Cambi THP - Psyttalia wwtp. Davide Perduca

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1 Cambi THP - Psyttalia wwtp Davide Perduca

2 CAMBI IN BRIEF Independent Norwegian technology & engineering company since 1989 Designs, builds & operates the CAMBI Thermal Hydrolysis Process (THP) A pre-treatment technology before anaerobic digestion of sewage sludge Optimizes digestion and dewatering, reduces digester volume, increases gas production Delivers a high quality (Class A) end product (biosolids) First installation in 1996, still in operation 44 plants for > t dry solids/year Typical WWTP size : to 10 Million People Equivalent!Cambi THP is a key technology for any sludge disposal strategy!

3 CAMBI S BUSINESS AREAS Biosolids: Plants for enhanced biogas production from municipal & industrial sludge Biowaste: Plants for biogas fertilizer from source-separated organic waste Operations: Cambi Operations provides support and operation services to maximize plant performance

4 THE CHALLENGE OF SLUDGE AND BIOWASTE Overloaded digesters? Biological sludge difficult to dewater? Quality/Class A requirements? High disposal costs? Odour? Waste and wastewater management does not come for free!

5 CAMBI THP - BENEFITS

6 CAMBI THP

7 CAMBI PLANT LOCATIONS

8 1,200 1, tones dry solids/year) CAMBI PLANTS ( , contracted) New Capacity Online, DTPY Cumulative Capacity, DTPY

9 CAMBI PLANTS (in operation, metric tons) Customer/project Location Country Design capacity (TDS/year) TPH type 1 Joint venture betw een Galliford Try Infrastructure Ltd, MWH Treatment Ltd and Mott McDonald Ltd. THP reactors TYPE Completed no. of plants HIAS (1) Hamar Norway 3,600 tonnes B10 1 WWTP F A Thames Water (2) Chertsey UK 9,600 tonnes B12 2 WWTP F A Borregaard Industries Sarspborg Norway 4,000 tonnes B12 1 PAPER W I The Municipality of Næstved Næstved Denmark 1,600 tonnes B6 1 WWTP* W A Nigg Bay Aberdeen UK 16,500 tonnes B12 4 WWTP F A Mjosanlegget, Biowaste Plant*** Lillehammer Norway 4,600 tonnes B12 2 OFMSW B A Ringsend Sewage Treatment Works Dublin Ireland 36,000 tonnes B12 8 WWTP F D, A The Municipality of Fredericia Fredericia Denmark 8,000 tonnes B12 2 WWTP F A Kobelco Eco-Solutions Niigata Japan 1,200 tonnes B3 1 WWTP F A Spolka Wodna Kapusciska Bydgoszcz Poland 8,000 tonnes B12 2 WWTP F A Thames Water Chertsey UK Included in (2) B12 0 Operations Part of 2 F A HIAS, additional digester Hamar Norway Included in (1) B12 0 New digester 2005 Expanding 1 F A Oxley Creek Brisbane Australia 12,900 tonnes B12 3 WWTP W A Bruxelles Nord Bruxelles Belgium 20,000 tonnes B12 5 WWTP W O HIAS- Expansion Hamar Norway 2,000 tonnes B12 1 WWTP 2007 Expanding 1 F A Cotton Valley (Anglian Water) Milton Keynes UK 20,000 tonnes B12 4 WWTP F A Ecopro, multi-waste** plant Verdal Norway 8,000 tonnes B12 2 OFMSW*** B + F A Whitlingham WWTW (Anglian Water) Norwich UK 19,000 tonnes B12 4 WWTP F A Biovakka Oy Åbo/Turku Finland 14,000 tonnes B12 3 WWTP F A Nigg Bay, upgrade Aberdeen UK 4,000 tonnes B12 0 WWTP 2009 Expanding 5 F A Bran Sands (Aker-Kværner/NWL) Tees Valley UK 37,000 tonnes B12 8 WWTP F A Amperverband, Cambi THP-C* Geiselbullach Germany 2,000 tonnes B12 1 WWTP H I Ringsend STW (New THP line) Dublin Ireland 20,000 tonnes B12 4 WWTP 2010 Expanding 7 F D, A Cardiff, Welsh Water (Imtech) Wales UK 30,000 tonnes B12 6 WWTP W A Afan, Welsh Water (Imtech) Wales UK 20,000 tonnes B12 4 WWTP F A Riverside, Thames W (Interserve) London UK 40,000 tonnes B12 8 WWTP F A Vilniaus Vandenys/ Vilnius Water Co. Vilnius Lithuania 23,000 tonnes B12 5 WWTP F D, A Mapocho WWTP (Degremont)* Santiago Chile 25,000 tonnes B12 6 WWTP H A Lindum, Cambi Compact Drammen Norway 6,000 tonnes B6 2 WWTP F A Davyhulme, UU (B&V) Manchester UK 91,000 tonnes B12 20 WWTP F A, I Howdon (Imtech/NWL) Newcastle UK 40,000 tonnes B12 8 WWTP F A Oslo EGE*** Oslo Norway 15,000 tonnes B12 2 OFMSW*** B A Crawley STW upgrade (GBM 1 ) West Sussex UK 11,300 tonnes B6 3 WWTP F A Crossness, Thames Water London UK 36,500 tonnes B12 6 WWTP W A, I 1 Joint venture betw een Galliford Try Infrastructure Ltd, MWH Treatment Ltd and Mott McDonald Ltd. Application Product end-use

10 CAMBI PLANTS (in design/construction, metric tons) Customer/project Location Country Ordered Plants / Under design/construction Design capacity (TDS/year) TPH type THP reactors TYPE Completed no. of plants Application DC Water Washington DC USA 130,000 tonnes B12 24 WWTP F A Heijmans, STC Tilburg Tilburg Netherlands 29,000 tonnes B12 3 WWTP F I Beckton, Thames Water London UK 36,500 tonnes B6 6 WWTP W A, I Sundet WWTP, Växjö Municipality** Växjö Sweden 8,600 tonnes B6 2 WWTP F A Vigo WWTP (UTE EDAR Lagares) Vigo Spain 22,000 tonnes B6 3 WWTP F A IVAR biogas plant** Stavanger Norway 11,800 tonnes B6 2 WWTP F A Seafield STW, MWH (Stirling Water) Edinburgh Scotland 27,000 tonnes B6 6 WWTP F A Long Reach, Aecom (T. Water)* Kent, London UK 13,000 tonnes B6 3 WWTP W A Burgos WWTP (Degremont) Burgos, Castile Spain 13,000 tonnes B6 2 WWTP F A Ourense WWTP (Degremont) Ourense, Galicia Spain 7,000 tonnes B2 4 WWTP F A Mjosanlegget*** New Plant Lillehammer Norway 4,800 tonnes B6 2 WWTP F A Bakdal WWTP* Anyang S. Korea 27,700 tonnes B12 4 WWTP F D, I Psyttalia WWTP* Athens Greece 15,500 tonnes B6 4 WWTP W A Hengelo* Hengelo Netherlands 11,100 tonnes B6 2 WWTP W I Gaobeidian WWTP Beijing China 99,100 tonnes B12 20 WWTP F A TDS = Total dry solids (1000 kg = 1 tonne) Total: 1,045,900 tonnes 216 Pop. Equiv. 35,818,000 Product end-use WWTP = sludge from muncipal w astew ater treatment plant, *biological sludge/was only mixed w ith untreated primary sludge before AD PAPER = bio-sludge/waste activated sludge from paper factory wastewater treatment plant *** OFMSW = Organic Fraction of Municipal Solid Waste, **Codigestion: mix of sludge, OFMSW, and other organic waste Applications: H: Cambi Hybrid (WAS only TH mixed with untreated P), not Class A W: WAS, biological sludge, only (usually extended aeration) F: Full Cambi, TH of both P and WAS sludge, Class A B: Biowaste O: Wet-air oxidation In operations: Under design/construction: Total: Product end-use: A: Use of end product in agriculture D: Drying of end-product I: Incineration of end-product 589,800 tonnes 456,100 tonnes 1,045,900 tonnes

11 CAMBI REFERENCE LIST, BIOWASTE AND CODIGESTION (metric) CAMBI REFERENCE LIST, BIOWASTE AND CODIGESTION Customer/project Location Design capacity (TDS/year) Design capacity (wet t/year) Approx t raw Sludge (a.r.) OFMSW tons (a.r.) TYPE Completed Product end-use Mjosanlegget, Biowaste Plant Lillehammer Norway 4,600 tonnes 15,000 tonnes 0 tonnes 15,000 tonnes OFMSW 2001 A Ecopro, Codigestion plant Verdal Norway 8,000 tonnes 33,000 tonnes 20,000 tonnes 13,000 tonnes OFMSW* 2008 A Oslo EGE Oslo Norway 15,000 tonnes 50,000 tonnes 0 tonnes 50,000 tonnes OFMSW 2014 A Sundet WWTP Växjö Sweden 8,600 tonnes 37,000 tonnes 26,000 tonnes 11,000 tonnes WWTP* 2014 A IVAR biogas plant Stavanger Norway 11,800 tonnes 44,000 tonnes 16,000 tonnes 28,000 tonnes WWTP* 2014 A Mjosanlegget, New Plant Lillehammer Norway 4,800 tonnes 20,000 tonnes 14,000 tonnes 6,000 tonnes OFMSW 2016 A Anyang City Anyang S. Korea 27,700 tonnes 128,000 tonnes 107,000 tonnes 21,000 tonnes WWTP* 2016 D TDS = Total dry solids (1000 kg = 1 tonne) Total: 80,500 tonnes 327,000 tonnes 183,000 tonnes 144,000 tonnes OFMSW = Organic Fraction of Municipal Solid Waste DS% in Food-w aste 30 % *Codigestion: mix of sludge, OFMSW, and other organic w aste DS% in raw sludge 20 % In operations: Under design/construction: Total: T DS 27,600 tonnes 52,900 tonnes 80,500 tonnes Product end-use: A: Use of end product in agriculture D: Drying of end-product I: Incineration of end-product

12

13 Psyttalia wwtp

14 CAMBI

15 Design data

16 Process flow diagram

17 Pre-treatments

18 Pre-treatments

19 Psyttalia installation

20 Psyttalia installation Process

21 Effluent quality 1/2

22 Effluent quality 2/2

23 Sludge treatment

24 Thickening

25 Digestion

26 Digestion

27 Digester internals

28 Dewatering

29 Drying

30 Psyttalia docking pier

31 CAMBI

32 CAMBI s Scope of supply 1 x B6-4 THP system 1 x dewatering centrifuge Option for a second system 1 x B6-4 THP The B6x4 unit will be combined with 4 existing digesters to form an advanced digestion system. The Advanced digestion system, treating 50% of the WAS sludge load, will operate totally independent from the conventional digestion plant (based on the other 4 digesters) which is treating the other 50% of the sludge load. In the future an additional, identical B6-4 line can be added to transform the remaining conventional digesters into a second advanced digestion line

33 1 x B6-4 Design Data Design values Unit Design Basis Normal dry solids% of feed into B6 unit %DS 12-16,5 Max dry solids% peak of feed into B6 unit %DS 18% Average daily treatment capacity Maximum daily treatment capacity, at 30 min. retention time in reactors Maximum daily treatment capacity, at 20 min. retention time in reactors m3/day ton DS/day (at 14% DS) m3/day ton DS/day (at 16.5% DS) m3/day ton DS/day (at 16.5% DS) Temperature of incoming feed, WAS C 25 Temperature of bypassed sludge, PS C 25 Hydrolysis temperature C ~ , ,0

34 1 x B6-4 Process scheme

35 THP CAMBI 1 x B6-4 CAMBI THP

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