A method of preparing organic or inorganic nanoparticles is useful in the manufacture of of fertilizers, pharmaceutical or phytopharmaceutical active ingredients, or insensitive energy materials. The method includes preparing a solution of a compound in a solvent, heating the solution under a pressure ranging from 3 to 300 bars at a temperature higher than the boiling point of the solvent, atomizing the solution in an spray drying chamber using at least one dispersion device and at an angle ranging from 30 to 150 under pressure ranging from 0.0001 to 2 bars, separating the solvent in gaseous form, and recovering the nanoparticles.

The present invention relates to a process for the preparation of Trisodium (4-{[(1S.3R)-1-([1,1-biphenyl]-4-yl-methyl)-4-ethoxy-3-methyl-4-oxobutyl]amino}-4-oxo butanoate)-(N-pentanoyl-N-{[2-(1H-tetrazol-1-id-5-yl)[1,1-biphenyl]-4-yl]methyl}-L-valinate) represented by the following structural formula-1: ##STR00001##

Disclosed is a process for the preparation of a urea product suitable for being diluted with water so as to form an aqueous urea comprising solution for use in a unit for the reduction of NOx in combustion engine exhaust gases, also known as Diesel Exhaust Fluid (DEF) or to be used in De NOx systems of exhaust vapor from industrial furnaces. The process comprises obtaining an aqueous urea solution from or after a recovery section in a urea production process. This solution, which has a low content of impurities, is subjected to flash crystallization at a low pressure, so as to obtain a solid crystallized urea containing product, which is a free-flowing powder containing less than 0.2 wt. % water. This product is packaged under conditions such that the water content in the packaged product is maintained below 0.2 wt. %. The invention can also be used in a method of increasing the capacity of an existing urea plant.

A surfactant-assisted self-assembly method can be used to crystallize energetic materials with controlled morphology. Microparticles of hexanitrohexaazaisowurtzitane (CL-20) formed by this method may have enhanced functional reproducibility due to their monodisperse nature, and decreased shock sensitivity due to their sub-2 m particle size.

An automated production line for preparing cannabidiol (CBD) extracts is disclosed. The production line comprises sequentially a solvent dispensing tank, an extraction tank, a first concentration tank, a dilution tank, a filter, a second concentration tank, a chromatography column and a crystallization device. Each of these elements is connected to and controlled by a central controller. The controller can control the operation of these elements such that one element may operate independently of the other. Hence, each of these elements may operate for a sufficient period of time to allow the completion of the particular CBD production step carried out by that particular element. The amount of operations by humans may be reduced, thereby increasing the production efficiency.

A method of forming lithium carbonate from a lithium-bearing solution including: evaporating the lithium-bearing solution to precipitate a first group of impurities; removing the first group of impurities to form a first purified solution; and performing a flash crystallisation step within a predetermined temperature range to crystallise a second group of impurities from the first purified solution; removing the second group of impurities from the first solution to form a second purified solution, wherein at least 90 wt % of lithium is recovered from the first purified solution; and reacting the second purified solution with a metal carbonate to form lithium carbonate of at least 90 wt % purity.

Boron nitride nanotube (BNNT) material can be placed in large volume configurations such as needed for cryopumps, high surface area filters, scaffolding for coatings, transition radiation detectors, neutron detectors, and similar systems where large volumes may range from cubic millimeters to cubic meters and beyond. The technology to secure the BNNT material includes creating a scaffold of a material acceptable to the final system such as stainless steel wires for a cryopump. The BNNTs can be arranged in the scaffold by freeze drying, filtration technologies, conformal surface attachment and BNNT glue where the as-synthesized BNNT material has been partially purified or fully purified and dispersed in a dispersant.

We provide an evaporation based method for water recovery from gasification wastewater to achieve zero liquid discharge. Grey water from a gasification system is processed by an evaporation system which recovers >99% of the influent water and generates a solid phase in a crystallizing reactor. The crystallizing reactor converts dissolved solids present as highly soluble species into alternative chemical forms that are amenable to precipitation and removal from the liquid phase to achieve zero liquid discharge.

A processing unit for a liquid washing medium contaminated with sulphur oxides and/or nitrogen oxides, has an evaporation stage for concentrating the active components of the washing medium by an evaporator and/or by a heat exchanger, and has a collecting tank connected to the evaporator and/or to the heat exchanger. The collecting tank is configured as a crystallizer for removing sulfur oxides from the washing medium by crystallization of a sulphate, in particular of potassium sulphate. A separating device for carbon dioxide has a corresponding processing unit, and a method for processing a washing medium contaminated with sulphur oxides and/or nitrogen oxides uses a corresponding processing unit.

A method (10) for the processing of lithium containing brines, the method comprising the method steps of: (i) Passing a lithium containing brine (12) to a filtration step (14) to remove sulphates; (ii) Passing a product (16) of step (i) to a first ion exchange step (18) to remove divalent impurities; (iii) Passing a product (20) of step (ii) to a second ion exchange step (22) to remove boron impurities; (iv) Passing a product (24) of step (iii) to an electrolysis step (26) to produce lithium hydroxide (28); and (v) Passing a product (30) of step (iv) to a crystallisation step (32) that in turn provides a lithium hydroxide monohydrate product (34).