Coordinatore | BIOENERGY 2020+ GMBH
Organization address
address: INFFELDGASSE 21B contact info |
Nazionalità Coordinatore | Austria [AT] |
Totale costo | 1˙046˙544 € |
EC contributo | 712˙000 € |
Programma | FP7-SME
Specific Programme "Capacities": Research for the benefit of SMEs |
Code Call | FP7-SME-2012 |
Funding Scheme | BSG-SME |
Anno di inizio | 2012 |
Periodo (anno-mese-giorno) | 2012-11-01 - 2014-12-31 |
# | ||||
---|---|---|---|---|
1 |
BIOENERGY 2020+ GMBH
Organization address
address: INFFELDGASSE 21B contact info |
AT (GRAZ) | coordinator | 32˙800.00 |
2 |
ATRES
Organization address
address: LISA MEITNER STRASSE 30 contact info |
DE (FREISING) | participant | 327˙213.00 |
3 |
ING. AIGNER WASSER-WAERME-UMWELT GMBH
Organization address
address: KREMSTALSTARSSE 18 contact info |
AT (NEUHOFEN AN DER KREMS) | participant | 167˙185.00 |
4 |
S&H UMWELTENGINEERING VERTRIEBS GMBH
Organization address
address: SCHWANEBECKER WEG 1 contact info |
DE (NAUEN OT NEUKAMMER) | participant | 86˙842.00 |
5 |
WADI-BRAU-HUUS AG
Organization address
address: FLORHOFSTRASSE 13 contact info |
CH (WADENSWIL) | participant | 51˙860.00 |
6 |
UNIVERSITAET FUER BODENKULTUR WIEN
Organization address
address: Gregor Mendel Strasse 33 contact info |
AT (WIEN) | participant | 39˙200.00 |
7 |
AAT ABWASSER- UND ABFALLTECHNIK GMBH
Organization address
address: KONRAD-DOPPELMAYR-STRASSE 17 contact info |
AT (WOLFURT) | participant | 6˙900.00 |
8 |
UNERTL WEISSBIER GMBH
Organization address
address: LERCHENBERGER STRASSE 6 contact info |
DE (HAAG) | participant | 0.00 |
Esplora la "nuvola delle parole (Word Cloud) per avere un'idea di massima del progetto.
'The aim of the project is the development of a thermochemical pre-treatment technology to increase the gas yield of brewers spent grains during an anaerobic digestion process. Thermochemical pre-treatment will be realised in a pressure vessel by addition of sulphuric acid. Pre-treatment of organic biomass will lead to a break down of the complex lignocellulose structure and release oligomeric/monomeric carbohydrate units which will then be better available for degradation by anaerobic digestion. This leads to improved utilization of the substrate and to a higher gas yield per tonne substrate inserted. After the pre-treatment the hydrolysate is digested in multi-stage biogas system. During anaerobic digestion H2S is formed out of sulphur containing compounds of the substrate by the anaerobic and facultative anaerobic bacteria. H2S is volatile and will be found in the biogas. Because of the fact that sulphuric acid is used in the pretreatment step, the H2S concentrations in the biogas will be increased. A clean up of the biogas is in all cases inevitable before feed in into e.g. a gas engine. The gas cleaning will be realised by using a trickle bed system. Here H2S will be converted into H2SO4 by microbiological desulphurisation process. The H2SO4 solution can be recovered for the thermochemical pre-treatment process. After lab scale investigation, a demonstration plant will be constructed and the process will be evaluated at two different breweries. For further application TherChem process will be tested on 5 different substrates in lab scale.'
Optimal digestion of brewery waste