OPERATIONAL CONSIDERATIONS FOR CO-DIGESTION



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Transcription:

OPERATIONAL CONSIDERATIONS FOR CO-DIGESTION California Water Environment Association SARBS Seminar on Math, Operations and Maintenance for Biosolids Systems September 2011 Fred Soroushian, P.E. PE CH2M HILL

PRESENTATION OVERVIEW Co-digestion overview Co-digestion i feedstock Bench scale testing Co-digestion implementation and business model

CO-DIGESTION OVERVIEW

CODIGESTION OVERVIEW BENEFITS OF CO-DIGESTION Solves environmental problem and increases renewable energy production Increase in gas and energy production Reduced load and energy demand for wastewater treatment Optimized gas production during peak power demand Efficient use of existing infrastructure More efficient compared to pretreatment at each sources Potential reduction in sewer system odors, blockage, and GHG emissions

CO-DIGESTION OVERVIEW - DRAWBACKS OF CO-DIGESTION Increases WWTP direct loads Changes C/N ration in influent when high h C, low N substrate t is directed d to digesters Need additional facilities for codigestion Substrate must be trucked-in May need additional pretreatment

CO-DIGESTION POTENTIAL IN CA Scenario Biogas (million cf/d) without with Co- Codigestiodigestion Electricity (MW) without with Co- Codigestiodigestion Scenario 1 98 155 223 352 (all 312 STPs) Scenario 2 45 71 102 161 (114 STPs with ADs) Biosolids : Food Waste = 80 : 20 by volume for codigestion Biogas can be increased by 58% with co-digestion 60 MW increase

CO-DIGESTION EXPERIENCE North America East Bay MUD, Riverside, IEUA, Watsonville, Millbrae, and CMSA, CA West Lafayette, IN Pendleton, OR Lethbridge and Edmonton, Canada Europe Denmark >100 Germany >10 Italy, Hungary, Poland, etc.

CO-DIGESTION FEEDSTOCK Many feedstock sources: FOG Breweries and distilleries Dairy Food manufacturers Baking industry Slaughter houses FOG, meat, fish, dairy, and fruit wastes produce most gas Issues include preservatives, other additives, and contaminants

CO-DIGESTION FEEDSTOCK Science of co-digestion is not well known Limited available data Current knowledge is site-specific ifi and often not transferable to other facilities Bench scale testing allows different food wastes to be evaluated for co-digestion Co-digestion g operation Blend ratios Dewaterability Dewatering filtrate quality

BENCH SCALE TEST SETUP

BENCH SCALE TEST SETUP Source: Jörg Krampe, SA Water Corporation, 2011

BENCH SCALE TEST PLAN Simulate anaerobic digester conditions Use digester sludge as inoculums 20 days retention time Mesophilic or thermophilic conditions to match digester operations Test various concentrations ti of substrate t mixtures 0% Reference 5% 10% 15% 20% 30% 50% Expected operation level Inhibition/Overloading

BENCH SCALE TEST GAS PRODUCTION Source: Jörg Krampe, SA Water Corporation, 2011

BENCH SCALE TEST GAS PRODUCTION Mesophilic Digestability Tests Gas Produc ction (ml) 3000 2500 2000 1500 1000 500 Control Tomato Salad Dressing Cheese 50:50 blend digestibility testing Mesophilic Thermophilic 0 1 3 5 7 9 11 13 15 17 19 21 23 25 27 Thermophilic Digestability Tests Day of Test 4000 3500 Gas Production (m ml) 3000 2500 2000 1500 1000 500 Control Tomato Salad Dressing Cheese 0 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 Day of Test

CO-DIGESTION IMPLEMENTATION Food waste sources identification Bench scale digestion testing Digester Loading Typically limit to 20 to 30% of digester VS feed Continuous feed if possible Optimum C:N ratio of 20-30 Receiving station Screens blending/mixing Heating

CO-DIGESTION IMPLEMENTATION Digestion system process modifications/ improvements Food waste flow distribution and measurement Gas collection, treatment and co-generation infrastructure improvements Solids handling systems assessment Dewatering e system operation o Recycle management

POTENTIAL BUSINESS MODEL

CO-DIGESTION COST - BENEFIT ANALYSIS Substrate Total cost of addition of 1 kl substrate ($) Total benefit of addition of 1 kl substrate ($) Total profit per kl added ($) Sweet Whey 2.14 6.36 4.22 Salty Whey 4.36 7.82 3.47 Chicken blood 37.00 14.37-22.63 Brewery 1.08 3.63 2.55 Cola based 026 0.26 27.2323 26.97 alcoholic beverage waste Source: Jörg Krampe, SA Water Corporation, 2011

CO-DIGESTION IMPLEMENTATION Food Waste Receiving, Storage and Feed System

CO-DIGESTION IMPLEMENTATION Food Waste Receiving, Storage and Feed System

CO-DIGESTION PERFORMANCE RP-1 Digester 4 Volatile Solids Reduction 15-day Running Average % VSR 80% 70% 60% 50% 40% 30% 20% 10% Baseline Operation Manure Foodwaste Codigestion 11% Points Improvement 0% 11/29/2004 1/18/2005 3/9/2005 4/28/2005 6/17/2005 8/6/2005 9/25/2005 11/14/2005 1/3/2006

CO-DIGESTION PERFORMANCE 270 240 210 180 Observed Acclimized System Average Biogas RP-1 Digester 4 Biogas Production Expected Biogas kcfd 150 120 90 60 30 0 Baseline Codigestion

CO-DIGESTION IMPLEMENTATION Slug feeding of digesters not recommended d Monitor delivered waste ph and %TS Mesophilic conditions appears to be less sensitive to feed fluctuations; high activity in thermophilic can result in sour conditions more rapidly Need to consider SRT in digester maximize digestion time while allowing capacity for food waste Sludge dewaterability, gas quality and filtrate quality need to be monitored at full-scale

QUESTIONS? Thanks! WEFTECH 2005