摘要:
A continuous extraction system for countercurrent chromatography to achieve continuous solvent extraction, is disclosed wherein two immiscible solvents move in opposite directions through a rotating helical column (11). The coiled tube (11) has two pairs of flow connecting tubes, I u and I u to respectively feed and collect phase 1, and II u and II u to respectively feed and collect phase II. Elution of a desired phase takes place by use of a separation device at the head end which selects either the heavier or the lighter phase. This may consist of a suitably weighted suspended outlet tube (18) of Figure 2 in a rotating cylindrical outlet chamber (16) or may consist of a shunt "S" and settling chamber (40 of Figure 6) located outside the rotating part; the heavier phase may be removed from the bottom and the lighter phase may be removed from the top.
摘要:
The invention relates to a method for extraction and separation of cannabinoids from industrial hemp, designed for medicinal purposes, and also the preparation of an extract, not containing tetrahydrocannabinol, and the preparation of maximum refined individual cannabinoids. The advantage of the method according to the invention consists in the preparation of an extract from hemp, which contains at a high percentage medically useful cannabinoids and doesn't contain undesirable admixtures and tetrahydrocannabinol, so that it can be used without any restrictions as a pharmaceutical. Moreover, the method allows the possibility of separation, if required, into individual useful cannabinoids as pure compounds, in ecological terms, without environmental pollution, as it is according to the most synthetic methods. The possibility of producing pure compounds represents a great contribution to the research of substances, related to a concrete medical application and the preparation of various combinations thereof, with the objective of expansion the field of application. The method is also cost-effective. The method consists in that the extract, obtained in accordance with various methods, undergoes a centrifugal countercurrent liquid-liquid chromatography, as the operation includes a centrifugation of solvents and the extract, obtained during the previous operations; the solvents form two phases, the phase, which the extract is dissolved in, is mobile, and the other one is stationary, whereby the mobile phase passes through the stationary phase, wherein several amounts of the components of the extract content are captured; this passing of the mobile phase through the stationary phase is repeated many times, until separation of the desired substances, which are analyzed in a familiar way, whereby as stationary phase solvents are used, which are selected from the group of straight-chain and branched-chain hydrocarbons, produced from crude oil, straight-chain and/or branched-chain alcohols, straight-chain and/or branched-chain ketones, straight-chain and/or branched chain carboxylic acids, straight-chain and/or branched-chain nitriles, gases in supercritical and subcritical condition, like carbon dioxide, nitrogen, nitrogen oxides, water with modified acidity with or without salts of organic and non-organic substances dissolved therein, as for example NaS0 3 , carbonate compounds or mixtures of the above-mentioned solvents, and as mobile phase solvents are used, which are selected from the group of straight-chain and branched-chain hydrocarbons, produced from crude oil, straight-chain and/or branched-chain alcohols, straight-chain and/or branched-chain ketones, straight-chain and/or branched chain carboxylic acids, straight-chain and/or branched-chain nitriles, gases in supercritical and subcritical condition, like carbon dioxide, nitrogen, nitrogen oxides, water with modified acidity by organic and/or inorganic acids and bases, as well as Lewis acids and bases in the interval from 0 to 14 pH, with or without salts of organic and non-organic substances dissolved therein, as for example NaS0 3 , carbonate compounds, or mixtures of the above-mentioned solvents, while the choice of the solvents between the two phases is conditional on that, they shall be different and immiscible with each other; the centrifugation revolutions and the flow speed of the mobile phase are designed (calculated or determined experimentally) depending on the total phase volume; thus at the finish of the process the tetrahydrocannabinols and/or the tetrahydrocannabinol acids are separated from the remaining cannabinoids and/or cannabinoid acids in the solution, the other cannabinoids in the process can also be separated as a pure substance, separate in a solution and the solvents are evaporated respectively, in order to obtain a pure substance.
摘要:
The present invention relates to a counter-current extraction process involving a plurality of mixing and separation stages for fractionating a phospholipid-containing feed material into two or more fractions enriched in one or more phospholipids, comprising (a) contacting the phospholipid-containing starting material under agitation with an extractant comprising an aliphatic alcohol selected from C1 to C3 alcohols; (b) separating the obtained emulsion into a phospholipid-enriched extract from a residual raffinate.
摘要:
The present invention relates to a device and a method for placing immiscible fluid phases in contact with each other by means of centrifugal force, in particular in order to extract compounds from one of said phases by another phase. Said device comprises at least one contacting unit (3*) which is capable of being rotated about an axis (X'X) and which includes a plurality of cells (210, A, D) intended to be passed through consecutively by said phases, in a given flow direction, each cell being provided with two inlet/outlet channels (214 and 215) which fluidly connect the cells together in pairs and which lead into each cell, respectively, via two inlet/outlet openings, which are proximal (214a) and distal (215a) relative to the said axis, respectively. According to the invention, for at least two adjacent cells (A and D) of said at least one unit, the two proximal (214a) or else distal (215a) openings thereof are connected together directly via one of said channels (214 or 215), whereby said phases flow through one of said adjacent cells towards said axis and through the other cell while moving away from said axis.
摘要:
L'extracteur comprend des moyens pour le recyclage de l'un au moins des deux liquides (A et B) à la sortie de la chambre de décantation en vue de le réintroduire dans la chambre de mélange. Le brevet décrit l'application de l'invention aux extracteurs centrifuges du type mono-étage et du type multi-étages.
摘要:
Apparatus for effecting mass transfer between two fluid phases the first of which is a liquid, which apparatus comprises (a) an element (9) which is permeable to the fluids, which has pores which present a tortuous path to the fluids, and which is rotatable about an axis such that the fluids, are subjected to a mean acceleration of at least 300 m sec- 2 as they flow through the pores with the first fluid flowing radially outwards away from the said axis, (b) means for charging the fluids to the permeable element and (c) at least means for discharging one of the fluids or a derivative thereof from the permeable element, characterised in that the permeable element comprises strands, fibres, fibrils or filaments or mixtures thereof. The apparatus may be used in absorption, distillation or extraction processes.
摘要:
Dans un systeme d'extraction continu pour la chromatographie a contre-courant pour obtenir une extraction continue de solvants, deux solvants non miscibles se deplacent en directions opposees a travers une colonne helicoidale rotative (11). Le tube helicoidal (11) presente deux paires de tubes de derivation, IF et IC pour respectivement alimenter et recueillir la phase I, et IIF et IIC pour alimenter et recueillir la phase II. La separation et la phase desiree s'obtient au moyen d'un dispositif de separation a l'extremite de tete qui selectionne la phase lourde ou la phase legere. Ce dispositif peut consister en un tube de sortie (18) convenablement equilibre dans une chambre de sortie cylindrique rotative (16), ou peut etre constitue par une derivation "s" et une chambre de stabilisation (40) situee en dehors de la partie rotative; la phase lourde peut etre extraite du fond et la phase legere de la partie superieure.
摘要:
The present invention relates to a counter-current extraction process involving a plurality of mixing and separation stages for fractionating a phospholipid-containing feed material into two or more fractions enriched in one or more phospholipids, comprising (a) contacting the phospholipid-containing starting material under agitation with an extractant comprising an aliphatic alcohol selected from C1 to C3 alcohols; (b) separating the obtained emulsion into a phospholipid-enriched extract from a residual raffinate.