Method and device for the preparation of monophasic powders of actinide salts which are precursors in the production of fuel pellets. In one aspect, a compact and simple device is provided to obtain dry monophasic powders of actinide salts in one stage, while increasing the productivity, chemical and nuclear safety of the process. In a second aspect, the method comprises feeding of nitric actinides-containing solution and formic acid to a cylindrical heated reactor, grinding the resulting powder, and discharging the powder. The nitric actinides-containing solution and formic acid are continuously metered to the upper zone of the reactor so that the reactive chemicals are mixed in a thin film on the heat-exchange surface, where the reaction mixture is continuously stirred by rotor blades. Also occurring are the processes of denitration, formation of the relevant compounds, their drying and grinding and collecting dry salts of actinides in a hopper by gravity.

A rotating evaporator includes a chamber, and a rotor assembly disposed in the chamber, and including distillation elements that each contain an internal cavity, condensation surfaces that face the internal cavity, and evaporation surfaces that face away from the internal cavity, and a vapor manifold extending through the distillation elements and configured to provide a vapor to the internal cavities. The evaporator also includes wiper assemblies configured to form a liquid film on the evaporation surfaces, condensate scoops located in the respective inner cavities of the distillation elements and configured to collect a condensate from the condensation surfaces, a condensate manifold extending through the vapor manifold and configured to receive the condensate from the condensate scoops, and a drive assembly configured to rotate the rotor assembly and including a drive shaft and drive rollers disposed on the drive shaft and contacting outer circumferential contact surfaces of the distillation elements.

A sewage treatment machine comprising: a closed container inside which the liquid to be treated is brought to boil; a vacuum-generating apparatus, which is adapted to maintain the inside of the closed container at a given pressure having a value lower than the environmental/external pressure; a heat-pump assembly which is associated to the closed container so as to be able to transfer heat to the liquid present on the bottom of the closed container, thus to bring said liquid to boil, and simultaneously remove heat from the vapours that reach the top of the closed container, thus to condense the vapour and obtain a distilled liquid, and which contains a refrigerant fluid comprising one or more gases of the family of the hydrofluoroolefins in a percentage greater than 3%.

A method for producing a transfer mixture by the direct dissolution method in a thin film evaporator (D) having a feed, a housing and a discharge, wherein the feed introduces a product consisting essentially of cellulose, water and a functional liquid into the housing, wherein an evaporator shaft (5) situated in the housing (4) rotationally wipes the product over the heated interior of the housing (4), wherein the product heats up and some of the water evaporates, so that the transfer mixture is obtained, wherein (a) the transfer mixture is discharged before the product substantially overheats; and (b) all heating surfaces of the thin film evaporator in contact with the product are subjected to a heating temperature, which is at least 20K above the temperature of the product.

Systems and methods for generating a thin film of a fluid are described. In an embodiment, a fluid support structure may be configured to receive a fluid, such as water, at a top surface and to support the fluid over at least a portion of the top surface. Channels may be formed in the top surface of the fluid support structure. Wiper blades may be configured to move over the top surface in contact with at least a portion of the fluid to form the fluid into a thin film. The wiper blades may include protrusions corresponding to the channels. As the wiper blades move over the top surface, the protrusions may move within the channels forming a thin film of the fluid within the channels. According to some embodiments, the fluid support structure may be configured as an evaporation surface configured to facilitate the evaporation of the fluid.

A method for cleaning a contaminated solvent used to treat a gas stream, for example a contaminated glycol or a contaminated amine stream, by vacuum evaporation using a mechanically-maintained horizontally-orientated thin film evaporator, where the contaminant material is recovered from the thin film in solvent-free form, as either a heavy organic material or as free flowing salts.

An evaporation-condensation system and methods of manufacturing and using the same are disclosed. The system may include a condensation surface having one or more wipers and a gas diffusion apparatus. The one or more wipers may be configured to move over the condensation surface to displace one or more of fouling material and condensed material that may be present on the condensation surface. The gas diffusion apparatus may include one or more anti-gas blades positioned substantially parallel to the condensation surface and one or more gas storage areas. The gas diffusion apparatus may be configured to guide an amount of vapor molecules towards the condensation surface and promote condensation of the vapor molecules by rotating the one or more anti-gas blades around a central axis and displacing an amount of non-condensable gas into the one or more gas storage areas.

A vertical centrifugal thin film evaporator is equipped with: a cylindrical body in which an central axis of a circle is set in a vertical direction; a rotor that rotates an interior of the cylindrical body in a circumferential direction thereof; a wiper that slides on an inner circumferential surface of the cylindrical body; a fixing support that fixes the wiper and is mounted on the rotor; and a heater that heats a circumferential surface of the cylindrical body. A liquid-withdrawing structure that communicates between a space surrounded by the wiper and the fixing support and a space outside the wiper and the fixing support is formed on at least one of the wiper and the fixing support, thereby preventing a liquid to be processed from being retained between the wiper and the fixing support.

A thin-film treatment apparatus for treating viscous material, including a housing, having a heatable and/or coolable housing casing, which encloses a rotationally symmetric treatment chamber extending in the axial direction, an inlet port, arranged in an inlet region of the housing, for feeding the material to be treated into the treatment chamber, an outlet port, arranged in an outlet region of the housings, for discharging the material from the treatment chamber, and a coaxially extending, drivable rotor shaft, arranged in the treatment chamber, for producing a material film on the inner face of the housing casing and for conveying the material in the direction from the inlet region toward the outlet region, the rotor shaft including a central rotor shaft body and rotor blades arranged on the circumference thereof, the radially outermost end of which rotor blades is distanced from the inner face of the housing casing.

A distiller for processing liquid influent, including a heating chamber. An evaporation arrangement can be positioned above the heating chamber and can include spaced apart evaporation surfaces forming a bottom evaporation stage, multiple intermediate evaporation stages, and an upper evaporation stage. The bottom evaporation stage can be in thermal contact with the heating chamber, and the multiple intermediate and upper evaporation stages can be sequentially positioned above the bottom evaporation stage one above another. The bottom and intermediate evaporation stages can evaporate at least a portion of the liquid influent applied thereon forming vapor and heating the stage positioned above with the vapor. A liquid delivery system can provide the liquid influent to the upper evaporation stage for initial evaporation, and transfer at least a portion of the liquid influent in the upper evaporation stage and intermediate evaporation stages downwardly in sequence to a stage below until reaching the bottom evaporation stage for sequential evaporation at each evaporation stage. A solids transfer system can move solids on an evaporation surface of the bottom evaporation stage remaining from evaporated liquid influent to the heating chamber for combustion and providing heat.