EP3877498A1 - Process for producing a filler from whole stillage, filler, use of a filler and foodstuff - Google Patents
Process for producing a filler from whole stillage, filler, use of a filler and foodstuffInfo
- Publication number
- EP3877498A1 EP3877498A1 EP18799710.1A EP18799710A EP3877498A1 EP 3877498 A1 EP3877498 A1 EP 3877498A1 EP 18799710 A EP18799710 A EP 18799710A EP 3877498 A1 EP3877498 A1 EP 3877498A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- weight
- stillage
- food
- filler
- sugar
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/115—Cereal fibre products, e.g. bran, husk
-
- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT OF FLOUR OR DOUGH FOR BAKING, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS
- A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
- A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
- A21D2/36—Vegetable material
- A21D2/368—Fermentation by-products, e.g. grapes, hops
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12F—RECOVERY OF BY-PRODUCTS OF FERMENTED SOLUTIONS; DENATURED ALCOHOL; PREPARATION THEREOF
- C12F3/00—Recovery of by-products
- C12F3/10—Recovery of by-products from distillery slops
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/20—Reducing nutritive value; Dietetic products with reduced nutritive value
- A23L33/21—Addition of substantially indigestible substances, e.g. dietary fibres
Definitions
- the invention relates to a method for producing a filler from stillage, a filler obtained or obtainable by this method, a use of such a filler and a food with at least one such filler.
- Sugar and / or sugar substitutes are used to sweeten many different foods.
- “sugar substitutes” are understood to mean, among other things, the substances that are listed in Appendix 2 to the German Ordinance on the Approval of Additives to Food for Technological Purposes (Additive Approval Ordinance of 29 January 1998 (BGBl. I.
- sugar substitute thus includes the sugar substitutes listed in part A of the said plant (sorbitol (E 420), mannitol (E 421), isomalt (E 953), maltitol
- sugar substitute also includes also the sugar substitute erythritol (E 968) and the sweeteners Advantam (E 969), stevioside glycosides (E 960), polyglycitol syrup (E 964) and lactitol (E 966).
- sweetener also includes also the sugar substitute erythritol (E 968) and the sweeteners Advantam (E 969), stevioside glycosides (E 960), polyglycitol syrup (E 964) and lactitol (E 966).
- sweetener are also to be understood in this sense below.
- a first aspect of the invention relates to a method for producing a filler from stillage.
- the residues of a fermentation liquid will be understood by carbohydrates and distilling ugur Anlagenen of alcohol Z to the Ab.
- Schlempe usually contains proteins, fats, fibers and also minerals. Among other things, it arises as a by-product obtained from the production of bioethanol based on starchy cereals. Dried mash from grain mash is also known as dry mash or DDGS ("Dried Distillers Grains with Solubles"). Mash has a high protein content of up to 30% in some cases.
- the process according to the invention contains the following steps, which are carried out preferably, but not necessarily in this order: a) comminuting the stillage,
- the crushing of the stillage in step a) is necessary for further processing and the sensory properties in the end product.
- Heating the stillage in step b) serves to decontaminate and thus to eliminate pathogenic germs and spoilage organisms in particular. This is important on the one hand for the further processing of the stillage and on the other hand for a food for which the filler is used.
- the fermentation of the stillage in optional step c) serves to develop a specific taste and to further stabilize the product.
- the optional reduction of the moisture of the stillage in step d) serves the final stabilization in order to obtain a storable product.
- the addition of taste-modifying food additives such as sweeteners and / or flavors can compensate for the sensory quality which is adversely affected by a sugar reduction.
- the filler produced by the process according to the invention can be used as a supplement in a foodstuff which contains in particular sugar and / or at least one sugar substitute.
- the volume in the recipe of the food can be replenished, which for example by reducing the sugar content and / or at least partially replacing sugar with a sugar substitute.
- the quality of the food is not adversely affected by the addition of the filler obtained by the process according to the invention.
- the method according to the invention permits further, economical use of the stillage in addition to use as animal feed.
- the process is used to produce a storable processing form of
- Stillage In addition, food can be upgraded in terms of nutritional value through the use of the filler, since the stillage has a relatively high protein and fiber content.
- stillage is used which was obtained as a by-product in the production of bioethanol based on starchy cereals. It is particularly advantageous if the stillage was removed directly from the bioethanol production before step a) and was not, for example, temporarily stored and / or transported. In this way, the perishability of the slurry can be counteracted.
- the grinding of the stillage in step a) can include grinding. Depending on the order of the process steps, this can be, for example, wet grinding or dry grinding. If the grinding is carried out as the first process step, wet grinding can be carried out, for example using a colloid mill. He follows the grinding after drying, preferably a dry grinding is carried out, for example with a roller.
- Step a), in particular after grinding, and before the optional reduction of moisture in step d) should see 200 ym and 1600 ym, preferably with an average particle diameter in the range of 250 ym to 500 ym, a narrower particle size distribution and a smaller average particle size diameter are preferred.
- the particle size distribution can be determined, for example, using a laser diffraction method known per se.
- step b) the stillage is preferably heated to a temperature which is in the range from 70 ° C. to 130 ° C., preferably in the range from 80 ° C. to 121 ° C. This temperature is preferably kept for a period of 2 minutes to 120 minutes.
- the heating step can also include at least two heating stages, with a cooling phase taking place between two heating stages, which leads to germination of the spores contained in the product. These germinated spores can be inactivated by the subsequent second heating stage.
- This heating step can optionally also be carried out before comminution, in particular before grinding.
- a fermentation can preferably take place in a step c).
- a fermentation can alternatively or additionally be carried out during at least one, in particular during all other process steps.
- the fermentation serves to increase digestibility, the sensory enhancement of the product and an additional stabilization of the stillage by suppressing pathogens and spoilage organisms.
- the fermentation can take place with yeast or lactic acid bacteria or other bacterial strains. Their metabolic products reduce the pH of the stillage and lead to the development of a specific taste. If the product is not used as a paste, there is a
- step d) contains a first sub-step dl) in which the
- Moisture of the stillage is reduced mechanically. This can be achieved, for example, by pressing out the stillage, for example with a belt or screw press. In this way, the moisture of the stillage can be reduced comparatively quickly and easily, and the cost of thermal moisture removal can be minimized.
- the moisture of the stillage immediately after the first sub-step dl) is in the range of
- 50% by weight to 70% by weight preferably in the range from 50% by weight to 65% by weight, particularly preferably in the range from 50% by weight to 60% by weight.
- the moisture of the stillage is preferably reduced after partial step dl) or directly without partial step dl) by a thermal process, for example with the aid of mill drying (for example with a so-called “flash dryer”) or roller drying.
- a further grinding step should preferably be carried out in order to achieve the desired particle sizes.
- the moisture in the stillage immediately after step d), in particular after the second sub-step d2), is in the range from 4% by weight to 15% by weight, preferably in the range from 5% by weight to 10% by weight. %, particularly preferably in the range from 6% by weight to 9% by weight. Moisture in this area allows the slurry to be stored or transported in a stable state.
- the dried product has particle sizes from 50 ⁇ m to 1000 ⁇ m, preferably from 100 ⁇ m to 800 ⁇ m, more preferably from 100 ⁇ m to 500 ⁇ m, in particular with a medium particle size cone size diameter from 100 ym to 300 ym (measured with laser diffraction method).
- At least one taste-modifying food additive in particular at least one sugar substitute and / or at least one aroma, is optional
- Step e) can take place in a mixer, for example in a so-called batch mixer.
- Another aspect of the invention relates to a filler obtained or obtainable by a method as described above.
- a filler can be provided and designed to supplement sugar and / or at least one sugar substitute in a food.
- This filler has the advantages already described.
- the filler can be in the form of a powder or a paste, for example.
- the filler can also be used in the context of the invention for other purposes than to supplement sugar and / or at least one sugar substitute in food.
- the invention relates to a use of the filler for supplementing in a food, in particular for supplementing sugar and / or at least one sugar substitute in a food.
- the filler can be used to supplement a sugar substitute and / or a sweetener.
- the invention relates to a food which contains at least one filler according to the invention.
- the food optionally also contains sugar and / or at least one sugar substitute.
- the food may contain at least one sugar substitute and / or at least one sweetener as at least one sugar substitute.
- the proportion of sugar in the food is at least 2% by weight, preferably at least 3.5% by weight, more preferably at least 5% by weight, particularly preferably at least 7.5% by weight; and or
- the proportion of sugar substitute is at least 0.06% by weight, preferably at least 0.10% by weight, further preferably at least 0.15% by weight, particularly preferably at least 0.23% by weight; and or
- the food can be selected from the group consisting of the following foods:
- Snacks in particular cereal bars and snack bars, where the snacks can be pressed, fried and / or toasted,
- step a In the production of bioethanol, which is known per se, stillage was separated with a moisture content of approx. 78% by weight. This stillage was stabilized in step a) by heating to about 100 ° C. for 5.4 minutes. Thereafter, in a step b), the moisture was mechanically reduced to about 70% by weight and in a step c) a fermentation was carried out using yeast. The material was then dried in a thermal drying step d) to 6.5% by weight moisture. This material was then in one
- This dry powder was used to make Schlempe butter biscuits from the following recipe: 250 g butter,
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Food Science & Technology (AREA)
- Organic Chemistry (AREA)
- Genetics & Genomics (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Nutrition Science (AREA)
- Biochemistry (AREA)
- Polymers & Plastics (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
Abstract
Description
Claims
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/EP2018/080194 WO2020094209A1 (en) | 2018-11-05 | 2018-11-05 | Process for producing a filler from whole stillage, filler, use of a filler and foodstuff |
Publications (1)
Publication Number | Publication Date |
---|---|
EP3877498A1 true EP3877498A1 (en) | 2021-09-15 |
Family
ID=64184062
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP18799710.1A Withdrawn EP3877498A1 (en) | 2018-11-05 | 2018-11-05 | Process for producing a filler from whole stillage, filler, use of a filler and foodstuff |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP3877498A1 (en) |
WO (1) | WO2020094209A1 (en) |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3704651A1 (en) * | 1987-02-14 | 1988-08-25 | Wickueler Kuepper Brauerei Gmb | Process for isolating high-fibre and low-lipid fractions from spent brewer's grains |
GB9216135D0 (en) * | 1992-07-29 | 1992-09-09 | Sandoz Nutrition Ltd | Organic compounds |
DE4243879C1 (en) * | 1992-12-23 | 1994-03-24 | Lutz Kienlin | Prepn of foodstuffs obtd from brewers grains - by pressing and grinding grains, adding additives and drying |
DK9700015U3 (en) * | 1997-01-14 | 1997-04-11 | Anton Aarup | Fiber and protein product |
RU2609246C2 (en) * | 2011-12-16 | 2017-01-31 | Марк ТЁЛЛЕ | Method of milled grain distillery slop preparation |
-
2018
- 2018-11-05 EP EP18799710.1A patent/EP3877498A1/en not_active Withdrawn
- 2018-11-05 WO PCT/EP2018/080194 patent/WO2020094209A1/en unknown
Also Published As
Publication number | Publication date |
---|---|
WO2020094209A1 (en) | 2020-05-14 |
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