A filtering and concentrating apparatus having a stirring function for small ternary precursor particles, comprising a barrel (100). One end of the barrel (100) is provided with a first closure (101), and the other end of the barrel (100) is provided with a second closure (102). The barrel (100) or the first closure (101) or the second closure (102) is provided with a feed port (103). One or more discharge pipes (200) are provided on the inner wall of the barrel (100). Microporous filtering mediums (300) communicated with the interior of the discharge pipe (200) are provided on the discharge pipe (200). An end portion of the discharge pipe (200) is communicated with the exterior of the barrel (100). A stirring means (800) is provided inside the barrel (100).

A method for crystallizing calcium nitrate from an aqueous calcium nitrate composition including from 6 to 12 weight % nitric acid, from 11 to 17 weight % phosphoric acid, and from 36 to 49 weight % dissolved calcium nitrate, which aqueous composition is optionally directly obtainable from digesting phosphate rock in nitric acid. The method includes filling at least one vertical crystallizing tank through an inlet with the aqueous calcium nitrate composition. The crystallizing tank includes a vertical cylindrical section, a first inlet, a first outlet, a second inlet, three concentric banks of cooling coils, an agitator, and a temperature measurement device. The method includes circulating through the banks of cooling coils a cooling fluid, having an initial temperature ranging from −40° C. to −5° C., and rotating the agitator such that a minimum average heat transfer of 400 W/m.sup.2.Math.K is achieved on the cooling coil the most distant from the agitator.

Provided is a degassing apparatus having a fluid flow surface positioned within a tank and configured for decreasing the velocity of the fluid flowing through the tank; a cryogen fluid cooling system including the degassing apparatus positioned in fluid communication with a cryogen injector of the system; and a direct cryogen fluid cooling method including flowing fluid containing cryogen into a degassing apparatus for decreasing a velocity of and for removing cryogen gas from the flowing fluid.

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.

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.

A method for isolating curcuminoids from turmeric rhizome includes the steps of a) subjecting the turmeric rhizome to extraction with a first ethanol solution having an ethanol concentration ranging from 90% to 100% at a stirring speed ranging from 100 rpm to 300 rpm so as to obtain an ethanol-extracted product; and b) subjecting the ethanol-extracted product to crystallization with a second ethanol solution having an ethanol concentration ranging from 90% to 100 at a temperature ranging from 2° C. to 8° C. and a stirring speed ranging from 40 rpm to 300 rpm so as to obtain the curcuminoids.

Embodiments may provide systems and method for purifying natural and/or organically certified nutraceuticals, such as cannabinoids. Embodiments may include refined or unrefined solvents, refined or unrefined plant extracts, refined or unrefined source compounds to be purified to any degree. Embodiments may reduce the concentration of impurities such as other cannabinoids (e.g., THC), terpenes, pesticides, herbicides, mycotoxins, heavy metals, other solvents (e.g., ethanol), waxes, or other impurities. Embodiments may increase the concentration of target compound(s) from its respective source material.

An apparatus for purifying diamond CBD oil crystals. A cylindrical glass or metal vessel is provided and supported by least one support post, the vessel having an upper portion and a lower surface having laser etched nucleation sites for initiating crystal growth. A removable head is engageable with the upper portion of the vessel, the head having an uppermost portion and a plurality of ports extending therethrough. A pressurized nitrogen tank is operatively connected to a port of the head, as is a pressure gauge. A safety valve is disposed at the uppermost portion of the head. Optionally, an inline desiccant chamber is also operatively connected to the head. The apparatus crystalizes cannabinoids in either a solventless process or a solvent process.

A fluid processing method with which processing properties of fluids to be processed can be effectively controlled. Processing surfaces which are capable of being brought closer to each other and being separated from each other, and which rotate relatively are provided. A fluid to be processed is made to pass from inside to outside in a processing area between the processing surfaces to obtain a fluid thin film, and the resultant fluid thin film of the fluid to be processed is subjected to processing. Processing properties are controlled by changing the ratio of the distance to an outer peripheral end from a centre of rotation.

A device and method for increasing solid holdup in a reaction crystallizer are disclosed. The device includes a discharge pipe, a clear liquid pipe, a clear liquid tank and a gas collecting pipe. A lower end of the discharge pipe is inserted into the crystallizer below the liquid level, while that of the clear liquid pipe is inserted into the clear liquid tank below the liquid level. By using the gas collecting pipe, the reaction crystallizer and the clear liquid tank are communicated all the time. When feeding, a liquid-solid mixture in the crystallizer automatically enters the discharge pipe and flows upward slowly therein, during which solid particles gradually settle down and automatically fall back into the crystallizer while the clear liquid keeps on flowing upward, enters the clear liquid pipe and thereby flows into the clear liquid tank. The clear liquid tank maintains a constant liquid level via overflowing.