ad of the organic fraction of msw - iea bioenergy
TRANSCRIPT
AD of the organic fraction of MSW System overview for source and
central separated waste
David Baxter* and Teodorita Al Seadi**
* European Commission JRC and Task 37
** BIOSANTECH, Denmark and Task 37
Contents
• Policy background • Waste and biomass potential
– How much digestible waste – Biogas potentials of biogenic waste
• Biogenic waste as a resource – Treatment options – AD of OFMSW at a glance – Examples of AD plants – Comparative costs
• Conclusions and future trends
DRIVERS
Climate change mitigation
Resource efficiency
Security of energy supply
Environment and health (human and animal)
Policy Background
Reduced landfill (emissions and resource efficiency)
Renewable energy (biogenic component of MSW use
as fuel) (e.g. Directive 2009/28/EC in Europe)
Health protection (e.g. European animal by-products
regulation 1069/2009; EU Industrial Emissions
directive 2010/75/EC for air and water
protection)
Categories of waste
How much digestible waste do we have
Rules of thumb • Average of 1,2 kg household waste /inhabitant/day; Up to double amounts in high income countries • 1.3 billion tonnes of MSW are produced yearly; 46% of it is organic • Globally, MSW generation levels are expected to double by 2025 • Higher share of organic material in low income countries (62%) compared to (27%) in high income countries
Food waste represents 23 - 67,5% of the MSW (IPCC , 2000)
Global composition of MSW
Biogenic Waste
Organic MSW (OFMSW) has very high methane potential Specific Specific
Biomass type DM DM/VS VS methane methane
potential production
(%) (%) (%) m3 CH4/kgVS m3 CH4/t
Cattle slurry 8,00 80,0 6,40 0,200 12,8
Mixed fruit residues
15,00
85,0
12,75
0,370
42,1
Fats (Soy oil/margarine) 95,00 90,0 85,50 0,800 684,0
Household waste 30,00 85,0 25,50 0,400 102,0
Sewage sludge,
concentrated
10,00
75,0
7,50
0,400
30,0
Organic MSW (OFMSW) has very high methane potential
Waste as a resource
Drivers to separate OFMSW
• Policy and regulatory • Environmental • Economy (saving on post-treatment costs) • Industry
Why source separation ?
• Benefits the quality and the costs of the overall waste management • Benefits the quality of other waste recycling • Preserves resources and protects the environment • Separately collected digestible fraction can be supplied directly to a biogas plant
Treatment options for OFMSW
Overall, AD along with composting have the least negative impacts on
human health and the environment and the most benefits, when compared
to other MSW management options (ECN-2011)
?
Feedstock: The organic fraction of MSW (OFMSW) - Source separated, separately collected - Bulk collected, centrally separated
Various AD Systems:
- Wet or Dry - Batch or Continuous - Single Stage or Multi-Stage - Co-digestion or Mono -digestion (MSW alone)
Preprocessing and post-treatment
Pathogen inactivation/Sanitisation
AD of OFMSW at a glance
"Biogas Handbook: Science,
production and application"
Published in February 2013 by
Woodhead
ISBN 978-0-85709-498-8 (print)
ISBN 978-0-85709-741-5 (on-line)
http://www.woodheadpublishing.com/en/book.aspx?bookID=2576
AD of OFMSW at a glance
AD method
Process type
Dry matter %
Examples of AD plant concepts
Mono digestion (only MSW) Dry 20-30 Valorga, Kompogas (single phase, plug-flow) Dranco (single stage) Linde
Wet 2 BTA Co-digestion (with animal slurries, other wastes, crops etc)
Wet 8-15 Danish joint co-digestion plants (CAD)
Integrated Dry 20-30 AIKAN - Integrated dry AD and composting CAMBI – Integrated Hydrolysis + two stage AD
Types of AD systems used in MSW treatment
• Single Stage: - Single stage low solids (SSLS) ; Wassa
- Single stage high solids (SSHS); Dranco, Kompogas, Valorga
• Multi Stage - Multi stage low solids (MSLS); BTA, Biocomp
- Multi stage high solids (MSHS); Biopercolat • Batch - Aikan
Evolution of AD of OFMSW in Europe
Development of AD of OFMSW in Europe (Mattheeuws, 2012)
• More than 200 OFMSW plants operating in Europe; Average: 30,000 tons/year • Main drivers:
- reduced landfill - increased bioenergy - biofuels
• Restrictions/ regulations -Animal By-Product Regulation -Restrictive utilization of digestate as fertiliser, based on national quality standards
Commercial AD Treatment Systems
Single stage wet system; Wassa, Finland
Wet AD of bio-waste KOMPTECH biogas plant at Markgrafneusiedl, Austria
Single-stage Dry Systems High solids plug flow digesters
Multi-stage AD process
Linde-KCA two-stage dry digester
Multistage dry (high solids) systems
Batch digesters
• Single stage batch digester (e.g. Biocel) • Sequential batch digester ( e.g. SEBAC) • Hybrid batch UASB • Three step dry AD and composting (Aikan)
Batch digesters – Spiez (CH)
Integrated dry AD and composting
Three step dry AD and composting –Aikan™ Denmark
Co-digestion of manure and source separated household waste (e.g. biogas plant in Västerås/Sweden (Växtkraft )
Mechanical Biological Treatment (MBT)
Source: DEFRA (UK): MBT of MSW (2007)
Mechanical Biological Treatment (MBT)
An adaptation to MBT
AD of the liquid fraction after enzymatic treatment
(The REnescience Waste Refinery *) TM
REnescience technology uses enzymes to separate mixed MSW
into different fractions:
- without need for mechanical pretreatment (e.g. shredding)
(operates at low temperatures and atmospheric pressure)
- producing bioliquid for AD (digestate as fertiliser)
- producing clean materials for recycling and feedstocks for other
processes * DONG Pilot Facility" Copenhagen (2009)
Source separation and collection by door-to-door method a) Bin collection system
•Single-compartment bins •Two–compartments bin or double container
b) Bag collection system •Paper bags •Plastic bags •Biodegradable plastic bags
Source separation and separate collection in road containers
Underground containers
Optical sorting of household waste
Source separation options
Waste for optical sorting
Important quality
requirements !!!!
Digestate is an excellent biofertiliser for crops
• Sanitation (pathogen inactivation) • Free of physical pollutants (plastics, metals, glas, stones) • Declaration of nutrient content (NPK, DM, pH) • Strict control of chemical pollutants - heavy metals - organic pollutants (persistant!)
Quality standards/ certification / quality assurance implemented in many
countries, aiming to guarantee quality and to enhance use as biofertiliser
Organic pollutant Limit value
PAHs
(Polycyclic aromatic
hydrocarbons)
3
mg/kg DM
PCDD/F
(Dioxins and furans)
20
ng TE/kg DM
HCH, DDT, DDE etc.
(Chlorinated
pesticides)
0.5
mg/kg prod.
PCB
(Polychlorinated
biphenyls)
0.2
mg/kg DM
AOX
(Absorbable organic
halogens)
500
mg/kg DM
LAS
(Linear alkylbenzene
sulphonates)
1300
mg/kg DM
NPE
(Nonylphenol and
nonylphenolethoxyla
tes
10
mg/kg DM
DEPH
Di (2-ethylhexyl)
phthalate)
50
mg/kg DM
Example of limit values for organic pollutants in Austria, Denmark and Switzerland *I-TEC: International Toxicity Equivalents Limits of heavy metals (mg/kg DM) in ‘waste’ products
that can be applied to land in some IEA Bioenergy Task 37 member countries
Cd Pb Hg Ni Zn Cu Cr
EU,
recommendations
20 750 16 300 2500 1000 1000
EU,
recommendations
starting 2015
5 500 5 200 2000 800 600
EU,
recommendations
starting 2025
2 300 2 100 1500 600 600
Denmark 0.8 120 0.8 30 4000 1000 100
Finland 1.5 100 1 100 1500 600 300
France 3 180 2 60 600 300 120
Germany 10 900 8 200 2500 800 900
Ireland 20 750 16 300 2500 1000 1000
Norway 2 80 3 50 800 650 100
Sweden 1 100 1 50 800 600 100
Switzerland 1/0.7 120/45 1/0.4 30/25 400/200 100/70 70/na
The Netherlands 1.25 100 0,75 30 300 75 75
United Kingdom 1.5 200 1 50 400 200 100
IEA Bioenergy Task 37 Report: Digestate Quality (2012)
Some costs for different systems
ASSESSMENT OF THE OPTIONS TO IMPROVE THE MANAGEMENT
OF BIO-WASTE IN THE EUROPEAN UNION: ANNEX E: Approach to
estimating costs, ARCADIS Project number – 11/004759 | Version A |
30-11-2009:
http://ec.europa.eu/environment/waste/compost/pdf/ia_biowaste%20-
%20ANNEX%20E%20%20-%20approach%20to%20costs.pdf
Some capital costs for different systems
MBT SRF
Incineration Electricity
Incineration CHP
AD Electricity
AD CHP
AD Up-grading
250 630 750 380 480 450
CAPEX: Euro/tonne installed capacity
Some operating costs for different systems
OPEX: Euro/tonne installed capacity
MBT SRF
Incineration Electricity
Incineration CHP
AD Electricity
AD CHP
AD Up-grading
21 25 27 38 40 45
Conclusions and future trends
AD of sorted MSW is an integral part of organic waste management and recycling with renewable energy recovery
Intrinsic benefits / incentives: • Sustainable alternative to incineration, landfilling and uncontrolled waste dumping • Capture of renewable methane • Digestate as fertiliser, off-setting the use of fossil fertilisers • Preservation of natural resources: recycling of macro- and micro nutrients and carbon • Cleaner urban environment: less pollution from dumping of organic material • Less GHG emissions • Better public and animal health (breaking the chain of diseases spreading/ pathogen inactivation through AD
Barriers • Lack of awareness of benefits • Inadequate /lack of supporting policies • Negative public perception in some countries AD does not solve all problems, some wastes (residuals) still need other treatment (e.g. incineration or landfill), but AD helps maximise resource recovery
Don’t waste your waste!
Thank you for your attention
www.iea-biogas.net
Methane potentials of some Typical AD feedstock
Two-stage dry process
BTA multi-stage AD process
Multistage wet (low solids) systems
1 year 2 years 3 years 4 years 5 years 6 years 7 years
Preparation
Pre s tudy 4 to 6 months
Objectives 3 to 6 months
Stakeholder consultation 1 to 3 months
Decis ions taken in the Ci ty Counci l 3 months
Investigation for the introduction 4 to 8 months
Organization of collection
Contracting organization 6 months to 5 years Existing agreement to be reviewed, procurement of entrepreneur
Col lection in-house 1 to 2 years The operating organization to be reviewed, reorganization, purchase of vehicles
Optica l sorting 1 to 3 years Building permits, construction of facility
Treatment
Procurement 3 to 6 months
Own faci l i ty 3 to 5 years
Introduction
Purchase of equipment 3 to 5 months
Fee/Regulations/Consultation 4 to 6 months
Information to households and bus inesses 3 to 6 months Ongoing information during the introduction
Introduction in various s tages 1 to 5 years
Timeline for implementing a source separation system Swedish experience
1 year 2 years 3 years 4 years 5 years 6 years 7 years
Preparation
Pre s tudy 4 to 6 months
Objectives 3 to 6 months
Stakeholder consultation 1 to 3 months
Decis ions taken in the Ci ty Counci l 3 months
Investigation for the introduction 4 to 8 months
Organization of collection
Contracting organization 6 months to 5 years Existing agreement to be reviewed, procurement of entrepreneur
Col lection in-house 1 to 2 years The operating organization to be reviewed, reorganization, purchase of vehicles
Optica l sorting 1 to 3 years Building permits, construction of facility
Treatment
Procurement 3 to 6 months
Own faci l i ty 3 to 5 years
Introduction
Purchase of equipment 3 to 5 months
Fee/Regulations/Consultation 4 to 6 months
Information to households and bus inesses 3 to 6 months Ongoing information during the introduction
Introduction in various s tages 1 to 5 years
Examples of animal by-products suitable for AD Required pre-treatment
conform to
Category
Manure and digestive tract content from
slaughterhouse
No pre-treatment Category 2
Milk and colostrums No pre-treatment Category 2
Perished animals Pressure sterilisation Category 2
Slaughtered animal, not intended for human
consumption
Pressure sterilisation Category 2
Meat-containing wastes from foodstuff-industry Pasteurisation Category 3
Slaughterhouse wastes from animals fit for human
consumption
Pasteurisation Category 3
Catering waste, except for waste from international
transports (flights and trains etc)
In accordance with national
regulation
Category 3
Animal by products allowed to be supplied to AD plants, and the required conditions and pre-treatments
according to the EU Animal By-Product Regulation (ABP)