(MBT) and (wet) anaerobic digestion
Transcription
(MBT) and (wet) anaerobic digestion
University of Verona, Department of Biotechnology Mechanical Biological Treatment (MBT) and (Wet) Anaerobic Digestion David Bolzonella & Charles Banks Jyvaskyla Summer School 2011 1 University of Verona, Department of Biotechnology AD of biowaste is a well established but still growing technology …. De Baere, WST, 2006 Jyvaskyla Summer School 2011 2 University of Verona, Department of Biotechnology Source: De Baere et al 2010 Jyvaskyla Summer School 2011 3 De Baere, WST, 2006 Jyvaskyla Summer School 2011 4 University of Verona, Department of Biotechnology University of Verona, Department of Biotechnology The implementation of separate collection opened the possibility to treat biowaste. Despite this, the treatment of residual waste is still very important De Baere, WST, 2006 Jyvaskyla Summer School 2011 5 University of Verona, Department of Biotechnology In these cases AD is typically part of a Mechanical Biological Treatment (MBT) process This technology is dedicated to the treatment of unsorted Municipal Solid Waste (MSW) industrial waste the grey fraction of MSW (the residual part after separate collection) Jyvaskyla Summer School 2011 6 University of Verona, Department of Biotechnology The mechanical-biological-treatment (MBT) is combination of two processes: the first one, mechanical, is dedicated to the separation of recyclable materials and the organic fraction from the bulk waste while the second one, biological, is dedicated to the stabilization of this organic material. The biological step can be either aerobic or anaerobic. The main benefit of MBT technology is its capability of reducing the mass and volume of waste sent to landfills. At the same time, recyclable or thermally reusable fractions can be separated. Jyvaskyla Summer School 2011 7 University of Verona, Department of Biotechnology Mixed waste Recyclables (glass, metals) & Refuse Derived Fuel (RDF) Compost-like or RDF Mechanical sorting and Pre-treatment Biological process Rejects to landfill or inciniration Biogas (energy) + biostabilized in anaerobic systems + aerobic Generic MBT technology Jyvaskyla Summer School 2011 8 University of Verona, Department of Biotechnology Typical AEROBIC MBT RDF Residual waste Dry sorting Recoverable materials metals, paper, card, plastic Aerobic composting CO2 and water Jyvaskyla Summer School 2011 Drying Incineration Water 9 University of Verona, Department of Biotechnology Typical ANAEROBIC MBT RDF Residual waste Dry sorting Recoverable materials metals, paper, card, plastic Anaerobic digestion Biogas Jyvaskyla Summer School 2011 Drying Incineration Water 10 University of Verona, Department of Biotechnology A second option: The Biological Mechanical Treatment (BMT) Residual waste biological treatment Mechanical sorting posttreatment refining disposal or further recovery Recovery Jyvaskyla Summer School 2011 11 University of Verona, Department of Biotechnology AIMS typical aims of MBT plants include the: Pre-treatment of waste going to landfill; Diversion of non-biodegradable and biodegradable MSW going to landfill through the mechanical sorting of MSW into materials for recycling and/or energy recovery as refuse derived fuel (RDF); Diversion of biodegradable MSW going to landfill by reducing the dry mass of BMW prior to Landfill and the biodegradability of BMW prior to landfill; Stabilisation into a compost-like output (CLO) for use on land; Conversion into a combustible (RDF and biogas) for energy recovery Jyvaskyla Summer School 2011 12 University of Verona, Department of Biotechnology MBT components and configurations Jyvaskyla Summer School 2011 13 University of Verona, Department of Biotechnology The mechanical stage of the process generally has two main roles: to brake down the waste in smaller parts and recovery some recyclable materials The net result will be the reduction of the mass and volume of the treated waste due to the removal of materials for recycling and both carbon and moisture losses. Clearly, recycled material has a worst quality than the one coming from separate collection ! Beside the recyclable materials and the biogas the residual outputs are a biostabilized material and RDF. Jyvaskyla Summer School 2011 14 University of Verona, Department of Biotechnology Source DEFRA (UK) Jyvaskyla Summer School 2011 15 Source DEFRA (UK) Jyvaskyla Summer School 2011 16 University of Verona, Department of Biotechnology University of Verona, Department of Biotechnology Bags opening and size reduction Shredder Jyvaskyla Summer School 2011 17 Jyvaskyla Summer School 2011 18 University of Verona, Department of Biotechnology University of Verona, Department of Biotechnology Hammer mill Jyvaskyla Summer School 2011 19 University of Verona, Department of Biotechnology Ball mill Jyvaskyla Summer School 2011 20 University of Verona, Department of Biotechnology Metals separation and recovery Jyvaskyla Summer School 2011 21 University of Verona, Department of Biotechnology Mixed feed Conveyer Conveyer Fine Jyvaskyla Summer School 2011 Oversize 22 University of Verona, Department of Biotechnology Air classifier Jyvaskyla Summer School 2011 23 University of Verona, Department of Biotechnology Manual separation Jyvaskyla Summer School 2011 24 University of Verona, Department of Biotechnology Source DEFRA (UK) Jyvaskyla Summer School 2011 25 University of Verona, Department of Biotechnology MBT + AD Source DEFRA (UK) Jyvaskyla Summer School 2011 26 University of Verona, Department of Biotechnology The typical AD application is the DRY process. In case of the application of a WET AD process, a further “purification” step is needed to remove the residual fraction of inert material Linde process for wet AD Jyvaskyla Summer School 2011 27 University of Verona, Department of Biotechnology MARKETS & OUTLETS FOR THE OUTPUTS Recyclables derived from the various MBT processes are typically of a lower quality than those derived from a separate household recyclate collection system and therefore have a lower potential for high value markets. Materials which may be extracted from MBT processes include metals, glass, textiles, paper/card, and plastics. The most common of these is glass, which may be segregated with other inert materials such as stones and ceramics. Jyvaskyla Summer School 2011 28 University of Verona, Department of Biotechnology Carton baler Jyvaskyla Summer School 2011 29 University of Verona, Department of Biotechnology Plastic baler Jyvaskyla Summer School 2011 30 University of Verona, Department of Biotechnology Separated paper Jyvaskyla Summer School 2011 31 University of Verona, Department of Biotechnology Biogas can be produced, but at low extent, rarely exceeding 60 m3 per tonne of treated material (equivalent to some 120-140 kWh). Where the MSW is sorted / treated to produce a high calorific value waste stream comprising significant proportions of the available combustible materials such as mixed paper, plastics and card, this stream may be known as Refuse Derived Fuel (RDF). Jyvaskyla Summer School 2011 32 University of Verona, Department of Biotechnology Refuse Derived Fuel (RDF) High Heating Value up to 30 MJ/kg Jyvaskyla Summer School 2011 33 University of Verona, Department of Biotechnology Potential outlets for RDF 1. Industrial Combined Heat and Power (CHP) units 2. Cement kilns 3. Co-firing with coal at power stations 4. Co-firing with fuels like poultry litter and biomass 5. Advanced thermal technologies, such as pyrolysis and gasification Jyvaskyla Summer School 2011 34 University of Verona, Department of Biotechnology Compost – like output Jyvaskyla Summer School 2011 35 University of Verona, Department of Biotechnology Typical CITEC Process Electricity Flare Generator Biogas storage Gas Engine CHP Premix. Densiometric separator Tipping pit. Magnetic separator DIGESTER Press Aerobic maturation Hammer mill Drum screen Air Air classification classifier Pelletisation plant Compost Centrifuge RDF Jyvaskyla Summer School 2011 36 University of Verona, Department of Biotechnology Mass balance for 1 tonne of waste Household waste (MSW) Refuse derived fuel 420 kg ‘Biodegradable waste’ fraction (BMW) 400 kg Washing Sand 39kg BMW 261 kg Metals 30kg Paper / plastic 150 kg Process water Coarse inerts 100kg Digestion Biogas (per T of BMW) 142 m3 Biogas (per T of MSW) 37 m3 Process water 161 kg Digestate 100 kg Based on a 230,000 tonne/year plant at Vargon, NL Jyvaskyla Summer School 2011 37 University of Verona, Department of Biotechnology MBT & WET ANAEROBIC DIGESTION Jyvaskyla Summer School 2011 38 University of Verona, Department of Biotechnology Application of the WET anaerobic digestion in MBT systems The organic material recovered from a MSW through the mechanical processes can undergo to an aanerobic treatment for energy recvoery. However, this material is generally of bad quality. This is characterised by: A very high content of inert material (total solids typically around 50% or more and low volatile fraction, 60% of TS or lower) a very low biogas potential (normally some 60-70 m3/tonne, never exceeding 100 m3/tonne on the input material, but 140 m3/tonne on the organic material entering the AD unit Jyvaskyla Summer School 2011 39 University of Verona, Department of Biotechnology A case study: Valorsul s.a. waste treatment plant in Lisbon Jyvaskyla Summer School 2011 40 Jyvaskyla Summer School 2011 41 University of Verona, Department of Biotechnology University of Verona, Department of Biotechnology Collected bags from restaurants and canteens Jyvaskyla Summer School 2011 42 University of Verona, Department of Biotechnology Belt conveyor Jyvaskyla Summer School 2011 43 University of Verona, Department of Biotechnology Bags splitter / shredder Jyvaskyla Summer School 2011 44 University of Verona, Department of Biotechnology Quality of the organic material can be very low …… Jyvaskyla Summer School 2011 45 University of Verona, Department of Biotechnology “Inert” output of the trommel screen Jyvaskyla Summer School 2011 46 University of Verona, Department of Biotechnology Manual sorting Jyvaskyla Summer School 2011 47 University of Verona, Department of Biotechnology Wet rafination for heavy (glass, stones…) and light (plastic) inerts by means of a hydropulper Hydro-pulper (Linde) Jyvaskyla Summer School 2011 48 University of Verona, Department of Biotechnology Hydropulper (internal view) Jyvaskyla Summer School 2011 49 University of Verona, Department of Biotechnology Inert material from the pulper (bottom) …. Jyvaskyla Summer School 2011 50 Jyvaskyla Summer School 2011 51 University of Verona, Department of Biotechnology Jyvaskyla Summer School 2011 52 University of Verona, Department of Biotechnology University of Verona, Department of Biotechnology Compost from digestate Jyvaskyla Summer School 2011 53 University of Verona, Department of Biotechnology Compost from digestate Jyvaskyla Summer School 2011 54 University of Verona, Department of Biotechnology Compost from digestate (after polishing) Jyvaskyla Summer School 2011 55 University of Verona, Department of Biotechnology The problem of inert accumulation in wet AD reactors Jyvaskyla Summer School 2011 56 University of Verona, Department of Biotechnology Accumulation of inert material in the wet AD reactor BIOGAS Grease / oil Problem: phase separation Liquid Solid (inert) Jyvaskyla Summer School 2011 57 University of Verona, Department of Biotechnology Giacetti, Contri, Muraro (2009). BIOWASTE, Milano 24 febbraio 2009 Jyvaskyla Summer School 2011 58 University of Verona, Department of Biotechnology Giacetti, Contri, Muraro (2009). BIOWASTE, Milano 24 febbraio 2009 Jyvaskyla Summer School 2011 59 University of Verona, Department of Biotechnology Giacetti, Contri, Muraro (2009). BIOWASTE, Milano 24 febbraio 2009 Jyvaskyla Summer School 2011 60 University of Verona, Department of Biotechnology Giacetti, Contri, Muraro (2009). BIOWASTE, Milano 24 febbraio 2009 Jyvaskyla Summer School 2011 61 University of Verona, Department of Biotechnology Giacetti, Contri, Muraro (2009). BIOWASTE, Milano 24 febbraio 2009 Jyvaskyla Summer School 2011 62