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Technische Universität München Institute for Technologies of Biogenous Feedstocks Anaerobic Digestion of Bioorganic Municipal Solid Waste (BMW) Univ.-Prof. Dr.-Ing. Martin Faulstich Dipl.-Ing. Gunther Pesta „Asian-European Environmental Technology & Knowledge Transfer“ 17 th -18 th of March, 2006 Hefei, Anhui Province, China

TTechnische echnische UUniversität niversität MMünchenünchen€¦Gas storage Steam Thermal energy Electrical energy Gasflare Preselection Pretreatment. Pretreatment and preparationPretreatment

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Technische Universität MünchenTechnische Universität MünchenInstitute for Technologies of Biogenous Feedstocks

Anaerobic Digestion of Bioorganic Municipal Solid Waste (BMW)

Univ.-Prof. Dr.-Ing. Martin FaulstichDipl.-Ing. Gunther Pesta

„Asian-European Environmental Technology & Knowledge Transfer“17th-18th of March, 2006

Hefei, Anhui Province, China

Why Anaerobic Digestion?Why Anaerobic Digestion?

Anaerobic Digestion (AD) is state of the art• Wide range of applications, both agricultural and industrial

AD produces a renewable energy source• Biogas is produced out of biomass (e. g. manure, energy crops)• Biogas is rated as a „non CO2-emitting fuel“• Decentralised energy supply (4 livestock units supply a germanhousehold with electric energy)

AD produces a well balanced liquid fertiliser• Residues of AD offer high fertilising and ground waterprotecting effects

• Reduction of mineral fertilisers (up to 20 kg mineralicammonia per livestock unit and year)

...

Bioorganic Municipal Waste (BMW)Bioorganic Municipal Waste (BMW)

Average composition of organic fraction of municipal solid waste (Bioorganic Municipal solid Waste, BMW) from fruit and vegetable markets in Treviso, Northern Italy

Parameter Unit Average Standard Deviation Max Min

Dry matter (DM) g/kg 81.8 23.9 105.6 67.8

Organic Dry Matter (ODM) g/kg 73.6 10.8 85.9 67.3

Organic Dry Matter (ODM) % DM 90.0 9.6 99.5 81.5

Total Kjeldahl Nitrogen (TKN) g/kg DM 29.6 6.2 35.2 23.9

Phosphorous, total (Ptot)

g/kg DM 8.9 2.3 11.3 7.1

Source: Pavan, 2002

Flow Scheme of an AD-plant Flow Scheme of an AD-plant

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

Delivering and UnloadingDelivering and Unloading

Delivering in special trucks and transport facilities

• Sanitising by rinsing of tires when entering the plant

• Sanitising the equipment after unloading (outside and inside)

=> transfer of pathogens

Unloading within enclosed buildings

• Constant under-pressure by exhausting air

• Exhausted air should be cleaned by biofilters

=> transfer of microorganisms

=> odour emissions

Delivering and UnloadingDelivering and Unloading

Delivering and UnloadingDelivering and Unloading

Flow Scheme of an AD-plant Flow Scheme of an AD-plant

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

Pretreatment and preparationPretreatment and preparation

Pretreatment and preparationPretreatment and preparation

Mechanical pretreatment• Seperation by drum screens, vibration screens,magnetic seperators

• Manual selection belt• Shredding

Source: Linde KCA

Pretreatment and preparationPretreatment and preparation

Pretreatment and preparationPretreatment and preparation

Mechanical pretreatment• Seperation by drum screens, vibration screens,magnetic seperators

• Manual selection belt• Shredding of MSW

Mashing/pulping with process water• Non-organic fraction can be seperated(i. e. mineralic components, glass, batteries)• Shearing forces help to disintegrate substratedown to fibre size

Forming of a homogenius digestable slurry Source: Linde KCA

Hygienisation of Co-SubstratesHygienisation of Co-Substrates

Legislative regulations demand hygienic pretreatinge. g. kitchenwaste, food-leftovers, slaughterhousewastes category 2 and 3,leftovers from fishindustry, slaughterhouse wastewaters

Sterilisation pressure 2 bartemperature 121 °Cduration 20 min

Hygienisationtemperature 70-90 °Cduration 15-60 min

Sanitationheat treatment of lower temperature over an extendedtime periode

Flow Scheme of an AD-plant Flow Scheme of an AD-plant

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

Digestersystems for MSW-TreatmentDigestersystems for MSW-Treatment

Phases => single-/two-phaseDigester liquor => „dry“/liquidFeed-flow => batch/continuosTemperature => mesophilic/thermophilic

Pretreated waste Biogas

Digestersystem

Residues treatment

Pulper

Dewatering

Liquid phaseSolid phase

Source: Linde KCA

Linde-KCA System, Dresden

Digestersystems for MSW-TreatmentDigestersystems for MSW-Treatment

System Kompogas (BMW treatment)AD-plant in Passau

Flow Scheme of an AD-plant Flow Scheme of an AD-plant

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energyPreselectionPretreatment

Effluent TreatmentEffluent Treatment

Solid-Liquid-Separation=> liquid phase: fertiliser (liquid, solid), or aerobic post-treatment=> solid phase: composting, humiliser

Effluent TreatmentEffluent Treatment

AD plant for treating BMW, Passau

Flow Scheme of an AD-plant Flow Scheme of an AD-plant

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

Utilisation of BiogasUtilisation of Biogas

Biowaste treating biogasplant, Passau Capacity: 1 MWel

Gas-Cleaning=> scrubber (chemical, biological)=> dewatering

Possibilities for Utilisation of Biogas

=> Combined heat and power unit(CHP)

=> Boiler

=> Feeding the gas grid

=> Compressing for transportation/use in vehicels

Flow Scheme of an AD-plant Flow Scheme of an AD-plant

BMU, 1999

Fertiliser

Fertiliser storage

Thermal energy

Biogas digester

Mixing tank Manure

Combined heat and power unit

Co-Substrates

Gas storage

Steam

Thermal energy

Electrical energy

Gasflare

PreselectionPretreatment

Co-Digestion Plant Erkheim, Germany Co-Digestion Plant Erkheim, Germany

Biowaste and Food leftovers=> 10 000 t/a of each=> mesophilic, single-phase, hygienisation=> digestion residues are composted

7 200 MWh/aElectrical Energy

40 000 m³/aCompost (total)

820 kWhel.Biogas CHP

9 860 m³N/dBiogasproduction

Source: Bioenergie Schwaben, 2004

Co-Digestion Plant Finsterwalde, GermanyCo-Digestion Plant Finsterwalde, Germany

19 710Pig manure

13 505Food leftovers from restaurants

t/a

87 600Total

14 235Slaughterhouse waste

40 150Cow manure

11 000 MWh/aThermal Energy

1 100 t/aCristallic Ammonia-Hydrogen-Carbonat

6 800 MWh/aElectrical Energy

3 400 000 m³/aBiogas

QUELLE: Schwarting Umwelt GmbH, 2004

Co-Digestion Plant Gröden, GermanyCo-Digestion Plant Gröden, Germany

Installation 1995/96Digestervolume 2 x 3 000 m³Manure 75 000 t/aBiowaste 35 000 t/asingle-phase

397 kWtherm.Thermal energy, grid

244 kWSteam, industry

10 649 t/a CO2-equivalentsCO2-balance

3 x 403 kWel.CHP

10 000 m³N /dBiogas

QUELLE: HAASE Energietechnik, 2004

Co-Fermentation in Sewage PlantsCo-Fermentation in Sewage Plants

http://www.azv-breisgau.de/3_klaeranlage.htm

20-50 % Co-Substrates into the sewage sludge digester• Flotation sludge• Food leftovers• Biowaste• ...

40-200 % increased biogas production• Improved quantity• Improved quality

Depending on the rheology and concentrationof biowaste additional pre- and posttreatmentequipment needs to be installed.

Why Anaerobic Digestion?Why Anaerobic Digestion?

Harvesting

Growing

Waste water with nutrients(NH4, Na, Ca, K,S, Mg, PO4)

Biogas plant

Enriching consumer:AgricultureHouseholdsIndustry

Food leftovers, biowaste, BMW

Production residues

Co-DigestionAnimal feed

Manure

Production

CO2-Emissions

Products

Industryconsumer:AgricultureHouseholdsIndustry

Biogas

thermal energy

CHP

electrical energyBreeding

Pe06

Univ.-Prof. Dr.-Ing. Martin FaulstichInstitute for Technologies of Biogenous Feedstocks

[email protected]

Dipl.-Ing. Gunther [email protected]

[email protected]

Wissenschaftszentrum Straubing

Weihenstephan - Center of Life and Food Sciences