Abstract: Disclosed is a continuous process for the purification of steviol glycosides extracted from the dried stevia leaves using continuous simulated moving bed processes and nanofiltration without the addition of organic solvents to obtain a purified steviol product comprising sweet steviol glycosides. The sweet steviol glycosides can be used as substitutes for caloric sweeteners in beverages and in other food items.

Abstract: Disclosed is a method for purification and separation of cannabinoids, specifically cannabidiol and tetrahydrocannabinol, from the dried hemp and cannabis leaves using a combination of a sequence of purification steps including: filtration, decolorization, activation or decarboxylation, dewaxing, a continuous simulated moving bed process, polishing, and crystallization to separate cannabinoids from tetrahydrocannabinol and to provide phytocannabinoid rich oil and cannabidiol isolate. The cannabinoid products can be used in various pharmaceutical and nutraceutical applications.

Abstract: A method for purification and separation of cannabinoids, such as cannabidiol and tetrahydrocannabinol, e.g., from dried hemp and cannabis leaves can use a continuous simulated moving bed process, a batch column chromatography method, or a single column, and a combination of one or more of a sequence of purification steps including: filtration, decolorization, activation or decarboxylation, dewaxing, polishing, and crystallization to separate a cannabinoid from the cannabis plant and to provide various cannabinoid products. The cannabinoid products can be used in various pharmaceutical and nutraceutical applications.

Abstract: A method for purification and separation of cannabinoids, such as cannabidiol and tetrahydrocannabinol, e.g., from the dried hemp and cannabis leaves can use a continuous simulated moving bed process and a combination of one or more of a sequence of purification steps including: filtration, decolorization, activation or decarboxylation, dewaxing, polishing, and crystallization to separate a cannabinoid from the cannabis plant and to provide various cannabinoid products. The cannabinoid products can be used in various pharmaceutical and nutraceutical applications.

Abstract: Disclosed is a chromatographic process complex for the refining of krill oil extract including desalting, removal of impurities such as trimethylamine oxide (TMAO), and the production of krill oil products including desalted krill oil extract, polar lipid products having polar lipid contents greater than 50 wt-% on a dry or solvent free basis, neutral lipid streams for biodiesel production and astaxanthin. The refinery includes a continuous desalting zone, a fixed bed polar lipid extraction zone to adsorb neutral lipids and astaxanthin to provide a polar lipid extract stream comprising solvent and polar lipids and being essentially free of neutral lipids and astaxanthin, and an astaxanthin separation zone to recover essentially pure astaxanthin and provide a neutral lipid stream. The enriched products of the krill oil refinery are essentially free of TMAO and salt and provide products which can be used as dietary supplements and as medicinal additives.

Abstract: Disclosed is a chromatographic process complex for the refining of krill oil extract including desalting, removal of impurities such as trimethylamine oxide (TMAO), and the production of krill oil products including desalted krill oil extract, polar lipid products having polar lipid contents greater than 50 wt-% on a dry or solvent free basis, neutral lipid streams for biodiesel production and astaxanthin. The refinery includes a continuous desalting zone, a fixed bed polar lipid extraction zone to adsorb neutral lipids and astaxanthin to provide a polar lipid extract stream comprising solvent and polar lipids and being essentially free of neutral lipids and astaxanthin, and an astaxanthin separation zone to recover essentially pure astaxanthin and provide a neutral lipid stream. The enriched products of the krill oil refinery are essentially free of TMAO and salt and provide products which can be used as dietary supplements and as medicinal additives.

Abstract: Disclosed is a chromatographic process complex for the refining of krill oil extract including desalting, removal of impurities such as trimethylamine oxide (TMAO), and the production of krill oil products including desalted krill oil extract, polar lipid products having polar lipid contents greater than 50 wt-% on a dry or solvent free basis, neutral lipid streams for biodiesel production and astaxanthin. The refinery includes a continuous desalting zone, a fixed bed polar lipid extraction zone to adsorb neutral lipids and astaxanthin to provide a polar lipid extract stream comprising solvent and polar lipids and being essentially free of neutral lipids and astaxanthin, and an astaxanthin separation zone to recover essentially pure astaxanthin and provide a neutral lipid stream. The enriched products of the krill oil refinery are essentially free of TMAO and salt and provide products which can be used as dietary supplements and as medicinal additives.

Abstract: Disclosed is a process for the direct extraction of an omega-3 fatty acid enriched triglyceride product comprising unsaturated triglycerides with a fatty acid strand of docosahexaenoic acid (DHA) or eicosapentaenoic acid (EPA) from a crude fish oil comprising unsaturated triglycerides and saturated triglycerides having strands comprising fatty acids of at least one stearic acid, palmitic and oleic acid. Each triglyceride in the crude fish oil can be characterized by a Partition Number (PN) according to the formula: PN=TC?2DB wherein TC is a total number of carbon atoms in the fatty acid strand, and DB is the number of double bonds in the fatty acid strand. Crude fish oil diluted in non-polar solvent directly passed to an SMB zone, comprising a normal phase separation with a hydrophilic stationary phase agent and a non-polar/organic polar mobile phase desorbent to provide an omega-3 fatty acid enriched triglyceride product.

Abstract: A flash chromatography apparatus which provides an improved apparatus for large and medium commercial scale flash chromatography columns. More particularly, the invention relates to a flash chromatography column and cartridge system for positioning and ease of loading and unloading of stationary phase agent in the flash chromatography column. The flash chromatography column further provides flow distributors to support the stationary phase and permit plug flow through the column. The apparatus of the present invention is a modular and can be disposed in any configuration to reduce maintenance cost and downtime in a commercial installation. Flash chromatography is widely used for purification of low molecular weight organic compounds and products of organic synthetic reactions.

Abstract: This invention relates to a method and apparatus or kit for extracting major metabolites of vitamin D from human plasma or serum. More particularly, the invention provides for the extraction from human plasma or serum samples comprising vitamin D metabolites such as 1,25-dihydroxy vitamin D3, 25-hydroxy vitamin D2, and D3 from protein binding, removal of protein and phospholipids, and isolation of the metabolites using a combination of ion-exchange and Lewis acid mechanisms without the requirement to acidify the samples. The method and apparatus of the invention comprise a cartridge or plurality of cartridges comprising at least one protein crash frit, a strong cation exchanged sorbent, and an acidified alumina sorbent to provide higher recoveries of vitamin D metabolites than existing phospholipid depletion plate techniques.

Abstract: Disclosed is a process for extracting and purifying EPA (Eicosapentanoic acid) ethyl ester from a crude fish oil feedstock using a combination of novel esterification and simulated moving bed (SMB) techniques. Crude fish oil diluted in non-polar solvent is esterified with an acid and then transesterified with a base. Following washing, the non-polar phase is directly passed to an SMB zone, comprising a normal phase separation with a hydrophilic stationary phase agent and a non-polar/organic polar mobile phase desorbent to provide an enhanced omega-3 product, comprising EPA. In a further embodiment, the enhanced omega-3 product is passed to a second and third SMB zones operating in reverse phase using a hydrophobic stationary phase and a polar mobile phase desorbent. The process is useful for producing high purity EPA at purities in excess of 97 wt-% which are not economically recoverable by conventional distillation methods combined with conventional SMB configurations.

Abstract: This invention relates to a kit and a method for the collection and analysis of complex protein mixtures. More particularly, the invention relates to a kit comprising a single barrel filtration well or a multi-well filtration plate wherein each well comprises an upper filtration zone; a lower filtration zone; a conical flow director zone; and, an elution tip, wherein the upper filtration zone and the lower filtration zone are separated by a retainer ring disposed within the lower filtration zone. The upper filtration zone comprises an upper collection zone, a sponge zone, and a deep bed filtration zone; and, the lower filtration zone comprises the retainer ring, a supported hydrophilic membrane and a lower bed filtration media. When used with an array of selected buffer solutions, the multi-well filtration plate can provide accurate, automated, high-throughput protein analysis by affinity chromatography.

Abstract: A flash chromatography apparatus which provides an improved apparatus for large and medium commercial scale flash chromatography columns. More particularly, the invention relates to a flash chromatography column and cartridge system for positioning and ease of loading and unloading of stationary phase agent in the flash chromatography column. The flash chromatography column further provides flow distributors to support the stationary phase and permit plug flow through the column. The apparatus of the present is modular and can be disposed in any configuration to reduce maintenance cost and downtime in a commercial installation. Flash chromatography is widely used for purification of low molecular weight organic compounds and products of organic synthetic reactions.

Abstract: Disclosed is a process for the production of high purity alpha-tocotrienol from palm oil extract. More particularly, the invention relates to a process for the separation of alpha-tocotrienol from a mixtures of other tocotrienols and tocopherols and the use of a simplified separation scheme based on a combination of solid phase extraction and simulated moving bed (SMB) separation steps employing polar phase simulated moving bed operation. The process is useful for providing a continuous route and a simplified processing route to providing pure alpha-tocotrienol as a major product essentially free of other tocotrienols and tocopherols including: beta-tocopherol, gamma-tocotrienol, delta-tocotrienol, gamma-tocopherol, delta-tocopherol, front end and back end carotenoids, and alpha-tocopherol as a by-product from palm oil extract. Alpha-tocotrienol is a form of vitamin E and may be useful as a treatment for preventing stroke or reducing brain and nerve damage following a stroke.

Abstract: Disclosed is a process for the production of d-tagatose from lactose after acid hydrolysis to provide a hydrolysate having 1 equiv of d-glucose and 1 equiv of d-galactose for each unit of lactose converted. More particularly, the invention relates to a process for the isomerization of d-galactose to d-tagatose and the use of a simplified separation scheme based on simulated moving bed (SMB) separation. The isomerization of d-galactose to d-tagatose is carried out in the presence of calcium oxide or calcium hydroxide. The process is useful for providing a simplified processing route to providing pure d-tagatose and glucose as two products from lactose hydrolysate. In an alternate embodiment, a process is disclosed for the production of d-tagatose from fermented lactose hydrolysate to provide a crystallized d-tagatose product. D-tagatose is useful as a food additive, as a sweetener, as a texturizer, as a stabilizer, or as a humectant.

Abstract: Disclosed is an improved SMB process incorporating novel regeneration steps for the separation of ethanol associated oxygenates such as butanediol from a dilute mixture of ethanol and associated oxygenates in water in the presence of organic compounds derived from a biofermentation process. Applicant discovered that increasing the number of raffinate streams alone or in combination with a hot regeneration zone within the SMB cycle can significantly reduce the capital and operating costs associated with the incorporation of the SMB process in a complex for the production of ethanol and butanediol from biofermentation effluent. The process is useful for removing water from dilute aqueous mixtures of organic compounds comprising ethanol in dilute concentration in water and produced by fermentation, biomass extraction, biocatalytic and enzymatic processes which are not economically recoverable by conventional distillation methods.

Abstract: Disclosed is a process and an adsorbent for the separation of ethanol associated oxygenates from a dilute mixture of ethanol and associated oxygenates in water in the presence of organic compounds derived from a biofermentation process. After pretreatment, the separation is carried out in a simulated moving bed adsorption system employing an stationary phase adsorbent comprising fluorinated carbon or modified C18 silica gel selective for the adsorption of ethanol and associated oxygenates, such as 2,3-butanediol, with a mobile phase desorbent selected from the group consisting of methanol, ethanol, propanol, and methyl tertiary butyl ether. The process is useful for removing water from dilute aqueous mixtures of organic compounds comprising ethanol in dilute concentration in water and produced by fermentation, biomass extraction, biocatalytic and enzymatic processes which are not economically recoverable by conventional distillation methods.

Abstract: A process is disclosed for producing organic nitriles such as Acetonitrile or Hydrogen Cyanide, in which yields may exceed 90%, undesirable by-products are not produced, and handling of ammonia gas is avoided. In one aspect, a process includes preparing a feed including ammonium salts and water; introducing the feed into a reactor containing a catalyst; and heating the feed in the presence of the catalyst. The catalyst may advantageously include molybdenum on a silica or silica alumina support. The feed may be ammonium acetate in water with about 50 wt % ammonium acetate and the balance water or ammonium formate in water. In another aspect, a process includes preparing a feed including ammonium hydroxide and acetic acid; introducing the feed into a reactor containing a catalyst; and heating the feed in the presence of the catalyst.

Abstract: This invention concerns generally with a process for purifying crude pharmaceutical compositions, wherein the crude pharmaceutical composition comprises a sodium salt of Montelukast and more particularly relates to a process for the production of pharmaceutically pure preparations of Montelukast sodium using simulated moving bed technology, without requiring an intermediate acid formation step to separate isomers and to remove impurities.

Abstract: This invention relates to a kit and a method for the collection and analysis of complex protein mixtures. More particularly, the invention relates to a kit comprising a single barrel filtration well or a multi-well filtration plate wherein each well comprises an upper filtration zone; a lower filtration zone; a conical flow director zone; and, an elution tip, wherein the upper filtration zone and the lower filtration zone are separated by a retainer ring disposed within the lower filtration zone. The upper filtration zone comprises an upper collection zone, a sponge zone, and a deep bed filtration zone; and, the lower filtration zone comprises the retainer ring, a supported hydrophilic membrane and a lower bed filtration media. When used with an array of selected buffer solutions, the multi-well filtration plate can provide accurate, automated, high-throughput protein analysis by affinity chromatography.