Energy efficient biogas upgrading by anaerobic hydrolysis
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1 Engineering Conferences International ECI Digital Archives BioEnergy IV: Innovations in Biomass Conversion for Heat, Power, Fuels and Chemicals Proceedings Spring Energy efficient biogas upgrading by anaerobic hydrolysis Rolf Jung Fraunhofer UMSICHT Follow this and additional works at: Part of the Chemical Engineering Commons Recommended Citation Rolf Jung, "Energy efficient biogas upgrading by anaerobic hydrolysis" in "BioEnergy IV: Innovations in Biomass Conversion for Heat, Power, Fuels and Chemicals", Manuel Garcia-Perez,Washington State University, USA Dietrich Meier, Thünen Institute of Wood Research, Germany Raffaella Ocone, Heriot-Watt University, United Kingdom Paul de Wild, Biomass & Energy Efficiency, ECN, The Netherlands Eds, ECI Symposium Series, (2013). This Conference Proceeding is brought to you for free and open access by the Proceedings at ECI Digital Archives. It has been accepted for inclusion in BioEnergy IV: Innovations in Biomass Conversion for Heat, Power, Fuels and Chemicals by an authorized administrator of ECI Digital Archives. For more information, please contact
2 Energy efficient biogas upgrading by anaerobic hydrolysis Engineering Conferences International BioEnergy IV: Innovations in Biomass Conversion for Heat & Power, Fuels and Chemicals June 9-14, 2013 Basiliani Resort, Otranto, Italy Rolf Jung Fraunhofer UMSICHT, Institute branch Sulzbach-Rosenberg Folie 1
3 Our motivation Energy conversion and storage Raw and functional materials Folie 2
4 AGENDA Introduction Background Materials and Methods Results and Discussion Conclusions Fraunhofer
5 INTRODUCTION Fraunhofer
6 Introduction Motivation Strong growth of biogas plants Biomethane can be stored or fed into the public natural gas grid Efficient energy usage via public grid Biogas upgrading is an energy intensive process Carbon dioxide reduction before biogas upgrade increase efficiency and decline costs Folie 5
7 BACKGROUND Fraunhofer
8 Methane step Hydrolysis step Background Anaerobic process steps ph-value acidic ph-value neutral Folie 7
9 Background One-phase and two-phase digestion CO 2 CH 4 CO 2 H 2 CO 2 CH 4 Biogas (50-55 Vol.-% CH 4 ) CO 2 -rich Hydrolysis gas Biogas (60-70 Vol.-% CH 4 ) Input Substrate Input Substrate Digestate Digestate Hydrolysis Methane reactor One-phase digestion Two-phase digestion Folie 8
10 Background Process key parameters for hydrolysis step Hydraulic retention time (HRT) Temperature ph-value Organic loading rate Folie 9
11 MATERIALS AND METHODS Fraunhofer
12 Materials and methods Experimental setup (1) Input (2) Reactor (3) Stirrer (4) ph value (5) Gas outlet Hydrolysis reactor V R = 22 l (6) Output Methane reactors V R = 45 l Folie 11
13 Materials and methods Experimental parameters One-phase digestion Two-phase digestion Substrate: maize silage Temperature: 39 C Retention time: 20 d Organic loading rate: 1 kg odm /(m 3 d) Substrate: maize silage Temperature: 39 C Hydrolysis phase: Retention time: 5 d Organic loading rate: 38 kg odm /(m 3 d) Digestion phase: Retention time: 15 d Organic loading rate: 3 kg odm /(m 3 d) Folie 12
14 RESULTS AND DISCUSSION Fraunhofer
15 Results and discussion experimental trials carbon mass balance One-phase digestion Two-phase digestion vol.% CH vol.% CH 4 Folie 14
16 Results and discussion Comparison of energy yield gas Folie 15
17 CONCLUSIONS Fraunhofer
18 Conclusions Assets and drawbacks One-phase digestion Two-phase digestion PSA PSA Increase of methane concentration Lower energy costs for biogas upgrading Higher investment costs Energy loss by hydrolysis gas (H 2 ) P P!! Folie 17
19 Conclusions Outlook Comparison of power consumption for biogas upgrade Energy saving Folie 18
20 Energy efficient biogas upgrading by anaerobic hydrolysis Contact: Thank you very much! Dipl.-Ing. (FH) Rolf Jung recycling management Funded by Fraunhofer UMSICHT Institute branch Sulzbach-Rosenberg An der Maxhütte Sulzbach-Rosenberg Telefon: rolf.jung@umsicht.fraunhofer.de Internet: Folie 19
21 Energy efficient biogas upgrading by anaerobic hydrolysis Contact: Thank you very much! Dipl.-Ing. recycling management Funded by Fraunhofer UMSICHT Institute branch Sulzbach-Rosenberg An der Maxhütte Sulzbach-Rosenberg Telefon: rolf.jung@umsicht.fraunhofer.de Internet: Folie 20
22 Material and methods Carbon mass balance Carbon (CO 2 ) hydrolysis gas Carbon (CH 4, CO 2 ) biogas Carbon (TOC) Input substrate Carbon (TOC) Output hydrolysis Carbon (TOC) Output digester Hydrolysis Methane step Folie 21
23 Material and methods ph and activity microorganism Hydrolysis Methane step Folie 22
24 Conclusions xxx Estimated cost of biogas upgrading using different technologies (Urban et al.2008). Folie 23
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