Patent classifications
B01D9/0009
Method for drying and purifying lithium bis(fluorosulfonyl)imide salt
A method for drying and purifying a lithium bis(fluorosulfonyl)imide salt. Also, a method for producing a lithium bis(fluorosulfonyl)imide salt which is then dried and purified by the method. Further, a composition containing lithium bis(fluorosulfonyl)imide salt having a water content by mass of between 5 and 45 ppm. And, the use of the composition C in Li-ion batteries.
A PROCESS FOR OBTAINING 4,4'-DICHLORODIPHENYL SULFONE
The invention relates to a process for obtaining 4,4′-dichlorodiphenyl sulfone from an organic mixture comprising 4,4′-dichlorodiphenyl sulfone and a linear C.sub.6 to C.sub.10 carboxylic acid as organic solvent, comprising: (a) cooling the organic mixture by (a1a) mixing the organic mixture with water in a crystallization vessel to obtain a liquid mixture; (a1b) cooling the liquid mixture obtained in (a1a) to a temperature below the saturation point of 4,4′-dichlorodiphenyl sulfone by (i) reducing the pressure in the crystallization vessel to a pressure at which the water starts to evaporate, (ii) condensing the evaporated water by cooling, (iii) mixing the condensed water into the liquid mixture in the crystallization vessel, to obtain a suspension comprising crystallized 4,4′-dichlorodiphenyl sulfone; or by (a2) bringing the organic mixture into contact with at least one coolable surface and thereby reducing the temperature in the organic mixture with a cooling rate in the range from 5 to 50 K/h until a temperature in the range from 10 to 30° C. is reached, wherein the organic mixture and the at least one coolable surface have a temperature difference which is kept during the whole cooling process in the range from 1 to 30 K to obtain a suspension comprising crystallized 4,4′-dichlorodiphenyl sulfone. (b) carrying out a solid-liquid-separation of the suspension obtained in (a1b) or in (a2) to obtain a residual moisture containing solid 4,4′-dichlorodiphenyl sulfone as product and mother liquor comprising the organic solvent and water.
METHOD FOR DRYING AND PURIFYING LITHIUM BIS(FLUOROSULFONYL)IMIDE SALT
A method for drying and purifying a lithium bis(fluorosulfonyl)imide salt. Also, a method for producing a lithium bis(fluorosulfonyl)imide salt which is then dried and purified by the method. Further, a composition containing lithium bis(fluorosulfonyl)imide salt having a water content by mass of between 5 and 45 ppm.
And, the use of the composition C in Li-ion batteries.
CONTINUOUS CRYSTALLIZATION OF CANNABINOIDS IN A TUBULAR FLOW REACTOR
Disclosed herein is a method for producing crystalline cannabinoid particles in continuous mode. The method comprises preparing a cannabinoid-rich solution that comprises a first cannabinoid, and inducing the cannabinoid-rich solution to a supersaturated state in which the first cannabinoid has a supersaturated concentration that is greater than a corresponding saturation concentration of the first cannabinoid. The method further comprises flowing the cannabinoid-rich solution through a tubular reactor in a continuous manner under turbulent flow conditions to form a plurality of crystalline cannabinoid particles and a cannabinoid-depleted solution within the tubular reactor, and separating crystalline cannabinoid particles from the plurality of crystalline cannabinoid particles and the cannabinoid-depleted solution. The turbulent flow conditions are defined by a Reynold number that is greater than a critical Reynolds number for the cannabinoid-rich solution and the tubular reactor.
CONTINUOUS CRYSTALLIZATION OF CANNABINOIDS IN A STIRRED-TANK REACTOR
Disclosed herein is a method for continuously preparing crystalline cannabinoid particles. The method includes preparing a cannabinoid-rich solution that comprises a first cannabinoid and inducing the cannabinoid-rich solution to a supersaturated state in which the first cannabinoid has a supersaturated concentration that is greater than a corresponding saturation concentration of the first cannabinoid. The method includes flowing the cannabinoid-rich solution into a continuous stirred-tank reactor (CSTR) in a continuous manner, mixing the cannabinoid-rich solution under turbulent mixing conditions to form a plurality of crystalline cannabinoid particles and a cannabinoid-depleted solution within the CSTR, and discharging the plurality of crystalline cannabinoid particles and the cannabinoid-depleted solution from the CSTR in a continuous manner to provide a flow rate through the CSTR. The method includes separating crystalline cannabinoid particles from the plurality of crystalline cannabinoid particles and the cannabinoid-depleted solution in a continuous manner.
Systems and methods for separating surface materials from a fluid using acoustic pressure shock waves
A method of separating material, such as foam, sludge, oil or grease, at a fluid's surface, by applying acoustic pressure shock waves to the material and the fluid's surface such that acoustic pressure shock waves are propagated in liquid medium of the fluid and in gas medium above the fluid surface.
Method for improving nucleation of crystals from solution
The present invention is related to a method for nucleating crystals from a solution comprising the steps of: injecting in a first capillary (1) tube an under saturated solution comprising a solvent and a soluble compound to be crystallised; changing the local conditions of the solution downstream of the capillary tube (1) to supersaturated conditions above the metastable conditions, the transition time of the fluid flowing in the capillary tube between the under saturated conditions and the supersaturated conditions above the metastable conditions being less than 1000 ms, preferably below 100 ms, even more preferably less than 10 ms.
Prebiotic formulation
A method of generating an oligosaccharide encapsulated cannabidiol (CBD) formulation includes forming a cannabidiol ethanol mixture comprising ethanol and cannabidiol, forming an oligosaccharide CBD slurry by mixing the oligosaccharide with the cannabidiol ethanol mixture. The slurry is heated and mixed in a pressurized chamber to form a colloidal mixture, which is distributed into a tray as a layer. A cover is added to the tray to form an evaporation vessel, which is heated in a heating chamber. A rapid cooling process is performed on the colloidal mixture layer by removing the cover and spraying pulverized dry ice on the layer. The rapid cooling process is repeated until crystal formation is detected within the layer, the crystals including oligosaccharide encapsulated cannabidiol. An oligosaccharide encapsulated cannabidiol formulation includes cannabidiol and at least one oligosaccharide in a ratio in the range between about 1000:1 to 2200:1 (w/w) of CBD.
Injectable Suspensions
The present invention relates to aseptic suspensions, physically stable and injectable through a 25 G needle or thinner, comprising crystalline, non-micronized 3-beta-hydroxy-5-alpha-pregnan-20-one particles, a mixture of acylglycerols and cholesterol, processes for preparing crystalline, non-micronized, 3-beta-hydroxy-5-alpha-pregnan-20-one suitable for such suspensions, as well as methods for manufacturing such suspensions.
SOLIDS SEPARATION AND RECOVERY SYSTEM
A separator is provided for removing hydrocarbons and fluid from solids from a slurry. The separator includes a first separator tank for receiving a slurry of fluid and solids contaminated with hydrocarbons, said first separator tank comprising agitating means for agitating hydrocarbons to separate from the slurry and rise as foam and comprising a lower end to collect the solids; a first centrifuge in communication with the lower end of the first separator tank to receive and centrifuge the solids to further remove hydrocarbons therefrom, said first centrifuge comprising a fluid return to return fluids to the first separator tank; a second separator tank for receiving solids from the first centrifuge, said second separator tank comprising agitator means for agitating hydrocarbons to separate from the slurry and rise as foam and comprising a lower end to collect solids; a second centrifuge in communication with the lower end of the second separator tank to receive and centrifuge the solids to further remove hydrocarbons therefrom, said second centrifuge comprising a fluid return to return fluids to the second separator tank; and one or more settling tanks connected in series with each of said first and second separator tanks for further separation of hydrocarbons from fluid. Solids exiting the first and second centrifuges are at least 99% free of hydrocarbons.