Davyhulme,UK
| 91,000 tonnes DS/year |
Doubling of capacity of existing 8 x 7400 m³ digesters
|
|
4x5 reactor Cambi THP + cooler system
|
10 MW electricity + THP steam
|
|
Pasteurized product
|
Reduced energy for drying and incineration
|
|
Carbon emissions reduced by 32,000t CO2 equivalents/year
|
High performance digestion
|
|
High dry solids final product
|
Maximized VS reduction
|
[more]
Vilnius, Lithuania
| Timeline/Hand over: Beginning of 2010 |
Capacity: 23,000 tonnes of DS/year |
| Raw material: Mixed primary and secondary sludge, some imports |
Biogas utilization: Combined heat & power (CHP) and low- temp. drying |
| Biosolids utilization: Dewatered and dried cake to agriculture |
Digestion: 3 x 3700m³ digesters, incl. Cambi fin-fan coolers
|
[more]
Afan, UK
| • 25.000 metric tonnes DS/year |
• 2 x 4000 m³ digesters transport |
| • 4-reactor Cambi THP + coolers |
• 2.1 MW electricity + cogen steam |
| • Pasteurized product |
• Reduced energy for drying |
| • Significantly less carbon emissions |
• High performance digestion |
| • Final product > 30%DS |
• Maximized VS destruction |
[more]
Cardiff, UK
| • 35.000 metric tonnes DS/year |
• 2 x 7.500 m³ digesters |
| • 2 x 3-reactor Cambi THP + coolers |
• 3.2 MW electricity + cogen steam |
| • Pasteurized product |
• Reduced energy for drying |
| • Significantly less carbon emissions |
• High performance digestion |
| • Final product > 30% DS |
• Maximized VS destruction |
[more]
Aberdeen, UK
Plant capacity and performance:
| • Treats 16,500 metric tonnes DS/year |
• Final product: > 32% DS |
| • 2 x 4,000 m³ digesters |
• Digester loading: Twice the conventional |
| • 1 MWe + steam cogen |
• < 20,000 Tonnes pasteurized product for grassland |
| • 4-reactor Cambi THP + coolers |
|
[more]
Whitlingham,UK
Plant capacity and expected performance:
| • 20,000 metric tonnes DS/year |
• Doubled digester loading |
| • 2 x 4000m³ digesters |
• Doubled biogas production |
| • 4-reactor Cambi THP+coolers |
• Class A pasteurized cake |
| • Extra 1.5 MW green electricity |
• Avoiding lime operations |
[more]
Dublin, IRL
Plant capacity and performance:
| • 36,000 metric tonnes DS/year |
• Digester loading 6 kg VS/m3/day, 2-3 x conventional |
| • 3 x 4,300 m³ digesters |
• ~10% DS feed to digesters |
| • Cogen: 4 MWe + steam |
• >60 % VS reduction |
| • 2x4 reactor Cambi THP+coolers |
• High dry solids Class A cake |
[more]
Bydgoszcz, PL
Plant capacity and performance:
| • 7,500 m³/day biogas |
• 10 % DS feed to digestion |
| • 7,650 metric tonnes DS/year |
• 2 reactor Cambi THP |
| • 2 x 3,800 m³ digesters |
• >57% VS destruction |
| • 2 x 529 kWe cogeneration |
• Pasteurized and odour-free cake |
| • Final product: 31-33% DS |
|
[more]
Turku, FIN
Plant capacity and expected performance:
| • 14,000 metric tonnes DS/year |
• Pasteurized cake |
| • High dry solids loading (>10%DS) |
• High biogas production |
| • 2 x 3,500 m3 digester volume |
|
[more]
Milton Keynes, UK
Plant capacity and performance:
| • 22,240 metric tonnes DS/year |
• Doubling digestion throughput |
| • 2 x 3,750 m³ digesters |
• Class A pasteurized product |
| • 4-reactor Cambi THP + coolers |
• Increased sludge dewaterability |
| • +1 MWe and process steam |
• Importing sludge avoids investments elsewhere |
[more]
Brussels, B
Plant capacity and performance:
| • 20,000 metric tonnes DS/year |
• Digested sludge to wet oxidation at ~8% DS |
| • 2 x 3,600 m³ digesters |
• Compact digestion with high biogas yields |
| • Dewatering >35% DS in filter press |
• 5-reactor Cambi THP |
[more]
Tees valley, UK
Plant capacity and expected performance:
| • 40,000 metric tonnes DS/year |
• Reduced energy for drying and transport |
| • 3 x 6,300 m³ digesters |
• 50,000 tons less carbon emissions |
| • 8-reactor Cambi THP + coolers |
• High performance digestion |
| • 4.7 MW electricity + cogen steam |
• Half the original cake volume |
| • Pasteurized product |
|
[more]
Geiselbullach, D
Plant capacity and expected performance:
| • 2,000 metric tonnes DS/year (secondary sludge only) |
• Increased biogas production |
| • 2 x 3,000 m³ digesters |
• Improved sludge dewaterability |
|
• Continuous Cambi THP
|
|
[more]
Hamar, N
Plant capacity and performance:
| • 3,600 metric tonnes DS/year |
• ~65% volatile solids reduction |
| • 2 x 1,300 m³ digesters |
• Half the original cake volume |
| • X kW electricity + steam |
• Meets highest biosolids standards |
|
• 2-reactor Cambi THP
|
|
[more]
Chertsey, UK
Plant capacity and performance:
| • 9,600 metric tonnes DS/year |
• ~ 3 times increased digester throughput |
| • 2 x 1,600 m³ digesters |
• Class A product |
| • 1.2 MWe (planned) |
• 99% availability on planned operations |
| • 2-reactor Cambi THP |
• >60% VS destruction |
[more]
Nęstved, DK
Plant capacity and performance:
| • 1,600 metric tonnes DS/year |
• Before Cambi 18% DS, aften 30% DS biosolids |
| • Bio-sludge (extended aeration) |
• Biosolids reduction by 50% |
| • 2,000 m³ digester |
• > 50% more biogas |
[more]
Sarpsborg, N
Plant capacity and performance:
| • 4,000 metric tonnes DS/year |
• Eliminating chemical hydrolysis |
| • 1 x 4,000 m³ digester |
• Increased biogas production |
| • Continuous Cambi THP |
• Reduced return load toWWTP |
[more]
Fredericia, DK
Plant capacity and performance:
| • 8,000 metric tonnes DS/year |
• 30 % DS dewatered cake |
| • 2 x 2,000 m³ digesters |
• Pasteurized cake with >40% vol. reduction |
| • 2-reactor Cambi THP |
• Doubling of biogas production |
| • Cogen: Electricity + steam |
• Doubling of digester loading |
[more]
Nagaoka, JP
Plant capacity and performance:
| • 1,200 metric tonnes DS/year |
• Increased biogas production |
| • 1,590 m³ digesters |
• Better dewatered biosolids |
| • Pasteurized cake |
|
[more]
Brisbane, AUS
Plant capacity and performance:
| • 12,900 tonnes DS/year |
• 1,000 kW electricity |
| • 13,500 m³/day biogas |
• 43 % DS reduction |
| • Final product: 30% DS |
• >50% VS destruction |
[more]
|
