent, is evaporated by continuously removing inert gas rich in vapor by means of a suction tube 5 whose open end is held close to the top surface of the liquid. Vapor in the gas is then extracted in a refrigerated condensing vessel 6, from where the purified gas is fed by a pump 7 for recirculation back into a sealed chamber 1 in which the container is mounted. In a modification, the inert gas is fed directly through a nozzle 17 into the container 2 wile the gas/vapor mixture is extracted from the chamber 1 for recirculation, after passing through a condenser 6 or the like.

Abstract: A process and system for conditioning a bulk container for ultra-high purity liquefied gas. Vapor is generated in the container from a conditioning quantity of the ultra-high purity liquefied gas by imposing a temperature difference on the container so that the vapor condenses when a temperature difference is achieved. The resulting liquid reflux, e.g., the condensed liquid drips or flows back to the conditioning quantity of the liquified gas, washes or removes contaminants, e.g., particles, metal and moisture, from the interior surface of the container. A portion of the vapor is vented from the container for reclamation. The used conditioning liquid may also be reclaimed.

Abstract: A circulation evaporator for separating mixtures having more volatile and less volatile components. The circulation evaporator contains an evaporator, a discharge container connected to the evaporator by a connecting piece, a condenser, a vacuum pump, a recirculating line, a feed line and an outflow line. The discharge container contains a chamber for feed and a chamber for outflow. The invention further relates to a process for the separation by distillation of a mixture having more volatile and less volatile components by employing the circulation evaporator.

Abstract: A vacuum low-temperature distilled pure water dispenser includes a water-supply tank communicating with a reaction chamber via a water supply line, a pure water storage tank communicably located above the reaction chamber, an actuating pump communicably located below the reaction chamber, and a refrigerating system having pipe lines extended between the reaction chamber and the pure water storage tank. When the actuating pump is actuated, a vacuum is produced in the reaction chamber to suck water in the water-supply tank into the reaction chamber, at where the sucked water is heated and vaporized by heat provided by a compressor of the refrigerating system, so that impurities, organic and inorganic matters, bacteria, and viruses in the water are separated therefrom through vacuum low-temperature distillation. When the actuating pump keeps pumping, the distilled water is sent from the reaction chamber into the pure water storage tank.

Abstract: The invention refers to a simultaneous system for the distillation and elevation of water on top of the water table itself, which driven by thermo solar energy allows in an autonomous operation the generation of electrical power through transportation and free fall of water.

Abstract: A system is described for recovering a purified distillable component from a starting mixture utilizing a transition tank to receive a transition mixture distilled from a starting mixture, which is returned to the system for further distillation. The system includes a condenser which features an annular tube having cooling fins arranged inside and outside its annular region to improve its cooling efficiency, and a reflux column which features a flow distributor and a flow centralizer to improve mixing of the rising vapors with the descending liquid. The system also includes a temperature sensor located between the reflux column and the condenser for supplying temperature measurements used in the automatic, operator-less control of the system.

Abstract: The inventive device for distilling a medium comprises at least one reservoir (11, 51) or accommodating the medium (15, 55) to be distilled, a heating element (12, 52) for vaporizing the medium (55), and comprises at least one collecting vessel (20, 60), which is situated downstream and which is provided with a cooling element for condensing the produced distillation vapor. In addition, a pipe (19, 59) or the like is provided on the top side of the reservoir (11, 51). Said pipe leads into the collecting vessel (20, 60) and connects the vapor space (14, 54) located inside the reservoir (51) to that which is located inside the collecting vessel (20, 60). To this end, means are provided, which, for the most part, completely remove foreign gases from the vapor spaces (14, 24; 54, 64) before or at the beginning of the distillation process.

Abstract: The distillation plant comprises a column (1) and a heat pump (4, 5) which operates between a sump vaporizer (3) and an exhaust vapor compressor (2) of the column. The heat pump is substitutable by devices (6, 7) which can be switched to the sump vaporizer and the exhaust vapor compressor when required. These substituting devices comprise devices (6 and 7 respectively) for the production of vapor or the provision of a coolant respectively as well as connection means (63, 63′, 72, 72′). The coolants can be liquids (water) or gases (air).

Abstract: The invention pertains to a device (1) for the condensation of water from an aqueous liquid by means of a temperature gradient, which device comprises, (a) a vapor chamber (5) that can be brought in contact with a condensation compartment (4) wherein at least part of the water vapor from the aqueous liquid condenses, and wherein inside of said vapor chamber is located, (b) an evaporation compartment (2) having a least a wall with an outer surface and comprising a closed, hollow and water permeable membrane, and which vapor chamber has an outer surface that comprises a substantially water-impermeable insulation skirt (3) with an inner and an outer surface, such that there is a gap between the inner surface of the insulation skirt and the outer surface of the evaporation compartment, and wherein the vapor chamber has a lower surface of an active width (w) which is at least 10% of the effective diameter (d) of the evaporation compartment.

Abstract: A system and method for purifying liquefied corrosive gases of metallic impurities is described. The principle for this purification method relies on vapor-phase transfilling the vapor phase from a source container into a receiving container. This method has been observed to decrease metal concentrations by a factor of at least 1000 and, decreases the metallic impurity levels in the resulting condensate. The vapor transfer is accomplished by controlled differential pressure rather than mechanical pumping, thereby generating no particle or metal impurities.

Abstract: A water-cooled distilling apparatus for purifying or distilling raw water. The apparatus includes a boiler, cooling tray assembly, and collection vessel. In use, raw water is initially poured into the boiler which has a self-regulating screen in it. As the water beings to boil, the screen rises to float above the raw water. The height of the screen above the water automatically adjusts proportionately to the rate of boil to proportionately expose more or less surface area of the screen. A water film forms on the exposed surface area of the screen and clean steam rises therefrom into the cooling tray assembly where it is deflected into a condensing area on each level of the assembly. In each condensing area, heat is transferred from the steam into coolant water in a reservoir, causing the coolant water to evaporate from the reservoir and the steam to condense on the bottom of the surface of the reservoir. Distillate formed by the condensing steam is then collected and transferred to a collection vessel.

Abstract: In a distillation unit (10) a rotary heat exchanger (32) receives from a radially inward position feed liquid to be purified and collects on the inner surface of a rotating exterior shell (36) liquid that has passed through its evaporation chambers (56). Stationary scoop tubes (122 and 124) scoop liquid from the resultant liquid layer that forms on the shell (36)'s inner surface, and the kinetic energy of the liquid scooped from the thus-spinning layer drives it radially inward through the scoop tubes (122 and 124) into spray arms (58) for reintroduction into the rotary heat exchanger's evaporation chambers (56).

Abstract: Garbage and waste of all types that includes or comprises organic matter, particularly including medical waste, plastics, paper, food waste, animal by-products, and the like, can be economically recycled into petroleum products, including oil. Machinery performs a method that mimics natural processes but accomplishes the task in minutes, at rates of about 15 tons per day in a typical processing machine, rather than taking hundreds of thousands of years in nature. The process and apparatus of the invention may chop the waste into small pieces, under negative pressure if appropriate, and then pass the waste into first and then second augers for compression and heating. Destructive distillation occurs, in which large molecular weight hydrocarbons and petrochemicals are heated by hot oil passing through the hollow shaft and by circulating hot, dense, hard material, such as steel balls or fragments or hard rock pieces and such, under pressure with steam, to produce low molecular weight hydrocarbons.

Abstract: A vapor-compression distiller includes a rotary heat exchanger. A reciprocating compressor (26) maintains a pressure difference between the compressor's evaporation chambers (46) and its condensation chambers (44). The compressor is assembled in a common rotating assembly with the compressor, so the distiller does not need rotating seals between the compressor and heat exchanger. The compressor includes two pistons (56 and 58) driven in opposite directions in a rotating piston chamber (54). The directions in which they thereby reciprocate are substantially parallel to the rotating assembly's axis.

Abstract: Apparatus and method for condensing moisture from an air stream. The condensing comprises concentric cylinders having a common wall. The outer cylinder contains a cooling material, such as water, and upon contact therewith, the air stream is cooled and moisture contained therein is condensed.

Abstract: A salt water desalinating device, characterized by having an absorption refrigerating machine using a first dilute salt water and concentrated salt water and characterized in that a second dilute salt water to be desalinated is evaporated by heat flowing out from the high-temperature heat source of the absorption refrigerating machine and vapor evaporated from the second dilute salt water is condensed by heat to be absorbed to a refrigeration source. A plurality of the absorption refrigerating machines may be series-connected in a series arrangement.

Abstract: Disclosed herewith is a distillation apparatus for water purifiers. The distillation apparatus includes a purifier body, a boiler, a condensing coil and a water storage tank that are sequentially connected to each other. The front portion of the condensing coil is extended through a preheating tube comprised of a heat chamber, an inlet and an outlet. The inlet of the preheating tube and the purifier body is connected by a first purified water supply line. The outlet of the preheating tube and the boiler is connected by a second purified water supply line.

Abstract: For a process for producing high-purity liquids, particularly liquid chemicals, by distillation it is proposed that the liquid to be purified (1) is heated by microwave radiation (5) preferably in the uppermost layers.

Abstract: For a process for producing high-purity liquids, particularly liquid chemicals, by distillation it is proposed that the liquid to be purified (1) is heated by microwave radiation (5) preferably in the uppermost layers. To implement this process a device with a liquid container (3), with a heat source (5) acting on the liquid container and with a condensation device (8, 9) connected to the liquid container is proposed, which is distinguished in that the heat source (5) in the form of a microwave radiation source is arranged above the liquid to be purified (1) in such a way that preferably the uppermost layers of the liquid (1) are heated.

Abstract: A system and method for purifying liquefied corrosive gases of metallic impurities is described. The principle for this purification method relies on vapor-phase transfilling the vapor phase from a source container into a receiving container. This method has been observed to decrease metal concentrations by a factor of at least 1000 and decreases the metallic impurity levels in the resulting condensate. The vapor transfer is accomplished by controlled differential pressure rather than mechanical pumping, thereby generating no particle or metal impurities.

Abstract: The invention relates to an improved evaporator and condenser unit for use in distilling a liquid such as water. The evaporator and condenser unit includes a plurality of stacked, spaced-apart plates disposed within a housing. The plates are horizontally arranged around a common, vertical axis for rotation. Adjacent plates define spaces between their oppositely facing surfaces, which are alternating configured as evaporating and condensing chambers. An outlet tube transfers vapor generated within the housing to a compressor and an inlet tube delivers compressed vapor to central receiving space within the stack of plates. A sump containing the liquid to be distilled is located at a lower portion of the housing. Each plate includes a plurality of ports for distributing liquid to be distilled and for extracting a condensate.

Abstract: Provided is a novel on-site system and method for providing ultra-high-purity nitric acid to a point of use. The system includes a source of nitric acid at a concentration greater than 68 wt %; a reflux distillation column having an inlet in communication with the nitric acid source for introducing nitric acid into the column, a reboiler, and a condensate outlet to provide a flow of nitric acid condensate from the column; a reservoir in communication with the condensate outlet for receiving the flow of nitric acid condensate; and piping for delivering nitric acid from the reservoir to a point of use. The system and method can be used as an on-site subsystem, in a semiconductor device fabrication facility for supplying the nitric acid condensate to points of use in the semiconductor device fabrication facility.

Abstract: An apparatus for reducing the coke dust in the decoking effluents of the hydrocarbon cracking ovens according to the invention provides means for the condensation of the effluent, means for collecting a liquid condensate, means for filtering said liquid condensate, and means for washing the residual vapours and gases that cannot be condensed by using the same condensate suitably filtered from coke, the filtered condensate being evaporated for the following discharge to the atmosphere by using the thermal content of the input decoking gases. A process for reducing the coke dust in the decoking effluents of the hydrocarbon cracking ovens according to the invention consists in that the solid content in the gaseous effluent from the decoking is removed by filtration of the condensate from said gaseous effluent and by washing of gases and vapours contained therein that cannot be condensed.