Challenges & Opportunities
- f pre-treatment for AD Plants
Challenges & Opportunities of pre-treatment for AD Plants Mike - - PowerPoint PPT Presentation
Challenges & Opportunities of pre-treatment for AD Plants Mike Bullard Managing Director, UTS Biogas Ltd Contents Introduction to UTS/Anaergia pre-treatment agricultural systems In contrast to pre-treatment SSO
Biogas plant May Farm, Ely, Cambs Biogas plant Dagenham, London
Manure/grass Biogas plant, Yorkshire
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streams
anaerobic digestion core
DBOO (including financing)
the UK and Ireland (UK based technical and project management)
production and utilisation; digestate management. CHP and BtG. EPC
Organics Pre-treatment Core Technology Post Treatment
Organics Extrusion DB Technologies Recyclable Recovery DB Technologies Solids Separation Anaergia / UTS Hydraulic Mixing Anaergia / UTS Service Box Anaergia / UTS Materials Handling Anaergia / UTS Residuals Drying Therma-Flite (Exclusive Partner) Membranes Fibracast (Subsidiary) Gasification KIV (Exclusive Partner) Biogas Upgrading Greenlane (Partner) Anaerobic Digesters Anaergia / UTS
Primary Fermenters Secondary Fermenters Digestate Storage Tank CHP Area Pasteurisers & Separator
Incoming Solid Feed Weighbridg e Conditioning Feed hopper Output-Fibre Separated Solid Digestate Separator Digestate Storage Tank Buffer Tank Batch pasteurisatio n Maceration Output Liquid digestate Primary Fermenter Secondary Fermenter CHP Output Electricity Output Heat Desulphurisatio n Conditioning
Incoming Solid Weighbridge Conditioning Feed hopper Output-Fibre Separated Solid Digestate Separator Digestate Storage Tank Output Liquid digestate Fermenter CHP Output Electricity Output Heat Desulphurisation Incoming Liquid Receptio n tank Stone Trap
Composting building
Incoming Waste Weighbridg e Reception building Biowaste Preparation equipment Output-Fibre Hall Separated Solid Digestate Separator Digestate Storage Tank Buffer Tank Batch pasteurisatio n Maceration Output Liquid digestate Receptio n tank Primary Fermenter Secondary Fermenter CHP Output Electricity Output Heat Desulphurisatio n
Process design parameter Unit Value Solid concentration organic fraction % of wet 25 – 35 Volatile solids organic fraction % of dry 85 – 95 Solid concentration input digester % of wet 25 - 30 Solid concentration output digester % of wet 10 - 15 Organic loading digester kg VS/(m3*d) 6.5 – 8 Hydraulic retention time (HRT) digester Days 40-60 Specific biogas production Nm3/t VS 680 – 750 Specific biogas production Nm3/t wet 130 – 150 Contamination levels % (w/w) 3-25%
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(glass, plastic)
‘contaminted‘ with glass, plastic
as more water is required to process the SSO
Grit and plastic separation systems are required if highly contaminated SSO is treated
size = greater costs
with high green waste content
reduce moisture content
wastes
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Mike Bullard Mike.bullard@uts-biogas.com 0044 1480 477608