A composition comprising a cannabidiol at least one compound selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, delta-8-tetrahydrocannabinols, delta-9-tetrahydrocannabinols, or any combination thereof; and a terpene. A nanoemulsion comprising a cannabidiol; a terpene; and an aqueous fluid, wherein the cannabidiol and terpene are in an emulsion in the aqueous fluid. A full spectrum hemp oil composition comprising at least one stereoisomer of tetrahydrocannabinol; cannabinodiol; and at least one cannabinoid selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, and a combination thereof.
C07C 37/82 - SéparationPurificationStabilisationEmploi d'additifs par traitement physique par traitement solide-liquideSéparationPurificationStabilisationEmploi d'additifs par traitement physique par absorption-adsorption chimique
A23L 29/00 - Aliments ou produits alimentaires contenant des additifsLeur préparation ou leur traitement
A23L 35/00 - Aliments ou produits alimentaires non prévus par les groupes Leur préparation ou leur traitement
The present disclosure generally relates to the enrichment of diglycerides (DAGs) over triglycerides (TAGs) in a naturally derived free fatty acid matrix. More particularly, the disclosure relates to the in-situ generation of surfactants naturally present in natural oils and fats, thereby effectively partitioning diglycerides and triglycerides, as minor lipid components, out of the oil phase into an aqueous extraction solution in which the extract is appreciably enriched in DAGs relative to TAGs. The oleaginous matrix can be further separated by inducing phase segregation to reform the neutral form of the surfactants, resulting in a separated concentrated fatty formulation enriched with the DAG composition relative to TAG despite statistical distribution in the starting mixture.
C11B 3/04 - Raffinage des graisses ou huiles par réaction chimique avec des acides
C11B 3/06 - Raffinage des graisses ou huiles par réaction chimique avec des bases
A61K 8/92 - Huiles, graisses ou ciresLeurs dérivés, p. ex. produits d'hydrogénation
A23K 20/158 - Acides grasGraissesProduits contenant des huiles ou des graisses
A23D 9/007 - Autres huiles ou graisses comestibles, p. ex. huiles pour cuisson caractérisées par des ingrédients autres que des triglycérides d'acides gras
An immobilized enzyme fiber contactor includes a plurality of fibers disposed within a hollow conduit. The fibers have an enzyme selected from an oxidoreductase, a transferase, a hydrolase, a lyases, an isomerase, or a ligase attached thereto. The enzymes can be attached to the fibers via an anchor group and, optionally, a bifunctional crosslinker. The enzymes can be applied, stripped, and reapplied without disassembling the reactor or discarding the fibers. The immobilized enzyme fiber contractor can be used to conduct two-phase or single-phase enzymatic reactions.
C12N 11/04 - Enzymes ou cellules microbiennes immobilisées sur ou dans un support organique piégées à l’intérieur du support, p. ex. dans un gel ou dans des fibres creuses
An immobilized enzyme fiber contactor includes a plurality of fibers disposed within a hollow conduit. The fibers have an enzyme selected from an oxidoreductase, a transferase, a hydrolase, a lysase, an isomerase, or a ligase attached thereto. The enzymes can be attached to the fibers via an anchor group and, optionally, a bifunctional crosslinker. The enzymes can be applied, stripped, and reapplied without disassembling the reactor or discarding the fibers. The immobilized enzyme fiber contractor can be used to conduct two-phase or single-phase enzymatic reactions.
C12M 1/40 - Appareillage spécialement destiné à l'utilisation d'enzymes libres, immobilisées ou liées à un support, p. ex. appareils contenant un lit fluidisé d'enzymes immobilisées
B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés
B01L 3/00 - Récipients ou ustensiles pour laboratoires, p. ex. verrerie de laboratoireCompte-gouttes
5.
IMMOBILIZED ENZYME FIBER REACTOR AND OIL REFINING USING THE SAME
An immobilized enzyme fiber reactor includes a plurality a fibers disposed within a hollow conduit. The fibers have an enzyme, such as a phospholipase, attached thereto. The enzymes can be attached to the fibers via an anchor group and, optionally, a bifunctional crosslinker. The enzymes can be applied, stripped, and reapplied without disassembling the reactor or discarding the fibers. The immobilized enzyme fiber reactor can be used to treat oils including phospholipids, such as soybean oil, and reduce an impurity content thereof.
C12M 1/02 - Appareillage pour l'enzymologie ou la microbiologie avec des moyens d'agitationAppareillage pour l'enzymologie ou la microbiologie avec des moyens d'échange de chaleur
C12M 1/40 - Appareillage spécialement destiné à l'utilisation d'enzymes libres, immobilisées ou liées à un support, p. ex. appareils contenant un lit fluidisé d'enzymes immobilisées
C12N 9/16 - Hydrolases (3.) agissant sur les liaisons esters (3.1)
C12N 11/04 - Enzymes ou cellules microbiennes immobilisées sur ou dans un support organique piégées à l’intérieur du support, p. ex. dans un gel ou dans des fibres creuses
C12N 11/082 - Enzymes ou cellules microbiennes immobilisées sur ou dans un support organique le support étant un polymère synthétique obtenu par des réactions faisant intervenir uniquement des liaisons non saturées carbone-carbone
An immobilized enzyme fiber reactor includes a plurality a fibers disposed within a hollow conduit. The fibers have an enzyme, such as a phospholipase, attached thereto. The enzymes can be attached to the fibers via an anchor group and, optionally, a bifunctional crosslinker. The enzymes can be applied, stripped, and reapplied without disassembling the reactor or discarding the fibers. The immobilized enzyme fiber reactor can be used to treat oils including phospholipids, such as soybean oil, and reduce an impurity content thereof.
A method of remediating cannabinoid containing compositions includes contacting the compounds with an aqueous solution to remove at least one impurity therefrom. The method may include additional contacting with further aqueous solutions of the same or different kind in order to remove additional impurities or higher amounts of the same impurity. A system for remediating cannabinoid containing compositions includes a cannabinoid containing composition supply and an aqueous solution supply fluidly coupled to a conduit reactor and a separator for collecting reaction products between the compound and the aqueous solution.
B01D 15/12 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives à la préparation de l'alimentation
B01D 15/16 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives au conditionnement du fluide vecteur
A method of extracting and isolating psilocybin and/or psilocin from psilocybin fungi includes forming a mixture of the fungi, an extraction solution, and a chitinase capable of digesting chitin present in the fungi. Solids can be filtered from the mixture to yield an extract including psilocybin and/or psilocin. The extract can be purified to isolate the psilocybin and/or psilocin.
C12P 17/10 - Préparation de composés hétérocycliques comportant O, N, S, Se ou Te comme uniques hétéro-atomes du cycle l'azote comme unique hétéro-atome du cycle
C12N 9/42 - Hydrolases (3.) agissant sur les composés glycosyliques (3.2) agissant sur les liaisons bêta-glucosidiques-1, 4, p. ex. cellulase
A method of extracting cannabinoids includes providing wet biomass having cannabinoids and a water activity level of at least 0.55, contacting the wet biomass with an extractant to form an extractant mixture, removing solid biomass from the extractant mixture to form a liquid extract, and removing a cannabinoid-enriched oil layer from the liquid extract.
C07C 51/47 - SéparationPurificationStabilisationEmploi d'additifs par traitement solide-liquideSéparationPurificationStabilisationEmploi d'additifs par absorption-adsorption chimique
C07D 311/70 - Benzo [b] pyrannes non hydrogénés dans le carbocycle avec des substituants autres que des atomes d'oxygène ou de soufre en position 2 ou 4 avec deux radicaux hydrocarbonés liés en position 2 et des éléments autres que le carbone et l'hydrogène en position 6
C07C 37/82 - SéparationPurificationStabilisationEmploi d'additifs par traitement physique par traitement solide-liquideSéparationPurificationStabilisationEmploi d'additifs par traitement physique par absorption-adsorption chimique
C07D 311/58 - Benzo [b] pyrannes non hydrogénés dans le carbocycle avec des substituants autres que des atomes d'oxygène ou de soufre en position 2 ou 4
A method of extracting and isolating psilocybin and/or psilocin from psilocybin fungi includes forming a mixture of the fungi, an extraction solution, and a chitinase capable of digesting chitin present in the fungi. Solids can be filtered from the mixture to yield an extract including psilocybin and/or psilocin. The extract can be purified to isolate the psilocybin and/or psilocin.
B01D 15/12 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives à la préparation de l'alimentation
B01D 15/16 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives au conditionnement du fluide vecteur
A method of extracting cannabinoids includes providing wet biomass having cannabinoids and a water activity level of at least 0.55, contacting the wet biomass with an extractant to form an extractant mixture, removing solid biomass from the extractant mixture to form a liquid extract, and removing a cannabinoid-enriched oil layer from the liquid extract.
A23L 33/105 - Extraits de plantes, leurs doublons artificiels ou leurs dérivés
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
A method of extracting cannabinoids includes providing wet biomass having cannabinoids and a water activity level of at least 0.55, contacting the wet biomass with an extractant to form an extractant mixture, removing solid biomass from the extractant mixture to form a liquid extract, and removing a cannabinoid-enriched oil layer from the liquid extract.
C07C 51/48 - SéparationPurificationStabilisationEmploi d'additifs par traitement liquide-liquide
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
A method of remediating cannabinoid containing compositions includes contacting the compounds with an aqueous solution to remove at least one impurity therefrom. The method may include additional contacting with further aqueous solutions of the same or different kind in order to remove additional impurities or higher amounts of the same impurity. A system for remediating cannabinoid containing compositions includes a cannabinoid containing composition supply and an aqueous solution supply fluidly coupled to a conduit reactor and a separator for collecting reaction products between the compound and the aqueous solution.
An integrated facility for the co-production of ethanol and the pretreatment of impure vegetable oils, waxes and (animal) fats is provided. A by-product from the ethanol plant, such as distillers corn oil or distillers sorghum oil, can be directly refined on site to remove contaminants such as metals, phospholipids and inorganic anions, to enable use as ready feedstocks for a renewable diesel hydrotreatment plant. The utility of the ethanol plant infrastructure can be directly harnessed to pretreat and purify a variety of impure feedstock materials. The pretreatment reduces catalytic poisoning in the reduction process at refining facilities during the synthesis of renewable diesel. By-products of the pretreatment process are recycled to various parts of the ethanol plant for incorporation into the animal feed(s) produced by the ethanol plant or incorporated into the existing wastewater treatment and disposal system within the ethanol plant.
A system for purifying edible oils includes a plurality of microchannel fiber reactors arranged in series. The edible oils may be first neutralized with an alkali solution and then washed with water to thereby remove impurities such as free fatty acids, mono- and diacylglycerols, phospholipids, glycolipids, trace metals, and unsaponifiable matter. The system allows for continuous, high-yield production of improved quality edible oils.
A system for purifying edible oils includes a plurality of microchannel fiber reactors arranged in series. The edible oils may be first neutralized with an alkali solution and then washed with water to thereby remove impurities such as free fatty acids, mono- and diacylglycerols, phospholipids, glycolipids, trace metals, and unsaponifiable matter. The system allows for continuous, high-yield production of improved quality edible oils.
A method for crystallization of cannabinoids includes: providing a substantially pure cannabinoid isolate; dissolving the cannabinoid isolate in a crystallization solvent; removing solvent by evaporation until the solution reaches saturation; adding a seed crystal of said cannabinoid; maintaining a supersaturated solution throughout the recrystallization process by the continual evaporation of solvent throughout the crystallization process by incubating the solution under heat and/or vacuum and repeating this process until crystals of the desired size have been produced.
A non-crystallizing blend includes cannabidiol (CBD) and cannabidiolic acid (CBDA). A method of forming a non-crystallizing blend of CBD and CBDA includes obtaining a CBD isolate including at least 80% by weight CBD, obtaining a CBDA isolate including at least 80% by weight CBDA, and combining and mixing the CBD isolate and the CBDA. A method of treating a condition includes administering a therapeutically effective amount of a non-crystallizing blend of CBD and CBDA to a patient in need thereof.
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
The present disclosure relates to the design of structural features that enable the facile and reproducible fabrication of a microfluidic reactor that eliminates the problem of scaling factors in turn enabling the broad integration of microchannel reactors to industrial scale production. The process is highlighted via the effective and successful scale up of a purification process for the removal of a variety of different classes of impurities from crude vegetable oils mixtures into feedstocks that can be directly integrated into the hydrotreatment vegetable oil hydrogenation process for mass production of synthetic diesel derived from renewable sources.
A method for utilizing the hard cracking of cannabinoids includes providing a substantially pure cannabinoid isolate; optionally, adding terpenes or other flavor additives; optionally, physically mixing the combination; heating the isolate or mixture to a hard cracking point of the cannabinoid for a period of time; rapidly cooling to form a crystalline cannabinoid.
A cannabinoid acid beverage includes an aqueous solution having a pH of greater than 7 and at least one cannabinoid acid dissolved therein. The cannabinoid acid may include CBDA, THCA, CBGA, CBCA, or combinations thereof. A method of preparing the beverage may include heating the solution to increase the solubility of the cannabinoid acid therein.
A23L 33/105 - Extraits de plantes, leurs doublons artificiels ou leurs dérivés
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
A61K 31/352 - Composés hétérocycliques ayant l'oxygène comme seul hétéro-atome d'un cycle, p. ex. fungichromine ayant des cycles à six chaînons avec un oxygène comme seul hétéro-atome d'un cycle condensés avec des carbocycles, p. ex. cannabinols, méthanthéline
A composition comprising a cannabidiol at least one compound selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, delta-8-tetrahydrocannabinols, delta-9-tetrahydrocannabinols, or any combination thereof; and a terpene. A nanoemulsion comprising a cannabidiol; a terpene; and an aqueous fluid, wherein the cannabidiol and terpene are in an emulsion in the aqueous fluid. A full spectrum hemp oil composition comprising at least one stereoisomer of tetrahydrocannabinol; cannabinodiol; and at least one cannabinoid selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, and a combination thereof.
A61K 31/352 - Composés hétérocycliques ayant l'oxygène comme seul hétéro-atome d'un cycle, p. ex. fungichromine ayant des cycles à six chaînons avec un oxygène comme seul hétéro-atome d'un cycle condensés avec des carbocycles, p. ex. cannabinols, méthanthéline
A composition comprising a cannabidiol at least one compound selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, delta-8-tetrahydrocannabinols, delta-9-tetrahydrocannabinols, or any combination thereof; and a terpene. A nanoemulsion comprising a cannabidiol; a terpene; and an aqueous fluid, wherein the cannabidiol and terpene are in an emulsion in the aqueous fluid. A full spectrum hemp oil composition comprising at least one stereoisomer of tetrahydrocannabinol; cannabinodiol; and at least one cannabinoid selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, and a combination thereof.
A61K 31/352 - Composés hétérocycliques ayant l'oxygène comme seul hétéro-atome d'un cycle, p. ex. fungichromine ayant des cycles à six chaînons avec un oxygène comme seul hétéro-atome d'un cycle condensés avec des carbocycles, p. ex. cannabinols, méthanthéline
A23L 33/105 - Extraits de plantes, leurs doublons artificiels ou leurs dérivés
A composition comprising a cannabidiol at least one compound selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, delta-8-tetrahydrocannabinols, delta-9-tetrahydrocannabinols, or any combination thereof; and a terpene. A nanoemulsion comprising a cannabidiol; a terpene; and an aqueous fluid, wherein the cannabidiol and terpene are in an emulsion in the aqueous fluid. A full spectrum hemp oil composition comprising at least one stereoisomer of tetrahydrocannabinol; cannabinodiol; and at least one cannabinoid selected from the group consisting of cannabichromenes, cannabicyclols, cannabidiols, cannabielsoins, cannabigerols, cannabinols, cannabinodiols, cannabitriols, and a combination thereof.
A61K 31/352 - Composés hétérocycliques ayant l'oxygène comme seul hétéro-atome d'un cycle, p. ex. fungichromine ayant des cycles à six chaînons avec un oxygène comme seul hétéro-atome d'un cycle condensés avec des carbocycles, p. ex. cannabinols, méthanthéline
The present disclosure relates to the design of structural features that enable the facile and reproducible fabrication of a microfluidic reactor that eliminates the problem of scaling factors in turn enabling the broad integration of microchannel reactors to industrial scale production. The process is highlighted via the effective and successful scale up of a purification process for the removal of a variety of different classes of impurities from crude vegetable oils mixtures into feedstocks that can be directly integrated into the hydrotreatment vegetable oil hydrogenation process for mass production of synthetic diesel derived from renewable sources.
The present disclosure relates to the design of structural features that enable the facile and reproducible fabrication of a microfluidic reactor that eliminates the problem of scaling factors in turn enabling the broad integration of microchannel reactors to industrial scale production. The process is highlighted via the effective and successful scale up of a purification process for the removal of a variety of different classes of impurities from crude vegetable oils mixtures into feedstocks that can be directly integrated into the hydrotreatment vegetable oil hydrogenation process for mass production of synthetic diesel derived from renewable sources.
A method for utilizing the hard cracking of cannabinoids includes providing a substantially pure cannabinoid isolate; optionally, adding terpenes or other flavor additives; optionally, physically mixing the combination; heating the isolate or mixture to a hard cracking point of the cannabinoid for a period of time; rapidly cooling to form a crystalline cannabinoid.
A method for utilizing the hard cracking of cannabinoids includes providing a substantially pure cannabinoid isolate; optionally, adding terpenes or other flavor additives; optionally, physically mixing the combination; heating the isolate or mixture to a hard cracking point of the cannabinoid for a period of time; rapidly cooling to form a crystalline cannabinoid.
A61K 31/352 - Composés hétérocycliques ayant l'oxygène comme seul hétéro-atome d'un cycle, p. ex. fungichromine ayant des cycles à six chaînons avec un oxygène comme seul hétéro-atome d'un cycle condensés avec des carbocycles, p. ex. cannabinols, méthanthéline
A method of producing biodiesel using a conduit contactor in fluid communication with a collection vessel includes: introducing a first stream including an alcohol proximate a plurality of fibers positioned within the conduit contactor and extending proximate to the collection vessel; introducing a second stream including an oil into the conduit contactor proximate to the plurality of fibers, wherein the second stream is in contact with the first stream; reacting the oil and the alcohol to for a single phase; receiving the single phase in the collection vessel; and separating biodiesel from the single phase.
An integrated facility for the co-production of ethanol and the pretreatment of impure vegetable oils, waxes and (animal) fats is provided. A by-product from the ethanol plant, such as distillers corn oil or distillers sorghum oil, can be directly refined on site to remove contaminants such as metals, phospholipids and inorganic anions, to enable use as ready feedstocks for a renewable diesel hydrotreatment plant. The utility of the ethanol plant infrastructure can be directly harnessed to pretreat and purify a variety of impure feedstock materials. The pretreatment reduces catalytic poisoning in the reduction process at refining facilities during the synthesis of renewable diesel. By-products of the pretreatment process are recycled to various parts of the ethanol plant for incorporation into the animal feed(s) produced by the ethanol plant or incorporated into the existing wastewater treatment and disposal system within the ethanol plant.
C07C 29/00 - Préparation de composés comportant des groupes hydroxyle ou O-métal liés à un atome de carbone ne faisant pas partie d'un cycle aromatique à six chaînons
C07C 29/132 - Préparation de composés comportant des groupes hydroxyle ou O-métal liés à un atome de carbone ne faisant pas partie d'un cycle aromatique à six chaînons par réduction d'un groupe fonctionnel contenant de l'oxygène
C07C 51/377 - Préparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par des réactions ne créant pas de groupes carboxyle par élimination d'hydrogène ou de groupes fonctionnelsPréparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par des réactions ne créant pas de groupes carboxyle par hydrogénolyse de groupes fonctionnels
An integrated facility for the co-production of ethanol and the pretreatment of impure vegetable oils, waxes and (animal) fats is provided. A by-product from the ethanol plant, such as distillers corn oil or distillers sorghum oil, can be directly refined on site to remove contaminants such as metals, phospholipids and inorganic anions, to enable use as ready feedstocks for a renewable diesel hydrotreatment plant. The utility of the ethanol plant infrastructure can be directly harnessed to pretreat and purify a variety of impure feedstock materials. The pretreatment reduces catalytic poisoning in the reduction process at refining facilities during the synthesis of renewable diesel. By-products of the pretreatment process are recycled to various parts of the ethanol plant for incorporation into the animal feed(s) produced by the ethanol plant or incorporated into the existing wastewater treatment and disposal system within the ethanol plant.
C07C 29/00 - Préparation de composés comportant des groupes hydroxyle ou O-métal liés à un atome de carbone ne faisant pas partie d'un cycle aromatique à six chaînons
C07C 29/132 - Préparation de composés comportant des groupes hydroxyle ou O-métal liés à un atome de carbone ne faisant pas partie d'un cycle aromatique à six chaînons par réduction d'un groupe fonctionnel contenant de l'oxygène
C07C 51/377 - Préparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par des réactions ne créant pas de groupes carboxyle par élimination d'hydrogène ou de groupes fonctionnelsPréparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par des réactions ne créant pas de groupes carboxyle par hydrogénolyse de groupes fonctionnels
A method for crystallization of cannabinoids includes: providing a substantially pure cannabinoid isolate; dissolving the cannabinoid isolate in a crystallization solvent; removing solvent by evaporation until the solution reaches saturation; adding a seed crystal of said cannabinoid; maintaining a supersaturated solution throughtout the recrystallization process by the continual evaporation of solvent throughtout the crystallization process by incubating the solution under heat and/or vacuum and repeating this process until crystals of the desired size have been produced.
A method for crystallization of cannabinoids includes: providing a substantially pure cannabinoid isolate; dissolving the cannabinoid isolate in a crystallization solvent; removing solvent by evaporation until the solution reaches saturation; adding a seed crystal of said cannabinoid; maintaining a supersaturated solution throughtout the recrystallization process by the continual evaporation of solvent throughtout the crystallization process by incubating the solution under heat and/or vacuum and repeating this process until crystals of the desired size have been produced.
A method for purification and extraction of cannabinoids includes: providing a cannabis oil including phospholipids and cannabinoid acids; contacting the cannabis oil with a degumming solvent, wherein the degumming solvent and cannabis oil are substantially immiscible; and separating an aqueous phase including the degumming solvent and at least a portion of the phospholipids from an oil phase including the cannabis oil. The method may further include contacting the oil phase with an extraction solvent, where the extraction solvent and oil phase are substantially immiscible; and separating an aqueous phase including the extraction solvent and at least a portion of the cannabinoid acids from a second oil solvent phase including the oil phase and/or simply the liberated cannabinoids following acidification of the extraction solvent.
A cannabinoid acid beverage includes an aqueous solution having a pH of greater than 7 and at least one cannabinoid acid dissolved therein. The cannabinoid acid may include CBDA, THCA, CBGA, CBCA, or combinations thereof. A method of preparing the beverage may include heating the solution to increase the solubility of the cannabinoid acid therein.
A23L 2/00 - Boissons non alcooliséesCompositions sèches ou concentrés pour les fabriquer Leur préparation ou leur traitement
A23L 33/105 - Extraits de plantes, leurs doublons artificiels ou leurs dérivés
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
A method for purification and extraction of cannabinoids includes: providing a cannabis oil including phospholipids and cannabinoid acids; contacting the cannabis oil with a degumming solvent, wherein the degumming solvent and cannabis oil are substantially immiscible; and separating an aqueous phase including the degumming solvent and at least a portion of the phospholipids from an oil phase including the cannabis oil. The method may further include contacting the oil phase with an extraction solvent, where the extraction solvent and oil phase are substantially immiscible; and separating an aqueous phase including the extraction solvent and at least a portion of the cannabinoid acids from a second oil solvent phase including the oil phase and/or simply the liberated cannabinoids following acidification of the extraction solvent.
A method for purification and extraction of cannabinoids includes: providing a cannabis oil including phospholipids and cannabinoid acids; contacting the cannabis oil with a degumming solvent, wherein the degumming solvent and cannabis oil are substantially immiscible; and separating an aqueous phase including the degumming solvent and at least a portion of the phospholipids from an oil phase including the cannabis oil. The method may further include contacting the oil phase with an extraction solvent, where the extraction solvent and oil phase are substantially immiscible; and separating an aqueous phase including the extraction solvent and at least a portion of the cannabinoid acids from a second oil solvent phase including the oil phase and/or simply the liberated cannabinoids following acidification of the extraction solvent.
A non-crystallizing blend includes cannabidiol (CBD) and cannabidiolic acid (CBDA). A method of forming a non-crystallizing blend of CBD and CBDA includes obtaining a CBD isolate including at least 80% by weight CBD, obtaining a CBDA isolate including at least 80% by weight CBDA, and combining and mixing the CBD isolate and the CBDA. A method of treating a condition includes administering a therapeutically effective amount of a non-crystallizing blend of CBD and CBDA to a patient in need thereof.
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
C07C 39/23 - Composés comportant au moins un groupe hydroxyle ou O-métal lié à un atome de carbone d'un cycle aromatique à six chaînons polycycliques contenant des cycles aromatiques à six chaînons et d'autres cycles avec une insaturation autre que celle des cycles aromatiques
C07C 65/19 - Composés comportant des groupes carboxyle liés à des atomes de carbone de cycles aromatiques à six chaînons et contenant l'un des groupes OH, O-métal, —CHO, cétone, éther, des groupes , des groupes ou des groupes contenant des groupes hydroxyle ou O-métal avec des insaturations autres que celles du cycle aromatique
A non-crystallizing blend includes cannabidiol (CBD) and cannabidiolic acid (CBDA). A method of forming a non-crystallizing blend of CBD and CBDA includes obtaining a CBD isolate including at least 80% by weight CBD, obtaining a CBDA isolate including at least 80% by weight CBDA, and combining and mixing the CBD isolate and the CBDA. A method of treating a condition includes administering a therapeutically effective amount of a non-crystallizing blend of CBD and CBDA to a patient in need thereof.
B65D 73/00 - Paquets comportant des objets fixés à des cartes, des feuilles ou des bandes
C07C 37/50 - Préparation de composés comportant des groupes hydroxyle ou O-métal liés à un atome de carbone d'un cycle aromatique à six chaînons par des réactions diminuant le nombre d'atomes de carbone
C07C 37/70 - SéparationPurificationStabilisationEmploi d'additifs par traitement physique
A non-crystallizing blend includes cannabidiol (CBD) and cannabidiolic acid (CBDA). A method of forming a non-crystallizing blend of CBD and CBDA includes obtaining a CBD isolate including at least 80% by weight CBD, obtaining a CBDA isolate including at least 80% by weight CBDA, and combining and mixing the CBD isolate and the CBDA. A method of treating a condition includes administering a therapeutically effective amount of a non-crystallizing blend of CBD and CBDA to a patient in need thereof.
A01N 43/00 - Biocides, produits repoussant ou attirant les animaux nuisibles, ou régulateurs de croissance des végétaux, contenant des composés hétérocycliques
A01N 43/46 - Biocides, produits repoussant ou attirant les animaux nuisibles, ou régulateurs de croissance des végétaux, contenant des composés hétérocycliques comportant des cycles avec un atome d'azote comme unique hétéro-atome du cycle des cycles à plus de six chaînons
A61K 31/55 - Composés hétérocycliques ayant l'azote comme hétéro-atome d'un cycle, p. ex. guanéthidine ou rifamycines ayant des cycles à sept chaînons, p. ex. azélastine, pentylènetétrazole
A61K 31/192 - Acides carboxyliques, p. ex. acide valproïque ayant des groupes aromatiques, p. ex. sulindac, acides 2-aryl-propioniques, acide éthacrynique
A conduit contactor for conducting chemical reactions or chemical extractions between immiscible liquids includes a conduit having a hollow interior, a first open end, and a second open end opposite the first open end; a separator in fluid communication with and proximate the second open end; and a plurality of fibers disposed within the conduit. A total surface area of the fibers per volume of the hollow interior of the conduit is from 100 cm2/cm3 to 490 cm2/cm3.
An apparatus includes a conduit with two process fluid inlets at one end of the conduit, one process fluid outlet at an opposing end, a heat exchange medium inlet, and a heat exchange medium outlet. One of the fluid inlets includes a tube extending into the conduit and a perforated node at the end of the tube, and the other of the fluid inlets is arranged up stream of the perforated node. The apparatus further includes hollow tubes positioned longitudinally within the conduit between the two process fluid inlets, the process fluid outlet, the heat exchange medium inlet and the heat exchange medium outlet. In addition, the apparatus includes a collection vessel positioned proximate the fluid outlet and fibers extending through each of the hollow tubes, wherein one end of the fibers is secured to the perforated node and the other end of the fibers extends into the collection vessel.
C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
C07C 41/14 - Préparation d'éthers par remplacement des substituants sur l'oxygène de la fonction éther par d'autres substituants, p. ex. par transéthérification
C11C 3/14 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par isomérisation
C07C 67/03 - Préparation d'esters d'acides carboxyliques par réaction d'un groupe ester avec un groupe hydroxyle
B01J 19/24 - Réacteurs fixes sans élément interne mobile
B01J 14/00 - Procédés chimiques généraux faisant réagir des liquides avec des liquidesAppareillage spécialement adapté à cet effet
C08G 59/02 - Polycondensats contenant plusieurs groupes époxyde par molécule
C11C 3/10 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par estérification des graisses ou des huiles par interestérification
C07D 301/28 - Condensation d'épihalohydrines ou d'halohydrines avec des composés contenant des atomes d'hydrogène actif par réaction avec des radicaux hydroxyle
C11C 3/04 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par estérification des graisses ou des huiles
Chromatographic processes are provided which utilize fiber conduit contactors to effect separation of chemical substances from a mixture. In particular, processes are provided which constrain a substance on the fibers and move a mixture of chemical substances and another fluid through the coated fibers to effect separation of a substance from the mixture. In addition, fiber conduit contactors configured to affect such processes are disclosed. Some apparatuses include a sample injection mechanism for selectively inserting an analytical or preparative chromatography mixture into a fluid being supplied to the conduit. Additional or alternative apparatuses include fibers positioned longitudinally within a conduit with their opposing ends respectively bundled into a fluid inlet and a fluid outlet at opposing ends of the conduit. The portions of the fibers between the bundled ends are sufficiently slack such that larger spaces exist between individual fibers along the slack portions than at the bundled ends.
B01D 15/18 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives aux différents types d'écoulement
B01D 15/20 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives au conditionnement de la matière adsorbante ou absorbante
B01D 15/22 - Adsorption sélective, p. ex. chromatographie caractérisée par des caractéristiques de structure ou de fonctionnement relatives à la structure de la colonne
Processes are provided which utilize fiber conduit reactors/contactors to effect extraction from a fluid stream, particularly a fermentation broth, a waste stream of a fermentation process, a fluid comprising a dye, or a fluid comprising a pharmaceutical compound. In particular, methods are provided which include introducing a first stream comprising an extractant and a second stream which is substantially immiscible with the first stream into a conduit reactor proximate a plurality of fibers. The streams are introduced into the conduit reactor such that they are in contact with each other and the extractant of the first stream interacts with the second stream to extract a fermentation product, a fermentation byproduct, a dye or a pharmaceutical compound from the second stream into the first stream. The method further includes receiving the first and second streams in collection vessel/s and withdrawing separately the first and second streams from collection vessel/s.
C02F 1/26 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par extraction
C22B 3/26 - Traitement ou purification de solutions, p. ex. de solutions obtenues par lixiviation par extraction liquide-liquide utilisant des composés organiques
C07C 29/76 - SéparationPurificationStabilisationEmploi d'additifs par traitement physique
C07C 51/47 - SéparationPurificationStabilisationEmploi d'additifs par traitement solide-liquideSéparationPurificationStabilisationEmploi d'additifs par absorption-adsorption chimique
C07C 67/56 - SéparationPurificationStabilisationEmploi d'additifs par traitement solide-liquideSéparationPurificationStabilisationEmploi d'additifs par absorption-adsorption chimique
C07D 207/06 - Composés hétérocycliques contenant des cycles à cinq chaînons, non condensés avec d'autres cycles, ne comportant qu'un atome d'azote comme unique hétéro-atome du cycle avec uniquement des atomes d'hydrogène ou de carbone liés directement à l'atome d'azote du cycle ne comportant pas de liaison double entre chaînons cycliques ou entre chaînons cycliques et chaînons non cycliques avec des radicaux contenant uniquement des atomes d'hydrogène et de carbone, liés aux atomes de carbone du cycle
C02F 103/10 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de carrières ou d'activités minières
C02F 103/24 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant du traitement d'animaux, p. ex. de volaille ou de poissons, ou de parties de ceux-ci provenant de tanneries
C02F 103/30 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de l'industrie textile
C02F 103/32 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de l'industrie alimentaire, p. ex. eaux résiduaires de brasseries
C02F 101/34 - Composés organiques contenant de l'oxygène
C02F 103/34 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de l'industrie chimique non prévue dans les groupes
48.
Fiber conduit apparatus for conducting chemical reactions and chemical extractions
A fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers onto which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process.
B01J 19/24 - Réacteurs fixes sans élément interne mobile
C07D 301/28 - Condensation d'épihalohydrines ou d'halohydrines avec des composés contenant des atomes d'hydrogène actif par réaction avec des radicaux hydroxyle
B01J 14/00 - Procédés chimiques généraux faisant réagir des liquides avec des liquidesAppareillage spécialement adapté à cet effet
C07C 67/03 - Préparation d'esters d'acides carboxyliques par réaction d'un groupe ester avec un groupe hydroxyle
C07C 41/16 - Préparation d'éthers par réactions d'esters d'acides minéraux ou organiques avec des groupes hydroxyle ou O-métal
C08G 59/02 - Polycondensats contenant plusieurs groupes époxyde par molécule
C11C 3/10 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par estérification des graisses ou des huiles par interestérification
C07C 41/14 - Préparation d'éthers par remplacement des substituants sur l'oxygène de la fonction éther par d'autres substituants, p. ex. par transéthérification
C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
C11C 3/04 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par estérification des graisses ou des huiles
An integrated facility for the co-production of ethanol and biodiesel fuel is provided. Ethanol and corn oil, the primary product and a by-product from the ethanol plant, are utilized as feedstocks for a biodiesel plant operating within the same general facility as the corn ethanol plant. By-products of the biodiesel plant, principally crude liquid glycerol and gaseous ethanol or methanol, are recycled to various parts of the ethanol plant.
C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
C12P 7/10 - Éthanol en tant que produit chimique et non en tant que boisson alcoolique préparé comme sous-produit, ou préparé à partir d'un substrat constitué par des déchets ou par des matières cellulosiques d'un substrat constitué par des matières cellulosiques
C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
C07C 67/03 - Préparation d'esters d'acides carboxyliques par réaction d'un groupe ester avec un groupe hydroxyle
C07C 29/80 - SéparationPurificationStabilisationEmploi d'additifs par traitement physique par distillation
C11C 3/00 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse
C12P 7/06 - Éthanol en tant que produit chimique et non en tant que boisson alcoolique
An integrated facility for the co-production of ethanol and biodiesel fuel is provided. Ethanol and corn oil, the primary product and a by-product from the ethanol plant, are utilized as feedstocks for a biodiesel plant operating within the same general facility as the corn ethanol plant. By-products of the biodiesel plant, principally crude liquid glycerol and gaseous ethanol or methanol, are recycled to various parts of the ethanol plant.
ABSTRACT Processes are provided which utilize fiber conduit reactors/contactors to effect extraction of metal element/s, metal compound/s, metalloid element/s, and/or metalloid compound/s from a fluid stream. In particular, methods are provided which include introducing a first stream comprising an extractant and a second stream comprising a metal element, a metal compound, a metalloid element, and/or a metalloid compound into a conduit reactor proximate a plurality of fibers. The second stream is substantially immiscible with the first stream. The streams are introduced into the conduit reactor such that they are in contact and the extractant of the first stream interacts with the second stream to extract the metal element, a metal compound, a metalloid element, and/or a metalloid compound from the second stream into the first stream. The method further includes receiving the first and second streams in collection vessel/s and withdrawing separately the first and second streams from collection vessel/s. Date Recue/Date Received 2021-02-19
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
C02F 1/26 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par extraction
C07C 57/30 - Composés non saturés comportant des groupes carboxyle liés à des atomes de carbone acycliques contenant des cycles aromatiques à six chaînons
C22B 3/24 - Traitement ou purification de solutions, p. ex. de solutions obtenues par lixiviation par des procédés physiques, p. ex. par filtration, par des moyens magnétiques par adsorption sur des substances solides, p. ex. par extraction avec des résines solides
Processes are provided which utilize fiber conduit reactors/contactors to effect extraction of metal element/s, metal compound/s, metalloid element/s, and/or metalloid compound/s from a fluid stream. In particular, methods are provided which include introducing a first stream comprising an extractant and a second stream comprising a metal element, a metal compound, a metalloid element, and/or a metalloid compound into a conduit reactor proximate a plurality of fibers. The second stream is substantially immiscible with the first stream. The streams are introduced into the conduit reactor such that they are in contact and the extractant of the first stream interacts with the second stream to extract the metal element, a metal compound, a metalloid element, and/or a metalloid compound from the second stream into the first stream. The method further includes receiving the first and second streams in collection vessel/s and withdrawing separately the first and second streams from collection vessel/s.
C22B 3/24 - Traitement ou purification de solutions, p. ex. de solutions obtenues par lixiviation par des procédés physiques, p. ex. par filtration, par des moyens magnétiques par adsorption sur des substances solides, p. ex. par extraction avec des résines solides
Processes are provided which utilize fiber conduit reactors/contactors to effect extraction of metal element/s, metal compound/s, metalloid element/s, and/or metalloid compound/s from a fluid stream. In particular, methods are provided which include introducing a first stream comprising an extractant and a second stream comprising a metal element, a metal compound, a metalloid element, and/or a metalloid compound into a conduit reactor proximate a plurality of fibers. The second stream is substantially immiscible with the first stream. The streams are introduced into the conduit reactor such that they are in contact and the extractant of the first stream interacts with the second stream to extract the metal element, a metal compound, a metalloid element, and/or a metalloid compound from the second stream into the first stream. The method further includes receiving the first and second streams in collection vessel/s and withdrawing separately the first and second streams from collection vessel/s.
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
54.
Use of a fiber conduit contactor for metal and/or metalloid extraction
Processes are provided which utilize fiber conduit reactors/contactors to effect extraction of metal element/s, metal compound/s, metalloid element/s, and/or metalloid compound/s from a fluid stream. In particular, methods are provided which include introducing a first stream comprising an extractant and a second stream comprising a metal element, a metal compound, a metalloid element, and/or a metalloid compound into a conduit reactor proximate a plurality of fibers. The second stream is substantially immiscible with the first stream. The streams are introduced into the conduit reactor such that they are in contact and the extractant of the first stream interacts with the second stream to extract the metal element, a metal compound, a metalloid element, and/or a metalloid compound from the second stream into the first stream. The method further includes receiving the first and second streams in collection vessel/s and withdrawing separately the first and second streams from collection vessel/s.
C02F 1/26 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par extraction
C22B 3/26 - Traitement ou purification de solutions, p. ex. de solutions obtenues par lixiviation par extraction liquide-liquide utilisant des composés organiques
C02F 103/10 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de carrières ou d'activités minières
C02F 103/24 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant du traitement d'animaux, p. ex. de volaille ou de poissons, ou de parties de ceux-ci provenant de tanneries
C02F 103/30 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de l'industrie textile
C02F 103/32 - Nature de l'eau, des eaux résiduaires ou des eaux ou boues d'égout à traiter provenant de l'industrie alimentaire, p. ex. eaux résiduaires de brasseries
55.
METHOD AND SYSTEM FOR USING A FIBER CONDUIT REACTOR
A fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers onto which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process.
A fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers onto which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process.
B01J 19/24 - Réacteurs fixes sans élément interne mobile
C11C 3/04 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par estérification des graisses ou des huiles
C07C 41/14 - Préparation d'éthers par remplacement des substituants sur l'oxygène de la fonction éther par d'autres substituants, p. ex. par transéthérification
C07D 301/28 - Condensation d'épihalohydrines ou d'halohydrines avec des composés contenant des atomes d'hydrogène actif par réaction avec des radicaux hydroxyle
B01J 14/00 - Procédés chimiques généraux faisant réagir des liquides avec des liquidesAppareillage spécialement adapté à cet effet
C07C 67/03 - Préparation d'esters d'acides carboxyliques par réaction d'un groupe ester avec un groupe hydroxyle
C07C 41/16 - Préparation d'éthers par réactions d'esters d'acides minéraux ou organiques avec des groupes hydroxyle ou O-métal
C08G 59/02 - Polycondensats contenant plusieurs groupes époxyde par molécule
C11C 3/10 - Graisses, huiles ou acides gras obtenus par transformation chimique des graisses, huiles ou acides gras, p. ex. ozonolyse par estérification des graisses ou des huiles par interestérification
57.
Method and system for production of biofuels using a fiber conduit reactor
A fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers onto which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process.
A fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers into which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process.
B01J 8/06 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes dans des réacteurs tubulairesProcédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes les particules solides étant disposées dans des tubes
B01J 19/18 - Réacteurs fixes avec éléments internes mobiles
C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
C11D 3/04 - Composés inorganiques solubles dans l'eau
59.
USE OF FIBER FILM REACTORS TO EFFECT SEPARATION AND REACTION BETWEEN TWO IMMISCIBLE REACTION COMPONENTS
The present invention provides a fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers into which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process. The invention also provides for an apparatus comprising a conduit, a plurality of functionalized polymer fibers positioned within the conduit and a collection vessel.
The present invention provides a fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers into which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process. The invention also provides for an apparatus comprising a conduit, a plurality of functionalized polymer fibers positioned within the conduit and a collection vessel.
B01J 8/06 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes dans des réacteurs tubulairesProcédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes les particules solides étant disposées dans des tubes
B01J 19/18 - Réacteurs fixes avec éléments internes mobiles
C11B 3/02 - Raffinage des graisses ou huiles par réaction chimique
61.
Fiber film reactors to effect separation and reaction between two immiscible reaction components
A fiber reaction process whereby reactive components contained in immiscible streams are brought into contact to effect chemical reactions and separations. The conduit reactor utilized contains wettable fibers onto which one stream is substantially constrained and a second stream is flowed over to continuously create a new interface there between to efficiently bring about contact of the reactive species and thus promote reactions thereof or extractions thereby. Co-solvents and phase transfer catalysts may be employed to facilitate the process.
C07C 7/148 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par traitement provoquant une modification chimique d'au moins un composé
brevets
