Mass & Energy balance in full scale plants for food waste AD

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Mass & Energy balances around full scale plants for food waste anaerobic digestion Franco Cecchi, David Bolzonella, Francesco Fatone, ADSW&EC Vienna 2011 1 Veronica Facchin, Nicola Frison University of Verona, Department of Biotechnology Valorgas(ENERGY-2009-3.2.2) workshop

Transcript of Mass & Energy balance in full scale plants for food waste AD

Page 1: Mass & Energy balance in full scale plants for food waste AD

Mass & Energy balances

around full scale plants for food

waste anaerobic digestion

Franco Cecchi, David Bolzonella, Francesco Fatone,

ADSW&EC Vienna 2011 1

Franco Cecchi, David Bolzonella, Francesco Fatone,

Veronica Facchin, Nicola Frison

University of Verona, Department of Biotechnology

Valorgas (ENERGY-2009-3.2.2) workshop

Page 2: Mass & Energy balance in full scale plants for food waste AD

Mass and energy balances around plants operating the

mesophilic and thermophilic AD of food waste

Solid

Biogas

In the Valorgas project we are considering not

only the global ….

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Pre-

treatments AD Food

waste

S/L

Separation

Liquid

Rejects

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Solid

Biogas

…. mass and energy balance, but also ……

3ADSW&EC Vienna 2011

Pre-

treatments AD Food

waste

S/L

Separation

Liquid

Rejects

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… the balance for single parts of the train of processes for food waste

treatment ….

Solid

Biogas

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Pre-

treatments AD Food

waste

S/L

Separation

Liquid

Rejects

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Solid

Biogas

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Pre-

treatments AD Food

waste

S/L

Separation

Liquid

Rejects

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Solid

Biogas

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Pre-

treatments AD Food

waste

S/L

Separation

Liquid

Rejects

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Solid

Biogas

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Pre-

treatments AD Food

waste

S/L

Separation

Liquid

Rejects

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Solid

Biogas

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Pre-

treatments AD Food

waste

S/L

Separation

Liquid

RejectsPost-

treatments ?

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We decided, together with the plant managers at Valorsul (P) and Biogen

Greenfinch (UK), to collect data on samples from the following points

(wherever possible)

Biogas

post-

Condensate solid phase treatments

water (if any)

(recycle)

pre- separation

raw treatments anaerobic digester

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raw treatments

food waste

post-

liquid phase treatments

inert / reject (if any)

sampling point

anaerobic digester

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Parameter Abbreviation Units Flowrate, Q kg day-1 Total solids TS g kg-1 or % on wet weight Total volatile solids TVS g kg-1 ,%TS Total COD TCOD gO2 kgTS-1 Total Kjeldahl Nitrogen TKN (as N) g kgTS-1 Total phosphorous TP (as P) g kgTS-1

And determine the following parameters (minimal set)

Solid/liquid streams

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Parameter Abbreviation Units Flowrate, Q Nm3 day-1 Mass flowrate kg day-1 CH4 content CH4 % CO2 content CO2 %

Biogas

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Then, also the energetic balance, as a global figure, and for different parts of

the treatment plants, will be determined considering:

a) the heat and power production from biogas

b) the overall power consumption of the plant (kWh per day)

c) the heat and power supply from nets (if any)

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On the other hand, the specific energy consumption for any si ngle unit(e.g., pre-treatment – and its parts, if possible - , digeste r, solid/liquid separation ....)is of fundamental interest for the study and comparison of di fferentprocesses/technologies/substrates.

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Two different treatment plants are considered in the

research project

a) The Biogen Greenfinch plant in Ludlow (UK) -

MESOPHILIC AD of food waste from separate collection

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b) The Valorsul plant in Almadora-Lisbon (P) –

THERMOPHILIC AD of both food waste from separate

collection and residues from restaurants /markets

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Biogen Greenfinch plant in Ludlow (UK)

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Courtesy of Paolo Pavan

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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Courtesy of Michael Chesshire

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MASS BALANCE

Preliminary figures from Greenfinch (tonnes/year)

MesoMeso AD AD

ofof

foodfood wastewaste

Inputs (total) 15.487Biowaste 11.959Industrial water 3.370Domestic water 158

Outputs (total) 12.051Liquid biofertiliser 11.982Solid biofertiliser 69

Biogas 2.249

(Condensate 20)

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foodfood wastewasteDomestic water 158 Solid biofertiliser 69

Rejects 122

Key figures

Specific biogas production 160 Nm3/tonne or 0.65 Nm3/kgVS

VS removal up to 84%

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ENERGY BALANCE

The average yearly data for Biogen Greenfinch

in Ludlow (UK) are

Electricity Generated 2.329 MWhParasitic 782 MWhImported Electricity 211 MWh

90% digester mix & CHP

10% fans and S/L separation

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Imported Electricity 211 MWhNet Electricity Output 1.547 MWh

Generated 194kWh/tonne

Consumed 23kWh/tonne

Energy Index (Gen/Cons) 8,5

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Valorsul treatment plant in

Lisbon Metro area (P) - thermophilic treatment of households and restaurants

food waste

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Courtesy of Paolo Pavan

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Page 28: Mass & Energy balance in full scale plants for food waste AD

19 Municipalities

3378 km²

1,5 million inhabitants

1 million tons of MSW per year

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1 million tons of MSW per year

20% of Portugal MSW

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Organic waste selective

collection programme,

exclusively for hotels,

Collection from large producers

(restaurants, canteens, supermarkets ….)

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exclusively for hotels,

restaurants, canteens and

other large producers

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Incentives to participation

- Free periodic bio-waste container

washes

- Free information support

- Free training from +valor agents

- +Valor network membership

- Programme Certification

- Technical support for complaints,

information and requests (phone line

and internet)

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• Solid Waste

- food waste

Obligatory

• Liquid waste

• Packages

Forbidden

- food waste

- fruit

- vegetables

- meat

- fish

- eggs

- cakes

- snacks

- tea bags

- paper napkins

• Packages

• Glasses, cups, knifes, forks, spoons

• Plastic bags

• Cigarette ends

• Textiles

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Source of OFMSW and type of collection

2547 collection points for

large producers

- Lisbon 1229

- Amadora 149

- Loures / Odivelas 550

b circuit: defined route a vehicle travels to collect from X waste organic producers

1988 household collection

points in 3 locations in Loures

added in 2010

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AD Plant

Digesters and

gas holder

Composting

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Reception and

pre-treatment

Water treatment

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AD Plant

Digesters and

gas holder

Composting

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Reception and

pre-treatment

Water treatment

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Collected bags from restaurants and canteens

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Up to 18% contaminants in large producers waste….

Courtesy of Paolo Pavan

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Courtesy of Paolo Pavan

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“Inert” output of the trommel screen

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Courtesy of Paolo Pavan

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Manual sorting

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Courtesy of Paolo Pavan

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Wet rafination

for heavy (glass,

stones…) and

light (plastic)

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Hydro-pulper

(Linde)

light (plastic)

inerts by means

of a hydro-

pulper

Courtesy of Paolo Pavan

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Hydropulper (internal view)

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From BTA website

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Inert material from the pulper (bottom) ….

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Courtesy of Paolo Pavan

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“Compost” (or compost-like ?) from digestate

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Courtesy of Paolo Pavan

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Compost from digestate

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Courtesy of Paolo Pavan

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Compost from digestate (after polishing)

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Courtesy of Paolo Pavan

Page 46: Mass & Energy balance in full scale plants for food waste AD

Preliminary figures from Valorsul (tonnes/year)

Biogas 4.708.675 m3/y Q, tons/y 854

(Mass) 5.180 tons/y post- TS, tons/y 598

solid phase treatments TVS, tons/y 359

Food waste

Q, tons/y 31.561 Q, tons/y 2.500

TS, tons/y 9.468

TVS, tons/y 7.575 pre- separation

21,000 tons/y from households

10,000 tons/y from large producers

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Key figures

Specific biogas production 149 Nm3/tonne or 0.62 Nm3/kgVS

Removal efficiency 80% (on VS)

TVS, tons/y 7.575 pre- separation

treatments

Water

Q, tons/y post-

Q, tons/y 51.000 liquid phase treatments Q, tons/y 40.000

Inert / reject TS, tons/y 1.377

Q, tons/y 6.030 TVS, tons/y 826 Q, tons/y 57.500

TS, tons/y 3.015

TVS, tons/y 1.508

anaerobic

digester

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ENERGY BALANCES

The average yearly data for Valorsul in Lisbon (P) are

Generated (specific) 160 kWh/tonne

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Consumed (specific) 110 kWh/tonne

Energy Index 1.5

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ENERGY BALANCES

The average consumption at Valorsul in 2010 was some 326 MWh per month for

the treatment of some 2,500 tonnes of biowaste per month.

300

400

500C

on

sum

pti

on

, M

Wh

/m

on

th

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0

100

200

300

0 2 4 6 8 10 12

Co

nsu

mp

tio

n,

MW

h/

mo

nth

Months (2010)

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Consumptions are related to different areas of the plant and a real break

down of the figure is difficult.

17%16%

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29%

38%

Area 1

Area 2

Area 3

Aux

Page 50: Mass & Energy balance in full scale plants for food waste AD

Consumptions are related to different areas of the plant and a real break down of

the figure is difficult.

In general, considering average data:

Area 1 (related to biowaste pre-treatments) accounted for some 56 MWh/month

17%16%

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29%

38%

Area 1

Area 2

Area 3

Aux

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Consumptions are related to different areas of the plant and a real break down of

the figure is difficult.

In general, considering average data:

Area 2 (related to the digester and the CHP unit) accounted for 94 MWh/month

17%16%

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29%

38%

Area 1

Area 2

Area 3

Aux

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Consumptions are related to different areas of the plant and a real break down of

the figure is difficult.

In general, considering average data

Area 3 (related to S/L separation, composting+exhaust air treatment, and WWTP)

accounted for some 125 MWh/month

17%16%

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29%

38%

Area 1

Area 2

Area 3

Aux

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Consumptions are related to different areas of the plant and a real break

down of the figure is difficult.

In general, considering average data

Auxiliary consumptions accounted for some 52 MWh/month.

17%16%

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29%

38%

Area 1

Area 2

Area 3

Aux

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Take home message

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The food waste quality does matter !!!