An etching solution recycling system for a wafer etching apparatus is provided. The etching solution recycling system includes a settling tank, a seed provider, and a fluid control unit. The settling tank is connected to an etching tank of the wafer etching apparatus and configured to receive an etching solution from the etching tank. The seed provider is configured to provide at least one seed crystal into the settling tank to reduce the silicate concentration in the etching solution in the settling tank. The fluid control unit is configured to deliver the etching solution in the settling tank back into the etching tank.

A method for producing high purity D-psicose crystals having a purity of 98% (w/w) or more and a grain size of MA200 or more. The method includes: removing impurities from a D-psicose solution to obtain a purified D-psicose solution; concentrating the purified D-psicose solution; cooling the concentrated D-psicose solution to 30 C. to 40 C. through a heat exchanger; seed crystallizing the D-psicose solution at 30 C. to 40 C. to obtain a seed crystallized massecuite; and full-scale crystallizing the seed crystallized massecuite. The method can produce pure D-psicose crystals in a suitable form for industrial application through an economical crystallization process from the D-psicose solution without using organic solvents.

A method of desalinating water through application of acoustic pressure shock waves to a slush to separate ice crystals from brine and recovering desalinated water from the separated ice crystals.

The present invention relates to sylvinite ore processing in the extraction industry and provides a resource-efficient method of separating potassium chloride and sodium chloride from polymineral sources comprising potassium chloride and sodium chloride and a vertical three-zone reactor for separating potassium chloride and sodium chloride from polymineral sources comprising potassium chloride and sodium chloride.

A reverse osmosis desalination system for treating feed water, the feed water containing minerals, the system comprising a reverse osmosis unit comprising a first reverse osmosis stage (21) and a second reverse osmosis stage (22), each of the reverse osmosis stages (21, 22) having a feed water input, a product water outlet and a brine outlet, and a fluidized bed crystallizer (30), configured to remove minerals from the water, wherein the fluidized bed crystallizer (30) receives brine from the first reverse osmosis stage (21) and passes treated water to the feed water input of the second reverse osmosis stage (22).

The present invention relates to a three-phase methodology to obtain a highly concentrated, purified chemical component from plant material in an industrial setting. The three phases of the methodology of the present invention include Phase 1: Preparing and solubilization, Phase 2: Separation and Salting and Phase 3: crystallization. The methodology results in dried composition purified from a plant material having at least 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, or 95% of the chemical component by weight.

Stable liquid formulations dominant in cannabidiol (CBD) can be manufactured by a sequential process of purification to create a formulation that does not crystallize under a variety of storage and use conditions, and without the use of potentially harmful additives. For example, the formulation may be used in vaporization devices (i.e., electronic cigarettes) that typically require formulations to remain in a non-crystalline, non-solid, or non-partially solid state. The liquid formulations dominant in CBD may further contain other phytocannabinoids, including, but not limited to, tetrahydrocannabinol (THC), cannabigerol (CBG), cannabichromene (CBC), cannabinol (CBN), and cannabidivarin (CBDV) in higher concentrations than unrefined and refined cannabis extracts obtained via existing methods.

Novel crystalline ponatinib hydrochloride forms designated Form alpha and Form beta are disclosed. Form alpha is characterized by data selected from an XRPD pattern with peaks at about 6.5, 9.0, 12.25, 14.4, 16.70, 19.6, 22.2, 24.5, 28.20.2 degrees 2-theta; an XRPD pattern substantially as depicted in FIG. 1; and/or a combination thereof. Form beta is characterized by data selected from an XRPD pattern with peaks at about 10.7, 15.2, 15.8, 16.4 23.1, 25.0, 27.80.2 degrees 2-theta; an XRPD pattern substantially as depicted in FIG. 3; and/or combinations thereof. Processes for making Form alpha and Form beta are disclosed.

The invention relates to a process of creating particles of controlled size by creating them in the interstitial regions in a batch, semi-continuous, or continuous liquid phase. The method comprises making solid particles comprising: adding a precursor material to a liquid carrier to form a liquid continuous phase, wherein the concentration of the precursor material is from about 5% to about 99% by weight of the continuous liquid phase; adding an inert phase into the liquid continuous phase of step a, resulting in an inert phase and continuous liquid phase mixture having a volume fraction of the inert phase of from about 30% to about 98% and inert phase domain size of about 0.2 to about 200 m; transforming the precursor material physically or chemically, resulting in the formation of solid particles.

Method and apparatus for temperature controlled processes in a vessel to provide improved process control, in particular to enable controlled temperatures to be applied to a substance in different process zones of a vessel, has a series of tubular members arranged and operatively connected in a flow system, and each process zone has temperature regulating means juxtaposed thereto for effecting temperature control therein.