EP1007884B1 - Verfahren und anlage zum thermischen verwerten von biertrebern - Google Patents

Verfahren und anlage zum thermischen verwerten von biertrebern Download PDF

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Publication number
EP1007884B1
EP1007884B1 EP97911953A EP97911953A EP1007884B1 EP 1007884 B1 EP1007884 B1 EP 1007884B1 EP 97911953 A EP97911953 A EP 97911953A EP 97911953 A EP97911953 A EP 97911953A EP 1007884 B1 EP1007884 B1 EP 1007884B1
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EP
European Patent Office
Prior art keywords
drying
several
spent grain
brewery
thermal
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.)
Expired - Lifetime
Application number
EP97911953A
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German (de)
English (en)
French (fr)
Other versions
EP1007884A1 (de
Inventor
Leopold Werner Kepplinger
Dieter Pelz
Gerald Zanker
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ziemann Energy GmbH
Original Assignee
Brau-Union Osterreich AG
Brau Union Oesterreich AG
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Filing date
Publication date
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Application filed by Brau-Union Osterreich AG, Brau Union Oesterreich AG filed Critical Brau-Union Osterreich AG
Publication of EP1007884A1 publication Critical patent/EP1007884A1/de
Application granted granted Critical
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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 spent grains, the wet beer spent grains mechanically predried in a first drying stage, in a further drying stage thermally dried and finally by burning or Gasification can be thermally recycled, as well as a plant to carry out the process.
  • the large amount of wet beer spent grains is a problem in beer production during disposal or recycling. About 20 kg of wet beer spent grains fall per hectoliter of beer so that hundreds of tons of spent beer are thrown away or thrown away at large breweries are recyclable.
  • beer spent grains Due to their composition, beer spent grains are a valuable feed; it is however difficult to use the beer spent grains cheaply as feed.
  • An easy one Settling as feed is only possible in winter - the beer grains, on the other hand, fall in summer in larger quantities than in winter.
  • beer spent grains are not without Store pre-drying. Drying is expensive because of the requirements of the Feed only indirect drying is possible; this means a bad one Heat transfer. Appropriate dryers are expensive and the energy expenditure is high.
  • the sale of beer spent grains as animal feed will become increasingly difficult in the future as the Livestock is declining.
  • a preservation of the spent grains through fermentation brings again 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, however, the sales market is only small and so is the production costly that it does not cover costs.
  • Beer spent grains are also suitable for the production of biogas, but are high for this Investment costs for a biogas plant required.
  • Direct combustion is an energetically practicable recycling process for beer spent grains. From the magazine “Brauwelt” No. 26 (1988), pages 1156 to 1158, "The energetic Utilization of beer spent grains ", is a process for producing energy from beer spent grains, such as described at the beginning, known. Beer spent grains incinerators work because of that intensive pre-drying (beer spent grains initially contain 75 to 80% by mass Water) and, due to the relatively poor calorific value of the spent beer, not very effective.
  • the invention aims at avoiding these disadvantages and difficulties and presents itself the task, a method of the type described above and a system for To carry out the process to create an energetically optimal, i.e. to Possibility of profitable utilization of beer grapes.
  • the Dried the spent grains with as much external energy as possible that the spent grains can be thermally recycled without auxiliary firing, i.e. burned or can be gassed.
  • the gas produced in the gasification is advantageously used for energy, preferably as Energy sources for steam generation in the brewery network, e.g. as additional gas to natural gas, so that it is energetically burned by the boiler system in the brewery can be used.
  • An additional one is preferably used for mechanical pre-drying of the spent grains Drying to remove capillary water using electrical fields or with Helped by high frequency fields.
  • the mechanical predrying is advantageously carried out to at least 65, preferably at least 62 mass% water content.
  • the thermal drying of the spent grains takes place advantageously on their self-firing permitting water content, preferably to at least 55 mass% water content.
  • the mechanical predrying Pressed water formed is processed anaerobically and the resulting methane-containing gas used energetically, preferably as an energy source for steam generation in the Brewery association used.
  • Exhaust gases produced when the dried beer spent grains are burned become inexpensive disposed of together with waste gases formed in a steam boiler of the brewery.
  • mixtures of beer spent grains and other organic, biogenic waste thermally recycled.
  • a system for carrying out the process with a beer spent grains a first Drying stage forming mechanical dryer and with one for mechanical dewatered spent grains a further drying stage forming thermal dryer as well with a device for thermal recovery by burning or gasifying the dried beer spent grains, is characterized in that in the thermal dryer Flue gas leading from a steam boiler of the brewery energy association leads out.
  • the device for thermal recycling of the beer spent grains preferably has one Combustion boiler on, where appropriate the combustion boiler with a Steam generating device is equipped and the steam generating device is advantageous is linked to the brewery's energy network.
  • a flue gas discharge from the combustion boiler ends up saving investment an exhaust system of a beer production system, where appropriate an exhaust pipe from thermal dryer also opens into the exhaust system of the beer production system.
  • the device for thermal Recycling a gasification device where appropriate one of the Gasification device outgoing and leading in the gasifier generated gases discharging line a burner of a steam boiler of the brewery's energy network.
  • the mechanical dryer can preferably be used as a belt press or as a screw press be trained.
  • a convection dryer is useful as a thermal dryer.
  • the thermal dryer preferably has one that can be operated with solar energy Drying facility.
  • the thermal drying, the Gasification and combustion combined in one apparatus, whereby expediently a the hot exhaust gases from the thermal drying, gasification and the device having the combustion discharge line directly to the steam boiler of the brewery's energy consumer.
  • the thermal drying can be operated with a solar energy Drying facility to be expanded.
  • FIGS. 1 and 2 each a process diagram illustrate according to a variant.
  • a thermal dryer 6 for this purpose, which is a drum dryer is provided.
  • This drum dryer 6 is directly connected via line 7 supplied flue gas heated by an installed in a beer production plant 8
  • Boiler 10 dates.
  • the boiler 10 is supplied with natural gas, which is supplied via line 9, heated; the steam-carrying pipes are designated 11. Part of the flue gas can via a branch line 12 directly to an exhaust fan 13 of the flue gas disposal system be fed. This also leads to the flue gas disposal system Drum dryer 6 outgoing flue gas discharge 14.
  • the water content can be reduced to below 55% by mass lower so that the spent grains 15 after ignition, i.e. without support firing, burn.
  • the dried beer spent grains 15 are burned in a burner 16 in one Combustion boiler 17 in which a steam generating device 18 is installed.
  • the in this steam generating device 18 steam is usefully for the Beer production, i.e. that natural gas-fired for the natural gas burner 19 Boiler 10 can be saved.
  • the ash discharge is designated 20.
  • the wet beer spent grains 1 are first in a first drying stage 2 by means of a belt press 21 of a mechanical Subjected to drying. Then the mechanically dewatered spent grains are used as Convection dryer 22 designed thermal dryer of the second drying stage 4th supplied, in which the spent beer 5 as well as shown in FIG. 1 with flue gas, which from a Beer production plant 8 comes to a water content below the self-burning limit be dried.
  • the thermal utilization of the dry beer spent grains 15 takes place according to FIG. 2 in one Carburetor 23, the oxygen or an oxygen-containing gas via a sieve plate 24, such as Air.
  • 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.
  • thermal drying can also in addition to mechanical and thermal drying, other drying processes can be used, for example drying with the help of high-frequency fields or electromagnetic fields.
  • thermal drying can also natural energy, such as solar energy, are used, with solar energy before or is fed after the thermal drying stage 4 - depending on the dew point of the flue gas.
  • 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.
  • a combustible gas containing methane is obtained.
  • Approx. 36,400 m 3 biogas / a is produced from the amount of press water mentioned.
  • the combustion of this gas, which contains 85% methane, produces about 300,000 kWh / a; this results in additional proceeds.
  • the water content of the spent grains 5 after the mechanical drying is about 62% by mass. To ensure self-flammability, a value of 55% by mass of water should be achieved.
  • a thermal one is then used Drying carried out to a greater or lesser extent to increase the degree of self-firing to reach.
  • the mechanically and alternatively pre-dried beer spent grains 5 are over a Buffer tank continuously in a directly heated dryer (e.g. drum dryer 6) promoted and with the 140 to 160 ° C hot flue gases from natural gas combustion convective path to at least the self-firing degree of approx. 55 mass% water dried.
  • a directly heated dryer e.g. drum dryer 6
  • 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 invention is not limited to the examples described above, but can be found in be modified in various ways. So the drying of the wet beer spent grains with any number of drying stages can be accomplished, but at least one is essential mechanical drying level 2 and at least one thermal drying level 4. Furthermore are combined equipment versions on thermal predrying, gasification and Combustion possible, which also meet the criteria listed above.
  • the method according to the invention can be expanded in addition to the beer spent grains other biogenic wastes, such as sewage sludge, are also included in the process To increase energy content and thus the production of steam. Treatment of the Mixing of spent grains and other biogenic waste takes place in the same way as in the process description explained.

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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)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Fertilizers (AREA)
  • Alcoholic Beverages (AREA)
  • Cereal-Derived Products (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
EP97911953A 1996-11-20 1997-11-18 Verfahren und anlage zum thermischen verwerten von biertrebern Expired - Lifetime EP1007884B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
AT0202296A AT404253B (de) 1996-11-20 1996-11-20 Verfahren zum thermischen verwerten von biertrebern
AT202296 1996-11-20
PCT/AT1997/000250 WO1998022751A1 (de) 1996-11-20 1997-11-18 Verfahren zum thermischen verwerten von biertrebern

Publications (2)

Publication Number Publication Date
EP1007884A1 EP1007884A1 (de) 2000-06-14
EP1007884B1 true EP1007884B1 (de) 2001-12-19

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EP97911953A Expired - Lifetime EP1007884B1 (de) 1996-11-20 1997-11-18 Verfahren und anlage zum thermischen verwerten von biertrebern

Country Status (20)

Country Link
US (1) US6167636B1 (xx)
EP (1) EP1007884B1 (xx)
JP (1) JP3963481B2 (xx)
KR (1) KR100502965B1 (xx)
CN (1) CN1135322C (xx)
AT (2) AT404253B (xx)
AU (1) AU4934397A (xx)
BG (1) BG63514B1 (xx)
BR (1) BR9713369A (xx)
DE (1) DE59705928D1 (xx)
DK (1) DK1007884T3 (xx)
ES (1) ES2170376T3 (xx)
HU (1) HU226171B1 (xx)
ID (1) ID22287A (xx)
PL (1) PL188043B1 (xx)
PT (1) PT1007884E (xx)
RO (1) RO118680B1 (xx)
SI (1) SI20034A (xx)
TR (1) TR199901798T2 (xx)
WO (1) WO1998022751A1 (xx)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2136138A2 (de) 2008-06-18 2009-12-23 Gea Brewery Systems Gmbh Sudhausanlage mit Filtrationseinrichtung und Verfahren zur thermischen Verwertung von feuchten Filtrationspartikeln
EP2253693A1 (de) 2009-05-18 2010-11-24 Ziemann Energy GmbH Verfahren zum Behandeln von Reststoffen von Brauereien
EP2292726A1 (de) 2009-08-07 2011-03-09 Marcus Hertel Bierbereitungsverfahren sowie zugehörige Vorrichtung
DE102013107985A1 (de) * 2013-07-25 2015-01-29 Kotyk Energy Ag Vorrichtung zur Erzeugung für Energie aus Biomasse und Verfahren zur Energiegewinnung aus Biomasse

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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
CN101970620A (zh) * 2008-02-18 2011-02-09 栗山真辅 固体燃料及固体燃料的制造方法
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
DE102010015039A1 (de) 2010-04-15 2013-01-31 Ziemann Energy Gmbh Verbrennungsanlage für Nasstreber und dergleichen
US10364400B2 (en) * 2011-09-01 2019-07-30 Akbev Group, Llc Spent grain fuel product and process
US11866669B2 (en) 2011-09-01 2024-01-09 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
US10781388B2 (en) 2011-09-01 2020-09-22 Akbev Group, Llc High protein organic materials as fuel and processes for making the same
US10982162B2 (en) 2011-09-01 2021-04-20 Akbev Group, Llc High protein organic materials as fuel and processes for making the same
US11441090B2 (en) 2011-09-01 2022-09-13 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
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
CA3130900C (en) 2012-12-28 2023-06-20 Thomas Brown Methods for making spent grain alcoholic and dough-based products
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
FI3532569T3 (fi) * 2016-10-28 2023-01-13 Menetelmä runsasproteiinisten orgaanisten polttoaineiden valmistamiseksi
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
RU2719508C1 (ru) 2019-10-21 2020-04-20 Общество с ограниченной ответственностью "БиоВи" (ООО "БиоВи") Белковая суспензия из пивной дробины, способ и установка для ее получения
RU2730134C1 (ru) 2020-04-02 2020-08-18 Общество с ограниченной ответственностью "БиоВи" (ООО "БиоВи") Белковый продукт из пивной дробины и способ его получения
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

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2136138A2 (de) 2008-06-18 2009-12-23 Gea Brewery Systems Gmbh Sudhausanlage mit Filtrationseinrichtung und Verfahren zur thermischen Verwertung von feuchten Filtrationspartikeln
DE102008028600A1 (de) 2008-06-18 2009-12-31 Gea Brewery Systems Gmbh Sudhausanlage mit Filtrationseinrichtung und Verfahren zur thermischen Verwertung von feuchten Filtrationspartikeln
EP2136138A3 (de) * 2008-06-18 2012-06-06 Gea Brewery Systems Gmbh Sudhausanlage mit Filtrationseinrichtung und Verfahren zur thermischen Verwertung von feuchten Filtrationspartikeln
EP2253693A1 (de) 2009-05-18 2010-11-24 Ziemann Energy GmbH Verfahren zum Behandeln von Reststoffen von Brauereien
DE102009021692A1 (de) 2009-05-18 2010-12-02 Ziemann Energy Gmbh Verfahren zum Behandeln von Reststoffen von Brauereien
EP2292726A1 (de) 2009-08-07 2011-03-09 Marcus Hertel Bierbereitungsverfahren sowie zugehörige Vorrichtung
DE102010033664A1 (de) 2009-08-07 2011-04-21 Hertel, Marcus, Dr.-Ing. Bierbereitungsverfahren sowie zugehörige Vorrichtung
EP2975109A1 (de) 2009-08-07 2016-01-20 Hertel, Katja Isabel Bearbeitungsverfahren sowie zugehörige vorrichtung
DE102013107985A1 (de) * 2013-07-25 2015-01-29 Kotyk Energy Ag Vorrichtung zur Erzeugung für Energie aus Biomasse und Verfahren zur Energiegewinnung aus Biomasse

Also Published As

Publication number Publication date
BR9713369A (pt) 2000-01-25
PL188043B1 (pl) 2004-11-30
ATA202296A (de) 1998-02-15
ES2170376T3 (es) 2002-08-01
SI20034A (sl) 2000-02-29
DK1007884T3 (da) 2002-04-15
EP1007884A1 (de) 2000-06-14
HU226171B1 (en) 2008-05-28
BG103481A (en) 2000-03-31
JP3963481B2 (ja) 2007-08-22
US6167636B1 (en) 2001-01-02
WO1998022751A1 (de) 1998-05-28
HUP0000151A2 (hu) 2000-06-28
RO118680B1 (ro) 2003-08-29
AU4934397A (en) 1998-06-10
CN1135322C (zh) 2004-01-21
DE59705928D1 (de) 2002-01-31
JP2001504205A (ja) 2001-03-27
BG63514B1 (bg) 2002-03-29
KR100502965B1 (ko) 2005-07-25
PT1007884E (pt) 2002-05-31
TR199901798T2 (xx) 1999-10-21
ID22287A (id) 1999-09-30
KR20000069062A (ko) 2000-11-25
CN1244908A (zh) 2000-02-16
HUP0000151A3 (en) 2000-11-28
AT404253B (de) 1998-10-27
ATE211238T1 (de) 2002-01-15

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