Abstract: Shown is a method of making a coffee concentrate, and a coffee concentrate obtainable by the method. The method involves primary and secondary extraction, with split tapping of the primary extract into a first and second primary draw off. The extraction is conducted under such conditions as to satisfy a minimum mass transfer Fourier number, and a minimum ratio of the extraction yield of the first primary draw-off to the extraction yield obtained in all extraction sections.

Abstract: Shown is a method of making a coffee concentrate, and a coffee concentrate obtainable by the method. The method involves primary and secondary extraction, with split tapping of the primary extract into a first and second primary draw off. The extraction is conducted under such conditions as to satisfy a minimum mass transfer Fourier number, and a minimum ratio of the extraction yield of the first primary draw-off to the extraction yield obtained in all extraction sections.

Abstract: In an embodiment of the described technology, a multi-chamber cup is used to brew coffee or other (hot) drink in a brewing machine. Such a device allows one to add any coffee, but use all the features of an automated single-cup or multi-cup brewing machine. The multi-chamber cup has an inner cup, an intermediate cup, and an outer cup each having sides with circular cross-sections between a top side and bottom side, defining an inner cavity there-between, each with a lip at a top side of the respective cup, extending outwards from a respective inner cavity of each cup. This allows water to enter and flow through multiple cups (at least three) before exiting the multi-chamber cup, such that the liquid becomes homogenized with dissolved particulate solid matter to produce a flavorful, high-quality drink.

Abstract: The invention relates to a process for improving the flavor of roasted Robusta and Arabica quality coffee and is characterized by modifying roasted coffee flavor precursors in aqueous extracts of green coffee beans.

Abstract: Provided is a packaged Oolong-tea beverage which contains an Oolong tea extract having a tannin/Brix ratio of from 200 to 265 (mg/100 mL/wt. %) and has a non-polymer catechin content of from 0.06 to 0.5 wt. %. The packaged Oolong-tea beverage of the present invention contains a high concentration of catechins and at the same time, tastes good without losing the original taste of Oolong tea.

Abstract: An apparatus for preparing a coffee beverage inducing the passage of an extraction fluid through a dose of coffee by heating said fluid, contains a separating device arranged to separate a fraction of said beverage obtained with a prevalently liquid phase of said fluid from a further fraction of said beverage obtained with a prevalently steam phase of said fluid; an apparatus for preparing a coffee beverage by imbibing a dose of coffee with an extraction fluid driven by heating through said dose, comprises an inhibition device arranged to inhibit said imbibing when said fluid contains a substantial steam phase; a method for obtaining a coffee beverage involves heating an extraction fluid so as to induce the passage of said extraction fluid through a dose of coffee to obtain said beverage and separating a fraction of said beverage obtained with a prevalently liquid phase of said extraction fluid from a further fraction of said beverage obtained with a prevalently steam phase of said extraction fluid is provide

Abstract: A processing system and methods for extracting phytochemicals from plant materials with subcritical water. The processing system includes a water supply interconnected with a high-pressure pump, diverter valve, a temperature-controllable extraction vessel, a cooler, a pressure-relief valve and a collection apparatus for collecting eluant fractions from the extraction vessel. The processing system controllably varies the temperature of subcritical water within the extraction vessel, and may optionally be configured to controllably vary the pH of subcritical water flowing into the extraction vessel. A plant material is placed into the extraction vessel after which a flow of subcritical water is provided through the extraction vessel for extraction of phytochemicals.

Abstract: A system that allows for hot water on demand and once the water is heated, it is delivered to flavor containing solid material in a pressurized pulse. By heating the water on demand, a more uniform temperature can be achieved and by delivering the heated water in a pressurized pulse, the extraction of flavor from the flavor containing solid material is greatly improved. In addition, to determine the volume of water used in the system, the number of pressurized pulses are counted and that gives a more uniform consistent measurement of the volume of water used instead of the timed delivery of water.

Abstract: The invention refers to a moka coffee machine, basically traditional, modified in order to obtain an expresso coffee without altering the organoleptic properties thereof. The machine according to the invention allows to control the temperature of the water inside the boiler, and to prepare the drink without having the water reaching exceedingly high pressures.

Abstract: A method is provided for producing a soluble coffee extract which, when reconstituted, produces an intensified in-cup brew color without altering the flavor of the cup of coffee. The method includes heating a coffee extract at a temperature and for a time selected to produce an intensified color coffee extract without altering the flavor of the coffee. The intensified color coffee is either immediately dried to form dried intensified color coffee or cooled while in the liquid state. The soluble coffee produced by this method has intensified color while its flavor remains unaltered. As desired, the soluble coffee may be packaged as an instant coffee, combined with traditional soluble coffee, incorporated into a liquid coffee product or combined with sugar, creamer, and flavors to form various soluble coffee products. Alternatively, the coffee exact may be directly incorporated into a ready-to-drink or a concentrated liquid coffee product without undergoing a drying step.

Abstract: Green coffee is introduced into a container where it is subjected to continuous mixing in temperature continuous mixing in temperature ranging between environment and values close to 120° C. and water vapor is introduced into said container until the single beans of coffee have become porous and permeable; micotoxins are removed by extraction with a solvent in an acid environment obtained with a given acid or with a buffer solution with a given acid pH.

Abstract: An aroma product resulting from the recovery of aroma components from coffee. A slurry of coffee grounds in an aqueous liquid is subjected to stripping for stripping aroma components from the slurry. The stripping is carried out using gas in a substantially counter-current manner to provide an aromatized gas containing aroma components. The aroma components are then collected from the aromatized gas. The aroma components may be added to concentrated coffee extract prior to drying of the extract. The coffee powder produced has much increased and improved aroma and flavor and contains higher levels of furans and diketones.

Abstract: A process for preparing a flavonoid extract from the leaves of ginkgo biloba comprising multiple distractions of the leaves of the ginkgo biloba with solvents wherein at least one of the extraction stages is a deterpenation step using a solvent of the formula RC(O)OR′ wherein R and R′ are individually lower alkyl.

Abstract: A method of intensifying the flavor of coffee extract is disclosed in which coffee extract is heated at a temperature and for a time sufficient to intensify the flavor of the coffee. The heated coffee extract is cooled and preferably dried to produce a soluble coffee product having intensified flavor. The flavor intensity of soluble coffee can be increased without deleteriously altering coffee flavor.

Abstract: A process for providing an isoflavone rich protein isolate is provided, along with the isoflavone rich protein isolate produced thereby. A vegetable material containing protein and at least one isoflavone compound is extracted with an aqueous extractant having a pH above the isoelectric point of the protein, and preferably an alkaline pH. The protein and isoflavones are extracted into the extractant, and the extractant containing the protein and isoflavones is separated from insoluble vegetable protein materials to form a protein extract. The pH of the protein extract is adjusted to about the isoelectric point of the protein to precipitate the protein. The extract containing the precipitated protein is cooled to a temperature of about 40.degree. F. to about 80.degree. F., and then the protein is separated from the extract. Washing of the separated protein is avoided, or, is conducted with minimum amounts of water.

Abstract: A process for the continuous extraction of water soluble solids from solid particles containing them for providing an extract product in one or more extraction stages. In each extraction stage, a slurry containing particles to be extracted and extract is introduced into an extraction reactor to form an upwardly moving packed bed. Particles are scraped from the packed bed for defining an upper surface of the packed bed. An extraction liquid is introduced into the extraction reactor above the upper surface of the packed bed. A portion of the extraction liquid percolating through the packed bed for extracting water soluble substances from the particles in the packed bed and forming an extract. The remaining portion of the extraction liquid entrains the particles scraped from the packed bed for providing a spent particles slurry. The spent particles slurry is removed from the extraction reactor. Extract is removed from below the packed bed and at least a portion of the extract forms the extract product.

Abstract: A process for providing an isoflavone rich protein isolate is provided, along with the isoflavone rich protein isolate produced thereby. A vegetable material containing protein and at least one isoflavone compound is extracted with an aqueous extractant having a neutral pH. The protein and isoflavones are extracted into the extractant, and the extractant containing the protein and isoflavones is separated from insoluble vegetable materials to form a protein extract. The pH of the protein extract is adjusted to about the isoelectric point of the protein to precipitate the protein. The extract containing the precipitated protein is cooled to a temperature of from about 40.degree. F. to about 80.degree. F., and then the protein is separated from the extract. The cool separation temperatures unexpectedly significantly increase the concentration of isoflavones recovered in the separated protein, while the neutral extract pH inhibits loss of protein normally observed at cool or cold separation temperatures.

Abstract: A process for the counter-current extraction of soluble coffee solids. Soluble coffee solids are extracted from roast and ground coffee in a first extraction stage using a primary extraction liquid at a temperature of 80.degree. C. to 160.degree. C. Then soluble coffee solids are extracted from the partially extracted grounds in a second extraction stage using a secondary extraction liquid at a temperature of 160.degree. C. to 190.degree. C., the coffee grounds having at least 25% by weight of soluble coffee solids extracted from them. The coffee grounds obtained from the second extraction stage are drained and thermally hydrolyzed in a hydrolysis stage at a temperature of 160.degree. C. to 220.degree. C. for 1 to 15 minutes. Soluble coffee solids are extracted from the hydrolyzed coffee grounds in a third extraction stage using a tertiary extraction liquid at a temperature of 170.degree. C. to 195.degree. C. to provide extracted coffee grounds and a hydrolyzed coffee extract.

Abstract: A process for extracting roasted and ground coffee in an extractor is presented. In this process, the coffee is wetted by a mixture of water at a temperature between 20.degree. and 100.degree. C. to obtain a water content 20-50% by weight. Then the wetted coffee is transferred to an oblong abstractor to essentially fill the extractor. After the coffee has been transferred, gasses and water vapor are evacuated from the extractor to obtain the pressure of between 600 millibar and a value corresponding to the vapor pressure of water at the temperature at which the wetted coffee obtained as a result of the initial pre-wetting process. While maintaining the extractor at this pressure, and without any further evacuation of gasses and water vapor, a hot aqueous extraction liquid is introduced at one end of the evacuated extractor to fill it. The extractor is maintained at temperatures above 100.degree. C. during this process.

Abstract: Supercritical solvent-treated cocoa powder is used as a flavoring to provide hypoallergenic chocolate-flavored beverages and confections. The dairy permeate is the product of ultrafiltration of milk or whey, which removes protein allergens. The mouth feel as well as the rheological properties of chocolate are retained with a fat content as low as 25% or less.

Abstract: An antioxidant composition and a process of recovering the same from a gelatinous retentate of spent ground coffee oil, comprising from 20 to 60% wt of complex lipids and from 10 to 75% wt of carboxylic acids 5-hydroxytryptamides, in which the 5-HT are for example those of behenic, arachidic and/or lignoceric acids, and the complex lipids are phospholipids and glycolipids. This composition may be advantageously used in food products.

Abstract: Roast and ground coffee is extracted by a split extraction process to obtain an extract from an atmospheric stage and an extract from a pressure stage. The extract produced by the atmospheric stage is evaporatively concentrated to a dry matter content of above 35% by weight, and the evaporation vapors produced during evaporative concentration are condensed and concentrated. The extract produced by the pressure stage also is evaporatively concentrated to increase its dry matter concentration to a dry matter concentration below 25% by weight. The two concentrated extracts then are mixed, and that mixture is evaporatively concentrated to a dry matter concentration of more than 40% by weight. The condensed and concentrated vapors obtained from evaporative concentration of the atmospheric stage are introduced into the evaporatively concentrated mixture or into a powder obtained from the concentrated mixture.

Abstract: Coffee oil is separated from a filtered extract produced by counter-current extraction and the separated oil is incorporated into soluble coffee powder.

Abstract: The invention relates to a process for preparing soluble coffee with an infusion quality similar to that of roast bean coffee, with which instant-typical off-flavour characters are no longer detectable, with which ground roast coffee of a particle size of at most approximately 1.

Abstract: To reduce insoluble solids contained in a coffee extract obtained from a countercurrent extraction process, the percolation rate of extraction liquid passing through at least one extraction cell, which is positioned intermediately in the countercurrent cell series between extraction cells containing the least extracted coffee material and the most extracted coffee material, is reduced. The flow of extraction liquid may be increased through an extraction cell in the series downstream from the at least one cell in which the percolation rate is reduced.

Abstract: Two flash evaporation steps are incorporated into a countercurrent extraction process employed to extract coffee. One flash evaporation step is performed upon a first extract obtained from an extraction cell having a temperature of above 150.degree. C., the flash evaporation being performed at a temperature reduced from 150.degree. C. The second flash evaporation step is performed upon a second extract obtained from an extraction cell positioned at least one cell downstream in the series from the cell from which the first extract was obtained, the second flash evaporation being carried out at a temperature higher than the temperature of the first flash evaporation and the product thereof being introduced to a further downstream extraction cell.

Abstract: Extraction yield of coffee extracted in a countercurrent extraction system is increased by separating sludge by centrifugation from coffee extract obtained from the system and introducing the sludge into at least one extraction cell of the system so that the sludge may be hydrolyzed during the extraction of the coffee.

Abstract: A pharmaceutical composition is described which comprises a pharmaceutically acceptable carrier and a compound of the formula (1): ##STR1## or a pharmaceutically acceptable salt thereof wherein X is CH.sub.2 or S, in an amount sufficient to stimulate selectively histamine H.sub.3 -receptors.

Abstract: A method of extracting roasted and ground coffee is disclosed. Exraction water is fed to one end of an extraction vessel containing roasted and ground coffee, and coffee extract is with drawn from the other end. Flow of water to and from the vessel is intermittently halted, and extracted roasted and ground coffee is intermittently discharged from the vessel, while a portion of unextracted coffee is charged to the vessel at the other end. The movement of coffee in the extraction vessel is countercurrent relative to the flow of the extraction water. The method of the present invention is less complex, is more easily controlled, requires a lower capital investment and produces a more aromatic coffee extract of better flavor balance.

Abstract: A method for producing a coffee extract which comprises: (1) contacting an aqueous mixture of ground roast coffee with steam under pressure at elevated temperatures followed by rapid decompression at atmospheric levels; and (2) treatment of the resulting mixture with a hydrolytic enzyme or with a mixture of hydrolytic enzymes. The coffee extract thus obtained is a concentrated liquid which can be made into a beverage by the addition of water or it may be dried to a soluble solid and reconstituted with water to provide instant coffee.

Abstract: A method of extracting caffeine from green coffee beans whereby an essentially caffeine-free supercritical fluid is continuously fed to one end of an extraction vessel containing green coffee beans and caffeine-laden supercritical fluid is continuously withdrawn from the opposite end. A portion of decaffeinated beans is periodically discharged while a fresh portion of undecaffeinated beans is essentially simultaneously charged to the extraction vessel. The caffeine-laden supercritical fluid is fed to a countercurrent water absorber. Supercritical carbon dioxide is the preferred supercritical fluid. The method of the present invention is more efficient than batch processes and produces an improved decaffeinated coffee.

Abstract: This invention relates to an improved process for steaming and later extracting roasted and ground coffee and the product of such process. The process comprises vacuum steaming roasted and ground coffee in a percolator at a temperature less than 200.degree. F. at a pressure of from 10" to 27"(Hg) and recovering the steam aroma produced by passing same through a wedge-wire draw-off apparatus, the draw-off apparatus comprising a helically wound wire assemblage being internal to the percolator. Thereafter the coffee is percolated to extract solids therefrom and the extract and aroma are combined and dehydrated to form a soluble coffee product.

Abstract: Process for extracting roasted and ground coffee characterized in that the coffee, having an average particle size not exceeding 2.0 mm, is wetted in the absence of air with at least twice its weight of an aqueous liquid, and the wetted coffee is transferred, in the absence of air, to an extractor where it is extracted with an aqueous liquid at a temperature of at least 100.degree. C.

Abstract: Coffee extracts are processed in a continuous countercurrent process of split extraction to obtain (1) atmospheric solids, (2) a push-out of low concentration, mainly atmospheric solids and (3) autoclave solids. Each stream can be further processed separately before recombining to achieve desired flavor characteristics.

Abstract: A process for collecting volatile aromatics which are entrained with gases evolved during the wetting and extraction of fresh roasted and ground coffee beans and contained in part within the extract itself, and thereafter combining the collected volatile aromatics with processed coffee extract and/or soluble coffee to produce an instant coffee product having improved flavor and aroma is disclosed. The instant coffee product obtained by this process is also disclosed.

Abstract: A process for the continuous extraction of roasted coffee or tea, which comprises introducing dry finely ground coffee or tea at a charging station in the form of a bed with a thickness of from 0.5 to 15 cm and displacing the bed along a closed circuit up to a discharging station by way of at least one extraction station where a stream of extraction liquid is passed through the bed while a pressure gradient of the liquid on the bed is maintained.

Abstract: A method of hydrolyzing a coffee extraction residue material to produce a mannan oligomer solution having oligomers from DP 1 to DP 10 is disclosed. The coffee material, preferably spent grounds from a commercial percolation system, is hydrolyzed in a reactor in the presence of an acid catalyst. A tubular plug flow reactor is convenient, although any reactor providing for the relatively high temperature, short time reaction will suffice. Particular acid catalysts include sulphuric acid, phosphoric acid, acetic acid and carbon dioxide gas. Depending on the specific time, temperature and catalyst concentration selected, a mannan oligomer solution having any desired distribution of oligomers between DP 1 and DP 10 is produced.

Abstract: A process for collecting volatile aromatics which are entrained with gases evolved during the wetting and extraction of fresh roasted and ground coffee beans and contained in part within the extract itself, and thereafter combining the collected volatile aromatics with processed coffee extract and/or soluble coffee to produce an instant coffee product having improved flavor and aroma is disclosed. The instant coffee product obtained by this process is also disclosed.

Abstract: A process for forming a vegetable extract in a system comprising a series of cells containing coffee and coffee substitute, by contacting progressively fresher vegetable materials countercurrently with an extraction liquid which enters an inlet cell and is withdrawn in batches from an outlet cell characterized in that the outlet cell and each succeeding alternate cell contains more coffee than any one of their respective adjacent cells and during or after each draw-off the pair of cells containing the most exhausted vegetable material is disconnected from the system for discharge and reloading, and after each draw-off a pair of cells with fresh loads of coffee and coffee substitute is added to the system so that the outlet cell is the second in series and contains the majority of coffee of the pair, the amount of soluble solids in each draw-off being approximately twice the amount drawn off in a standard process.

Abstract: Process and apparatus for the preparation of extracts from ground roasted coffee and the like comprising subjecting ground roasted coffee sequentially to (a) exhaustive extraction of the solubles at a temperature at which no substantial hydrolysis of coffee solids occurs, (b) heating for a short time to a temperature at which insoluble coffee solids are transformed into extractable substances, and (c) exhaustive leaching at a temperature within the same range as that used for step (a).

Abstract: A high quality coffee extract is prepared using a commercial percolation system utilizing a superficial velocity of aqueous extraction liquid past the roasted and ground coffee of at least about 0.50 ft/min in the fresh stage extraction column of a percolator set.

Abstract: An improvement to conventional processes for countercurrent extraction of roast ground coffee is disclosed. Therein, fresh roast ground coffee is contacted with previously produced aqueous coffee brew, and then the resultant admixture is added to the extraction zone.

Abstract: A novel process for extracting roasted coffee using split-extraction percolation techniques is disclosed comprising obtaining an autoclave coffee extract by passing aqueous extraction liquid through the autoclave section of the percolator set, splitting the autoclave extract into a product portion and a feed portion, obtaining an atmospheric coffee extract product from the atmospheric section of the percolator set by passing the feed portion of the autoclave coffee extract through the atmospheric section, and further processing the atmospheric coffee extract product and the product portion of the autoclave extract to obtain a dry instant coffee product.