Abstract: An edible confectionery ink composition for 3D printing comprises: from 20% to 75% by weight of sweetener, preferably sugar, and from 15% to 50% by weight of a fat composition, wherein the fat composition comprises from 0% to 3% by weight of lauric acid (C12:0); and from 35% to 70% by weight of saturated fatty acid (SAFA); said percentages of acid referring to acids bound as acyl groups in glycerides in the fat composition and being based on the total weight of C8 to C24 fatty acids; and a percentage of saturated fatty acid on the second position of triglyceride out of total saturated fatty acid (Sn-2 SAFA %) from 8.0% to 40.0%; and wherein the fat composition has; from 50 to 90 solid fat content at 10° C.; and from 30 to 75 solid fat content at 20° C.; and from 5 to 30 solid fat content at 30° C.; measured on unstabilized fat according to ISO 8292-1.

Abstract: An edible confectionery ink composition for 3D printing comprises: from 20% to 75% by weight of sweetener, preferably sugar, and from 15% to 50% by weight of a fat composition, wherein the fat composition comprises from 45% to 65% by weight of lauric acid (C12:0); and from 15% to 25% by weight of total palmitic acid (C16:0) and stearic acid (C18:0); said percentages of acid referring to acids bound as acyl groups in glycerides in the fat composition and being based on the total weight of C8 to C24 fatty acids; and wherein the fat composition has from 80 to 100 solid fat content at 20° C.; and from 70 to 98 solid fat content at 25° C.; and from 30 to 60 solid fat content at 30° C.; measured on unstabilized fat according to ISO 8292-1.

Abstract: One aspect of the present invention relates to a method of producing a mash extract, said method comprising: a. mashing particulate, starch-containing and optionally malted raw materials with a recirculated aqueous stream; b. heating the mash and enzymatically hydrolysing the starch; c. transferring the heat-treated mash into a first separator for separation into mash extract and spent grain; d. transferring the spent grain into a first mixing vessel and mixing it with sparging water; e. transferring the mixture of spent grain and sparging water into a second separator to remove spent grain; f. recirculating an aqueous stream from the second separator to the mashing step, wherein the gravity of the fermentable mash extract obtained from the first separator is maintained at above 15° P. The present method offers the advantage that it is highly efficient in terms of energy consumption and extraction yields.

Abstract: The present invention provides a continuous method of preparing a liquid extract of cereal grain by comminuting cereal grain at a rate of at least 100 kg of dry cereal grain per hour and extracting the comminuted cereal grain with a liquid, said method comprising: continuously combining cereal grain with a liquid; continuously disintegrating the grain particles contained within the liquid by colliding freely suspended grain particles with one or more rotating blades, thereby producing a milled suspension; continuously transferring at least a part of the milled suspension, optionally after further treatment, to a separation device for separation into spent grain and liquid extract; wherein the one or more rotating blades are rotating at a tip speed of at least 10 m/s; the total mechanical energy transferred into the milled suspension by the one or more rotating blades is in the range of 5-1000 kJ per kg of dry cereal grain; and the distance between a tip of said one or more rotating blades and the axis of

Abstract: The present invention relates to a continuous method of fermenting wort, said method comprising: -fermenting wort with a biologically active yeast to produce an alcohol containing fermented liquid; -introducing the fermented liquid containing at least 10 g/l of biologically active yeast into a maturation vessel; -separately removing yeast containing sediment and supernatant liquid from the vessel; and -optionally recirculating at least a part of the yeast containing sediment to the wort fermentation; wherein the residence time of the fermented liquid in the maturation vessel exceeds 6 hours. The present method offers the advantage that it combines maturation and yeast separation into one processing step, whereas conventional continuous processes require at least two separate processing steps, one for yeast separation and one for maturation.

Abstract: The invention relates to a method of producing a bright, yeast fermented beverage, said method comprising the continuous production of wort from mash. More particularly, the present method comprises: a. mashing in a particulate, starch-containing raw material with water and enzymatically hydrolysing the starch to fermentable sugars; b. continuously producing a fermentable wort from the heated mash; c. introducing the wort into a fermenter to ferment the wort with the help of biologically active yeast; d. removing yeast from the fermentate by means of sedimentation; and e. clarifying the low-yeast fermentate to produce a bright, yeast fermented beverage by: processing the low-yeast fermentate in one or more separators to remove suspended material, said one or more separators being selected from the group consisting of centrifuges and decanter centrifuges; and filtering the processed fermentate.

Abstract: The invention provides a continuous method for the production of a yeast fermented beverage, comprising consecutive continuous processing steps; wherein the gravity of a mash extract is maintained at more than 22° P; the gravity of the wort produced from the mash extract is maintained at more than 22° P until said wort is diluted with additional water; and the gravity of the diluted wort is within the range of 10-35° P; and wherein less than 30 wt. % of the fermentable sugars in the mash extract and wort are derived from fermentable sugars added after hydrolysis of the starch contained in the mash. The method offers the advantage that it is highly efficient in terms of energy consumption and extraction yields. Furthermore, it achieves extremely high productivity, especially in the operation of the brewhouse.

Abstract: The present invention relates to a method of producing yeast fermented beverages, which method comprises the following consecutive continuous processing steps: a. introducing wort into a series of one or more propagation vessels in which it is combined with a recirculated stream of yeast-containing residue and in which the yeast is allowed to propagate under aerobic conditions while being kept suspended; b. transferring the yeast-containing wort from the propagation vessel into a series of one or more fermentation vessels in which the yeast is kept suspended under anaerobic conditions and is allowed to metabolize carbohydrates present in the wort; c. transferring at least a part of the fermented wort from the series of one or more fermentation vessels to one or more separators to remove a yeast-containing residue; d. recirculating part of the yeast-containing residue to the series of one or more propagation vessels; and e.

Abstract: The present invention relates to a mash extract and a continuous method of producing the mash extract by decoction mashing. The method comprises: (a) mixing a first malt enzyme source with an aqueous liquid to obtain an aqueous malt enzyme suspension; (b) separately, mixing a second enzyme source with one or more starch-containing adjuncts to obtain a decoction suspension; (c) subjecting the decoction suspension to a first heat treatment at 60-85° C. and then a second heat treatment at a higher temperature; (d) combining the heated decoction suspension from the second heat treatment with the aqueous malt enzyme suspension to obtain a mash; (e) maintaining the mash at 35-85° C. for a time; and (f) removing spent grain from the heated mash to produce a mash extract.

Abstract: The present invention relates to a mash extract and a continuous method of producing the mash extract by decoction mashing. The method comprises: (a) mixing a first malt enzyme source with an aqueous liquid to obtain an aqueous malt enzyme suspension; (b) separately, mixing a second enzyme source with one or more starch-containing adjuncts to obtain a decoction suspension; (c) subjecting the decoction suspension to a first heat treatment at 60-85° C. and then a second heat treatment at a higher temperature; (d) combining the heated decoction suspension from the second heat treatment with the aqueous malt enzyme suspension to obtain a mash; (e) maintaining the mash at 35-85° C. for a time; and (f) removing spent grain from the heated mash to produce a mash extract.

Abstract: The present invention relates to a continuous method of producing a mash extract by decoction mashing, said method comprising: a. mixing a first malt enzyme source with an aqueous liquid to obtain an aqueous malt enzyme suspension; b. separately, mixing a second enzyme source with one or more starch-containing adjuncts to obtain a decoction suspension while maintaining temperature conditions that do not cause significant gelatinization of the starch; c. subjecting the decoction suspension to a first heat treatment at 60-85° C. to simultaneously partially gelatinize and enzymatically degrade the starch; d. subjecting the decoction suspension to a second heat treatment at a higher temperature than the first heat treatment to gelatinize the starch at an increased rate and to a higher extent; e. combining the heated decoction suspension obtained from the second heat treatment with the aqueous malt enzyme suspension from step a. to obtain a mash; f. maintaining the mash at 35-85° C. for at least minutes; and g.

Abstract: One aspect of the invention concerns a method comprising: a. mashing particulate, starch-containing and optionally malted raw materials with water; b. heating the mash and enzymatically hydrolysing the starch; c. passing the heat-treated mash across a first sieve for separation into a fermentable mash extract and wet spent grain; d. transferring the wet spent grain, optionally after said wet spent grain has been subjected to a washing and sieving operation, to a first press and pressing said wet spent grain to obtain dewatered spent grain and additional fermentable mash extract. The present method offers the advantages of (i) being very robust, (ii) enabling the production of high gravity mash extracts (iii) consuming very little electricity and (iv) achieving high extraction yields. The invention also provides an apparatus for carrying out the aforementioned method.

Abstract: The present invention provides a continuous method of preparing a liquid extract of cereal grain by comminuting cereal grain at a rate of at least 100 kg of dry cereal grain per hour and extracting the comminuted cereal grain with a liquid, said method comprising: continuously combining cereal grain with a liquid; continuously disintegrating the grain particles contained within the liquid by colliding freely suspended grain particles with one or more rotating blades, thereby producing a milled suspension; continuously transferring at least a part of the milled suspension, optionally after further treatment, to a separation device for separation into spent grain and liquid extract; wherein the one or more rotating blades are rotating at a tip speed of at least 10 m/s; the total mechanical energy transferred into the milled suspension by the one or more rotating blades is in the range of 5-1000 kJ per kg of dry cereal grain; and the distance between a tip of said one or more rotating blades and the axis of

Abstract: One aspect of the invention concerns a method comprising: a. mashing particulate, starch-containing and optionally malted raw materials with water; b. heating the mash and enzymatically hydrolysing the starch; c. passing the heat-treated mash across a first sieve for separation into a fermentable mash extract and wet spent grain; d. transferring the wet spent grain, optionally after said wet spent grain has been subjected to a washing and sieving operation, to a first press and pressing said wet spent grain to obtain dewatered spent grain and additional fermentable mash extract. The present method offers the advantages of (i) being very robust, (ii) enabling the production of high gravity mash extracts (iii) consuming very little electricity and (iv) achieving high extraction yields. The invention also provides an apparatus for carrying out the aforementioned method.

Abstract: The invention relates to a method of producing a bright, yeast fermented beverage, said method comprising the continuous production of wort from mash. More particularly, the present method comprises: a. mashing in a particulate, starch-containing raw material with water and enzymatically hydrolysing the starch to fermentable sugars; b. continuously producing a fermentable wort from the heated mash; c. introducing the wort into a fermenter to ferment the wort with the help of biologically active yeast; d. removing yeast from the fermentate by means of sedimentation; and e. clarifying the low-yeast fermentate to produce a bright, yeast fermented beverage by: processing the low-yeast fermentate in one or more separators to remove suspended material, said one or more separators being selected from the group consisting of centrifuges and decanter centrifuges; and filtering the processed fermentate.

Abstract: The present invention provides a continuous method for the production of a yeast fermented beverage, comprising the following consecutive continuous processing steps: a. mashing starch-containing and optionally malted raw materials with aqueous liquid; b. heating the mash and enzymatically hydrolysing the starch to fermentable sugars; c. removing spent grain from the heated mash to produce a mash extract, d. converting the mash extract into wort; e. removing organic volatiles from the hot wort; f. diluting the wort with additional water; g. feeding the diluted wort into a propagation vessel in which it is combined with a recirculated stream of yeast-containing residue and in which oxygen is supplied to initiate yeast growth; h. feeding the wort from the propagation vessel into a sequence of one or more fermentation vessels in which the yeast is kept suspended; i. feeding the fermented wort into one or more separators to remove a yeast-containing residue; j.

Abstract: The present invention relates to a continuous method of fermenting wort, said method comprising: —fermenting wort with a biologically active yeast to produce an alcohol containing fermented liquid; —introducing the fermented liquid containing at least 10 g/l of biologically active yeast into a maturation vessel; —separately removing yeast containing sediment and supernatant liquid from the vessel; and —optionally recirculating at least a part of the yeast containing sediment to the wort fermentation; wherein the residence time of the fermented liquid in the maturation vessel exceeds 6 hours. The present method offers the advantage that it combines maturation and yeast separation into one processing step, whereas conventional continuous processes require at least two separate processing steps, one for yeast separation and one for maturation.

Abstract: The present invention relates to a method of producing yeast fermented beverages, which method comprises the following consecutive continuous processing steps: a. introducing wort into a series of one or more propagation vessels in which it is combined with a recirculated stream of yeast-containing residue and in which the yeast is allowed to propagate under aerobic conditions whilst being kept suspended; b. transferring the yeast-containing wort from the propagation vessel into a series of one or more fermentation vessels in which the yeast is kept suspended under anaerobic conditions and is allowed to metabolise carbohydrates present in the wort; c. transferring at least a part of the fermented wort from the series of one or more fermentation vessels to one or more separators to remove a yeast-containing residue; d. recirculating part of the yeast-containing residue to the series of one or more propagation vessels; and e.

Abstract: One aspect of the present invention relates to a method of producing a mash extract, said method comprising: a. mashing particulate, starch-containing and optionally malted raw materials with a recirculated aqueous stream; b. heating the mash and enzymatically hydrolysing the starch; c. transferring the heat-treated mash into a first separator for separation into mash extract and spent grain; d. transferring the spent grain into a first mixing vessel and mixing it with sparging water; e. transferring the mixture of spent grain and sparging water into a second separator to remove spent grain; f. recirculating an aqueous stream from the second separator to the mashing step, wherein the gravity of the fermentable mash extract obtained from the first separator is maintained at above 15° P. The present method offers the advantage that it is highly efficient in terms of energy consumption and extraction yields.

Abstract: The present invention relates to a continuous method of producing a mash extract by decoction mashing, said method comprising: a. mixing a first malt enzyme source with an aqueous liquid to obtain an aqueous malt enzyme suspension; b. separately, mixing a second enzyme source with one or more starch-containing adjuncts to obtain a decoction suspension whilst maintaining temperature conditions that do not cause significant gelatinisation of the starch; c. subjecting the decoction suspension to a first heat treatment at 60-85° C. to simultaneously partially gelatinise and enzymatically degrade the starch; d. subjecting the decoction suspension to a second heat treatment at a higher temperature than the first heat treatment to gelatinise the starch at an increased rate and to a higher extent; e. combining the heated decoction suspension obtained from the second heat treatment with the aqueous malt enzyme suspension from step a. to obtain a mash; f. maintaining the mash at 35-85° C.