WO1998022751A1 - Verfahren zum thermischen verwerten von biertrebern - Google Patents
Verfahren zum thermischen verwerten von biertrebern Download PDFInfo
- Publication number
- WO1998022751A1 WO1998022751A1 PCT/AT1997/000250 AT9700250W WO9822751A1 WO 1998022751 A1 WO1998022751 A1 WO 1998022751A1 AT 9700250 W AT9700250 W AT 9700250W WO 9822751 A1 WO9822751 A1 WO 9822751A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- spent grains
- beer
- thermal
- brewery
- plant according
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/10—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of field or garden waste or biomasses
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/10—Drying by heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/20—Dewatering by mechanical means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/40—Gasification
Definitions
- the invention relates to a method for the thermal utilization of wet beer grains, the wet beer spent grains being mechanically predried in a first drying stage, thermally dried in a further drying stage and finally thermally utilized by combustion or gasification, and a plant for carrying out the method.
- beer spent grains are a valuable feed; however, it is difficult to use the spent grains cheaply as feed.
- a problem-free possibility to sell it as feed is only available in winter - however, the beer spent grains are more abundant in summer than in winter.
- spent grains cannot be stored without pre-drying. Drying is expensive because only indirect drying is possible due to the requirements for the animal feed; this means poor heat transfer. Appropriate dryers are expensive and the energy expenditure is high.
- the sale of beer grapes as feed will be increasingly difficult in the future, as the number of cattle is declining. Conservation of the spent grains by fermentation again has the disadvantage that high costs can be expected (Brauwelt No. 39 (1991), pages 1704 to 1707).
- a composting of the spent grains speaks for the fact that a high-quality product for soil improvement is formed, but the sales market is only small and the production is so expensive that it does not cover the costs.
- Beer spent grains are also suitable for the production of biogas, but this requires high investment costs for a biogas plant.
- Beer spent grains incinerators work less effectively because of the intensive pre-drying (beer spent grains initially contain 75 to 80% by mass of water) and because of the relatively poor calorific value of the beer spent grains.
- the prerequisite for an energetic optimal use is the achievement of self-flammability, which is achieved with approx. 55% H 2 O content.
- the invention aims to avoid these disadvantages and difficulties and has as its object to provide a method of the type described above and a system for carrying out the method, which have an energetically optimal, i.e. enable profitable recycling of beer grapes if possible.
- the beer spent grains should be dried with as much external energy as possible so that the beer spent grains are thermally recycled without auxiliary firing, i.e. can be burned or gasified.
- This object is achieved in a method of the type described above in that in the further drying stage the mechanically dewatered beer spent grains are heated with the help of a flue gas produced in the energy network of a brewery Steam generation.
- gasification of pre-dried spent grains is also possible, with a combustible gas being produced as an intermediate product.
- the gas produced during gasification is advantageously used for energy, preferably as an energy source for steam generation in the brewery network, e.g. as an additional gas to the natural gas, so that it can be used energetically by burning the boiler system in the brewery.
- an additional drying to remove capillary water is preferably carried out with the help of electric fields or with the help of high-frequency fields.
- the mechanical predrying is expediently carried out to a water content of at least 65, preferably at least 62,% by mass.
- thermal drying of the mechanically pre-dried beer spent grains additional solar energy can expediently be used.
- the thermal drying of the spent grains takes place advantageously to a water content which enables them to self-burn, preferably to at least 55% by mass of water.
- press water formed in the mechanical predrying is processed anaerobically and the methane-containing gas formed in this way is used for energy, preferably as an energy source for steam generation in the brewery network.
- Exhaust gases generated when the dried beer spent grains are burned are disposed of inexpensively together with exhaust gases formed in a steam boiler of the brewery.
- mixtures of beer spent grains and other organic, biogenic waste are thermally utilized.
- a system for carrying out the method with a mechanical dryer forming a first drying stage for beer spent grains and with a thermal dryer forming a further drying stage forming for mechanically dewatered beer spent grains and with a device for thermal recycling by burning or gasifying the dried beer spent grains is characterized in that the thermal dryer emits a flue gas leading from a steam boiler of the brewery energy network.
- the device for thermal recycling of the spent grains preferably has a combustion boiler, the combustion boiler expediently being equipped with a steam generation device and the steam generation device advantageously being coupled to the energy network of the brewery.
- a flue gas discharge from the combustion boiler opens into an exhaust system of a beer production system, with an exhaust line from the thermal dryer also advantageously opening into the exhaust system of the beer production system.
- the device for thermal utilization has a gasification device, wherein a line which leads from the gasification device and which conducts gases generated in the gasifier expediently leads to a burner of a steam boiler of the brewery's energy network.
- the mechanical dryer can preferably be designed as a belt press or as a screw press.
- a convection dryer is useful as a thermal dryer.
- the thermal dryer preferably has a drying device that can be operated with solar energy.
- the thermal drying, the gasification and the combustion can be combined in one apparatus, whereby it is expedient to direct the hot exhaust gases from the device having the thermal drying, the gasification and the combustion to the steam boiler of the energy consumer of the brewery is led.
- thermal drying can be extended by a drying device that can be operated with solar energy.
- FIGS. 1 and 2 each illustrating a process diagram according to an embodiment variant.
- a first drying stage 2 the wet beer spent grains 1 are brought to a water content in the range of about 65 to 62 mass% in a mechanical dryer 3, which is designed as a screw press according to FIG. 1. With this water content, it is not yet possible to burn the spent grains without auxiliary firing. For this reason, a further drying takes place in a further drying stage 4, in which the mechanically dewatered beer spent grains 5 are dried thermally.
- This drum dryer 6 is heated directly with flue gas supplied via line 7, which comes from a boiler 10 installed in a beer production system 8.
- the boiler 10 is heated with natural gas, which is supplied via line 9; the steam-carrying pipes are designated 11.
- Part of the flue gas can be fed directly to an exhaust gas blower 13 of the flue gas disposal system via a branch line 12.
- the flue gas discharge line 14 emerging from the drum dryer 6 also opens into this flue gas disposal system.
- the dried beer spent grains 15 are burned by means of burners 16 in a combustion boiler 17 in which a steam generating device 18 is installed.
- the steam generated in this steam generating device 18 is usefully used for beer production, ie natural gas for the natural gas burner 19 in the natural gas-fired boiler 10 can be saved.
- the ash discharge is designated 20.
- the wet beer spent grains 1 are first subjected to mechanical drying in a first drying stage 2 by means of a belt press 21.
- the mechanically dewatered spent grains are then fed to a thermal dryer designed as a convection dryer 22 in the second drying stage 4, in which the spent beer 5 is dried to a water content below the self-burning limit using flue gas, which comes from a beer production system 8, as shown in FIG. 1.
- the thermal utilization of the dry beer spent grains 15 takes place according to FIG. 2 in a gasifier 23, to which oxygen or an oxygen-containing gas, such as air, is supplied via a sieve plate 24.
- the ash discharge is designated 20.
- the gases produced in the gasifier 23 are highly flammable and can replace part of the natural gas used in the beer production plant as fuel gases; they are fed to the natural gas burner 19 via line 25.
- the advantage of this method compared to the combustion is that no additional solid combustion boiler is required and that the nitrogen and sulfur oxides generated during the combustion are avoided.
- Gasification produces a gas that consists primarily of carbon monoxide, carbon dioxide, hydrogen and molecular nitrogen.
- drying methods can also be used in addition to the mechanical and thermal drying, for example drying with the aid of high-frequency fields or electromagnetic fields.
- Natural energy such as solar energy, can also be used to support the thermal drying, the solar energy being supplied before or after the thermal drying stage 4 - depending on the dew point of the flue gas.
- Beer spent grains 1 with a water content of approx. 80% by mass per year.
- the accruing Beer spent grains 1 are mechanically pre-dried with a press (eg screw press 3) to a water content of approx. 62% by mass.
- a press eg screw press 3
- With a quantity of 24,000 t wet beer grains, which are mechanically dewatered to a water content of 62% by mass, 11,370 t press water / a are obtained.
- the resulting press water 26 is advantageously fed to an anaerobic water purification - which is not shown in the figures - in which a combustible gas containing methane is obtained. Approx.
- drying methods for reducing the capillary water can be used to further reduce the water content.
- Water transport in an electric field (electro-osmosis) or exposure to high-frequency fields can be used to mobilize part of the bound water, which can then be made accessible to further mechanical pressing.
- thermal drying is then carried out to a greater or lesser extent in order to achieve the self-burning degree.
- the mechanically and alternatively pre-dried beer spent grains 5 are continuously conveyed via a buffer tank into a directly heated dryer (e.g. drum dryer 6) and with the 140 to 160 ° C hot flue gases from natural gas combustion by convection to at least the self-burning degree of approx. 55 Ma. -% water dried.
- the dry material 15 is now fed to a combustion boiler 17 for biogenic waste and burned.
- the calorific value of the spent grains is linearly dependent on the water content and is 55 Ma .-% water at approx. 7.68 MJ / kg.
- Approximately 190 m 3 of natural gas can be substituted by burning one ton of spent grain.
- a total of 4.5 million Nm 3 natural gas / a is required in a brewery of the size mentioned. Of this, 2 million m 3 natural gas / a, which is more than a third, can be substituted by spent grain combustion.
- the NO x emissions can be minimized.
- Another problem is the sulfur dioxide produced during the combustion.
- the CO value can also be checked by adjusting the ⁇ value, thus optimizing the NO x value and the CO value.
- Another way of reducing NO x is, for example, the injection of NH 3 .
- the invention is not limited to the examples described above, but can be modified in various ways.
- the drying of the wet beer spent grains can be accomplished with any number of drying stages, however, at least one mechanical drying stage 2 and at least one thermal drying stage 4 are essential.
- combined apparatus designs for thermal predrying, gasification and combustion are possible, which also meet the criteria mentioned above .
- the method according to the invention can be expanded insofar as, in addition to the beer spent grains, other biogenic waste such as sewage sludge are also included in the process in order to be able to increase the energy content and thus the production of steam.
- biogenic waste such as sewage sludge
- the mixture of spent grains and other biogenic waste is treated in the same way as explained in the process description.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Processing Of Solid Wastes (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Treatment Of Sludge (AREA)
- Drying Of Solid Materials (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Alcoholic Beverages (AREA)
- Cereal-Derived Products (AREA)
- Fertilizers (AREA)
Abstract
Description
Claims
Priority Applications (14)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SI9720080A SI20034A (sl) | 1996-11-20 | 1997-11-18 | Postopek za toplotno izkoriščanje sladnih tropin |
RO99-00577A RO118680B1 (ro) | 1996-11-20 | 1997-11-18 | Procedeu si instalatie pentru valorificarea pe cale termica a borhotului de bere umed |
DK97911953T DK1007884T3 (da) | 1996-11-20 | 1997-11-18 | Fremgangsmåde og anlæg til termisk udnyttelse af mask |
KR10-1999-7004482A KR100502965B1 (ko) | 1996-11-20 | 1997-11-18 | 엿기름찌꺼기의 열적 활용 방법 |
JP52300798A JP3963481B2 (ja) | 1996-11-20 | 1997-11-18 | ビールかすを熱的に利用する方法 |
BR9713369-8A BR9713369A (pt) | 1996-11-20 | 1997-11-18 | Processo para o aproveitamento térmico de borras de cerveja |
AT97911953T ATE211238T1 (de) | 1996-11-20 | 1997-11-18 | Verfahren und anlage zum thermischen verwerten von biertrebern |
EP97911953A EP1007884B1 (de) | 1996-11-20 | 1997-11-18 | Verfahren und anlage zum thermischen verwerten von biertrebern |
HU0000151A HU226171B1 (en) | 1996-11-20 | 1997-11-18 | Method and equipment for the thermal utilization of spent grain |
DE59705928T DE59705928D1 (de) | 1996-11-20 | 1997-11-18 | Verfahren und anlage zum thermischen verwerten von biertrebern |
PL97333666A PL188043B1 (pl) | 1996-11-20 | 1997-11-18 | Sposób i instalacja do termicznej utylizacji mokrego młóta |
AU49343/97A AU4934397A (en) | 1996-11-20 | 1997-11-18 | Method for the thermal utilization of spent grain |
US09/315,199 US6167636B1 (en) | 1996-11-20 | 1999-05-19 | Process for thermally utilizing spent grains |
BG103481A BG63514B1 (bg) | 1996-11-20 | 1999-06-10 | Метод за термично оползотворяване на бирени джибри |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ATA2022/96 | 1996-11-20 | ||
AT0202296A AT404253B (de) | 1996-11-20 | 1996-11-20 | Verfahren zum thermischen verwerten von biertrebern |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/315,199 Continuation US6167636B1 (en) | 1996-11-20 | 1999-05-19 | Process for thermally utilizing spent grains |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998022751A1 true WO1998022751A1 (de) | 1998-05-28 |
Family
ID=3526124
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AT1997/000250 WO1998022751A1 (de) | 1996-11-20 | 1997-11-18 | Verfahren zum thermischen verwerten von biertrebern |
Country Status (20)
Country | Link |
---|---|
US (1) | US6167636B1 (de) |
EP (1) | EP1007884B1 (de) |
JP (1) | JP3963481B2 (de) |
KR (1) | KR100502965B1 (de) |
CN (1) | CN1135322C (de) |
AT (2) | AT404253B (de) |
AU (1) | AU4934397A (de) |
BG (1) | BG63514B1 (de) |
BR (1) | BR9713369A (de) |
DE (1) | DE59705928D1 (de) |
DK (1) | DK1007884T3 (de) |
ES (1) | ES2170376T3 (de) |
HU (1) | HU226171B1 (de) |
ID (1) | ID22287A (de) |
PL (1) | PL188043B1 (de) |
PT (1) | PT1007884E (de) |
RO (1) | RO118680B1 (de) |
SI (1) | SI20034A (de) |
TR (1) | TR199901798T2 (de) |
WO (1) | WO1998022751A1 (de) |
Cited By (10)
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EP2258816A1 (de) * | 2008-02-18 | 2010-12-08 | Kuriyama, Shinsuke | Fester brennstoff und verfahren zur herstellung von festem brennstoff |
WO2011141106A1 (de) | 2010-04-15 | 2011-11-17 | Ziemann Energy Gmbh | Verbrennungsanlage für nasstreber und dergleichen |
DE102012202532A1 (de) | 2012-02-20 | 2013-08-22 | Siemens Aktiengesellschaft | Verfahren zum Verwerten von Treber in einer Brauerei und zugehörige Vorrichtung |
US10364400B2 (en) * | 2011-09-01 | 2019-07-30 | Akbev Group, Llc | Spent grain fuel product and process |
US10982162B2 (en) | 2011-09-01 | 2021-04-20 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
WO2021080450A1 (ru) | 2019-10-21 | 2021-04-29 | БиоБо ГмбХ | Белковая суспензия из пивной дробины, способ и установка для ее получения |
WO2021201711A1 (ru) | 2020-04-02 | 2021-10-07 | "Биобо Гмбх" | Белковый продукт из пивной дробины и способ его получения |
US11441090B2 (en) | 2011-09-01 | 2022-09-13 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
US11866669B2 (en) | 2011-09-01 | 2024-01-09 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
EP4388887A1 (de) | 2022-12-21 | 2024-06-26 | Citerco Partners LP | Verfahren zur gewinnung von proteinkonzentrat, proteinmehl und gerstenöl aus nassen biertrebern |
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IT1316197B1 (it) * | 2000-06-14 | 2003-04-03 | Turatti Srl | Apparecchio per la asciugatura in continuo di verdure, in particolareverdure in foglie. |
US20090227452A1 (en) * | 2001-09-14 | 2009-09-10 | Birthisel Timothy D | Spent fermented grain soil additive |
MX2007001500A (es) * | 2004-08-05 | 2007-07-04 | Microcoal Inc | Control de energia en una planta de generacion de energia. |
FR2904825B1 (fr) * | 2006-08-08 | 2008-10-10 | Degremont Sa | Procede et installation de conditionnement de boues avant sechage |
DE102008028600A1 (de) | 2008-06-18 | 2009-12-31 | Gea Brewery Systems Gmbh | Sudhausanlage mit Filtrationseinrichtung und Verfahren zur thermischen Verwertung von feuchten Filtrationspartikeln |
AR069826A1 (es) * | 2008-11-05 | 2010-02-24 | Pampa Group Srl | Procedimiento para secar hez de malta |
DE102008060140B4 (de) | 2008-12-03 | 2020-05-20 | Gunther Pesta | Biertreberhydrolyseverfahren |
DE102009021692A1 (de) | 2009-05-18 | 2010-12-02 | Ziemann Energy Gmbh | Verfahren zum Behandeln von Reststoffen von Brauereien |
AT508723B1 (de) | 2009-08-07 | 2013-03-15 | Hertel Katja | Bierbereitungsverfahren sowie zugehörige vorrichtung |
US10781388B2 (en) | 2011-09-01 | 2020-09-22 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
US9447354B2 (en) * | 2011-09-01 | 2016-09-20 | Akbev Llc | Spent grain fuel product and process |
WO2018080593A1 (en) * | 2016-10-28 | 2018-05-03 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
US9184593B2 (en) | 2012-02-28 | 2015-11-10 | Microcoal Inc. | Method and apparatus for storing power from irregular and poorly controlled power sources |
CN102759257A (zh) * | 2012-04-22 | 2012-10-31 | 广州市香港科大霍英东研究院 | 一种应用于生物质发电系统的生物质干燥系统 |
US10104897B2 (en) | 2012-12-28 | 2018-10-23 | Thomas Brown | Systems and methods for making spent grain dough products |
DE102013107985A1 (de) * | 2013-07-25 | 2015-01-29 | Kotyk Energy Ag | Vorrichtung zur Erzeugung für Energie aus Biomasse und Verfahren zur Energiegewinnung aus Biomasse |
DE102013018040A1 (de) | 2013-12-02 | 2015-06-03 | Enwat Gmbh | Verfahren zur energetischen Verwertung von Trebern aus der Bierherstellung |
US9810480B2 (en) | 2015-06-12 | 2017-11-07 | Targeted Microwave Solutions Inc. | Methods and apparatus for electromagnetic processing of phyllosilicate minerals |
CN104913317B (zh) * | 2015-06-23 | 2017-12-12 | 内江市雨果生物科技有限公司 | 水稻秸秆的环保处理方法 |
CN107166401A (zh) * | 2017-05-24 | 2017-09-15 | 江苏大学 | 一种高湿醋糟气化直燃利用装置及其方法 |
CN112944382B (zh) * | 2021-02-05 | 2022-07-12 | 河南省锅炉压力容器安全检测研究院 | 一种高含水量生物质燃料烟气废热利用烘干预处理装置 |
US12091646B2 (en) * | 2022-11-04 | 2024-09-17 | Fermentation Technology Services | Methods for moisture removal and pest control of grains |
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EP0423400A1 (de) * | 1989-10-16 | 1991-04-24 | Deutsche Voest-Alpine Industrieanlagenbau Gmbh | Entsorgungseinrichtung |
DE4443482A1 (de) * | 1994-12-07 | 1996-06-13 | Kloeckner Humboldt Deutz Ag | Verfahren zur Erzeugung von in der Baustoffindustrie verwertbarer Schlacke aus Klärschlamm |
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US5191723A (en) * | 1991-01-09 | 1993-03-09 | Herzog Contracting Corporation | Apparatus and method for recovering spent lime for use as a nutritional flowing agent for poultry and animal feeds |
US5433019A (en) * | 1991-09-27 | 1995-07-18 | Industrial Technology Research Institute | Process and an apparatus for producing teas |
US5535528A (en) * | 1994-02-01 | 1996-07-16 | By-Product Solutions, Inc. | Agglomerating waste sludge and yard waste |
US5637336A (en) * | 1994-04-29 | 1997-06-10 | Kannenberg; James R. | Process for drying malt |
NL1000482C2 (nl) * | 1995-06-01 | 1996-12-03 | Tno | Werkwijze en inrichting voor het verwarmen en koelen van voedingsproduk- ten. |
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1996
- 1996-11-20 AT AT0202296A patent/AT404253B/de not_active IP Right Cessation
-
1997
- 1997-11-18 JP JP52300798A patent/JP3963481B2/ja not_active Expired - Fee Related
- 1997-11-18 ES ES97911953T patent/ES2170376T3/es not_active Expired - Lifetime
- 1997-11-18 CN CNB971813558A patent/CN1135322C/zh not_active Expired - Fee Related
- 1997-11-18 TR TR1999/01798T patent/TR199901798T2/xx unknown
- 1997-11-18 AT AT97911953T patent/ATE211238T1/de active
- 1997-11-18 WO PCT/AT1997/000250 patent/WO1998022751A1/de active IP Right Grant
- 1997-11-18 PL PL97333666A patent/PL188043B1/pl not_active IP Right Cessation
- 1997-11-18 HU HU0000151A patent/HU226171B1/hu not_active IP Right Cessation
- 1997-11-18 ID IDW990385A patent/ID22287A/id unknown
- 1997-11-18 PT PT97911953T patent/PT1007884E/pt unknown
- 1997-11-18 DE DE59705928T patent/DE59705928D1/de not_active Expired - Lifetime
- 1997-11-18 RO RO99-00577A patent/RO118680B1/ro unknown
- 1997-11-18 DK DK97911953T patent/DK1007884T3/da active
- 1997-11-18 KR KR10-1999-7004482A patent/KR100502965B1/ko not_active IP Right Cessation
- 1997-11-18 SI SI9720080A patent/SI20034A/sl not_active IP Right Cessation
- 1997-11-18 AU AU49343/97A patent/AU4934397A/en not_active Abandoned
- 1997-11-18 BR BR9713369-8A patent/BR9713369A/pt not_active IP Right Cessation
- 1997-11-18 EP EP97911953A patent/EP1007884B1/de not_active Expired - Lifetime
-
1999
- 1999-05-19 US US09/315,199 patent/US6167636B1/en not_active Expired - Fee Related
- 1999-06-10 BG BG103481A patent/BG63514B1/bg unknown
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US4290269A (en) * | 1979-10-09 | 1981-09-22 | Modo-Chemetics Ab | Process for the efficient conversion of water-containing organic materials as fuels into energy |
EP0423400A1 (de) * | 1989-10-16 | 1991-04-24 | Deutsche Voest-Alpine Industrieanlagenbau Gmbh | Entsorgungseinrichtung |
DE4443482A1 (de) * | 1994-12-07 | 1996-06-13 | Kloeckner Humboldt Deutz Ag | Verfahren zur Erzeugung von in der Baustoffindustrie verwertbarer Schlacke aus Klärschlamm |
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"Brauwelt", vol. 39, 1991, pages: 1704-7 |
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EP2258816A4 (de) * | 2008-02-18 | 2012-01-25 | Kuriyama Shinsuke | Fester brennstoff und verfahren zur herstellung von festem brennstoff |
EP2258816A1 (de) * | 2008-02-18 | 2010-12-08 | Kuriyama, Shinsuke | Fester brennstoff und verfahren zur herstellung von festem brennstoff |
WO2011141106A1 (de) | 2010-04-15 | 2011-11-17 | Ziemann Energy Gmbh | Verbrennungsanlage für nasstreber und dergleichen |
DE102010015039A1 (de) | 2010-04-15 | 2013-01-31 | Ziemann Energy Gmbh | Verbrennungsanlage für Nasstreber und dergleichen |
US11441090B2 (en) | 2011-09-01 | 2022-09-13 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
US10364400B2 (en) * | 2011-09-01 | 2019-07-30 | Akbev Group, Llc | Spent grain fuel product and process |
US10982162B2 (en) | 2011-09-01 | 2021-04-20 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
US11866669B2 (en) | 2011-09-01 | 2024-01-09 | Akbev Group, Llc | High protein organic materials as fuel and processes for making the same |
DE102012202532A1 (de) | 2012-02-20 | 2013-08-22 | Siemens Aktiengesellschaft | Verfahren zum Verwerten von Treber in einer Brauerei und zugehörige Vorrichtung |
WO2013124124A1 (de) | 2012-02-20 | 2013-08-29 | Siemens Aktiengesellschaft | Verfahren zum verwerten von treber in einer brauerei und zugehörige vorrichtung |
WO2021080450A1 (ru) | 2019-10-21 | 2021-04-29 | БиоБо ГмбХ | Белковая суспензия из пивной дробины, способ и установка для ее получения |
DE112019007829T5 (de) | 2019-10-21 | 2022-07-07 | BioBo GmbH | Proteinsuspension aus Biertreiber, Verfahren und Vorrichtung zu deren Erzeugung |
US11576401B2 (en) | 2019-10-21 | 2023-02-14 | BioBo GmbH | Protein suspension from brewer's grains, method and apparatus for obtaining same |
DE112020006997T5 (de) | 2020-04-02 | 2023-01-12 | BioBo GmbH | Proteinöses erzeugnis aus biertreber und verfahren zu dessen erzeugung |
US11712048B2 (en) | 2020-04-02 | 2023-08-01 | BioBo GmbH | Protein product obtained from brewer's grains and its production method |
WO2021201711A1 (ru) | 2020-04-02 | 2021-10-07 | "Биобо Гмбх" | Белковый продукт из пивной дробины и способ его получения |
EP4388887A1 (de) | 2022-12-21 | 2024-06-26 | Citerco Partners LP | Verfahren zur gewinnung von proteinkonzentrat, proteinmehl und gerstenöl aus nassen biertrebern |
Also Published As
Publication number | Publication date |
---|---|
JP3963481B2 (ja) | 2007-08-22 |
BG103481A (en) | 2000-03-31 |
AU4934397A (en) | 1998-06-10 |
ID22287A (id) | 1999-09-30 |
EP1007884B1 (de) | 2001-12-19 |
BR9713369A (pt) | 2000-01-25 |
HU226171B1 (en) | 2008-05-28 |
PT1007884E (pt) | 2002-05-31 |
HUP0000151A3 (en) | 2000-11-28 |
RO118680B1 (ro) | 2003-08-29 |
DE59705928D1 (de) | 2002-01-31 |
CN1135322C (zh) | 2004-01-21 |
JP2001504205A (ja) | 2001-03-27 |
CN1244908A (zh) | 2000-02-16 |
KR100502965B1 (ko) | 2005-07-25 |
ATE211238T1 (de) | 2002-01-15 |
KR20000069062A (ko) | 2000-11-25 |
PL188043B1 (pl) | 2004-11-30 |
HUP0000151A2 (hu) | 2000-06-28 |
DK1007884T3 (da) | 2002-04-15 |
ATA202296A (de) | 1998-02-15 |
AT404253B (de) | 1998-10-27 |
ES2170376T3 (es) | 2002-08-01 |
TR199901798T2 (xx) | 1999-10-21 |
EP1007884A1 (de) | 2000-06-14 |
US6167636B1 (en) | 2001-01-02 |
SI20034A (sl) | 2000-02-29 |
BG63514B1 (bg) | 2002-03-29 |
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