Energy Production from Waste Using The Anaerobic Membrane Bioreactor (AnMBR) Process

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Energy Production from Waste Using The Anaerobic Membrane Bioreactor (AnMBR) Process Peter McCarthy (pjm@adi.ca) ADI Systems Inc. Water Technologies Symposium 2010 (WaterTech 2010) April 21-23, 23, 2010 Fairmont Banff Springs

Acknowledgements Kubota Corporation: Masashi Moro Tetsuya Yamamoto ADI Systems Inc. : ADI Systems Inc. : Scott Christian Shannon Grant

Resource pressures (space, water, energy) ) drive innovation

A form of high-rate anaerobic digestion technology Uses physical membrane barrier to retain biomass Creates renewable energy source in the form of biogas (methane) In full-scale use since 2000, full-scale tests since mid-1990 1990 s Excellent for low flow, highly-concentrated (high COD/BOD/TSS) Compact footprint and simple operation/control AnMBR Technology

Membrane barrier allows for high mixing intensities Organic loading rates of 15 kg/m 3 d on high energy substrates HRT and SRT are dependant upon waste/wastewater type Thermophilic (130 o F/ 55 o C) and mesophilic (100 o F /35 o C) systems Thermophilic results in better removals, more biogas and reduced sludge production) ; membrane overcomes typical thermophilic AD downfall--- solids loss In-situ cleaning; simple citric acid cleaning procedure every 1-31 3 months AnMBR Technology

Anaerobic MBR (AnMBR)

Comparison of Anaerobic Digestion Processes Organic matters Organic matters Methane bacteria Methane bacteria Conventional Anaerobic System Anaerobic MBR System

Applications

Alcohol Stillage

Anaerobic MBR (1 st stage) Aerobic MBR (2 nd stage) Shochu Distillery (distilled spirits from barley and sweet potato) o) ; 20 ton/d

Shochu Distillery (distilled spirits from barley and sweet potato) o) ; 20 ton/d

Shochu Distillery; barley/sweet potato (60 ton/d)

Shochu Distillery; barley/sweet potato (60 ton/d)

Shochu Distillery; barley/sweet potato (60 ton/d)

Shochu Distillery (distilled spirits from barley and sweet potato) Gas holder Biogas flare Shochu Distillery; barley/sweet potato (20 ton/d)

Membrane Basin Anaerobic MBR (1 st stage) Aerobic MBR (2 nd stage) Awamori Distillery, Okinawa; millet/rice (15 ton/d)

Parameter Influent AnMBR Effluent MBR Effluent COD, mg/l 75,000-110,000 1,000 2,500 < 100 BOD, mg/l 63,000-79,000 500 1,500 < 5 TSS, mg/l 25,000-35,000 < 5 < 5 TS, mg/l 35,000 80,000 2,500 5,000 500 1,000 TN, mg/l 2,000 5,500 500 2,500 ** FOG, mg/l 1,600 - < 50 < 5 TP, mg/l 500 1,200 * ** Temp, o F 180-200 130 --- *- less than 20 mg/l can be achieved with chemical addition ** - depends on level of BNR performed Shochu/Awamori Distilleries (barley, sweet potato, rice)

Food Production/Processing Wastes

Confectionary Plant (operational since 2002)

Potato Processing Plant (5.2 ton/d) Operational since Sept.2003

Full-scale energy generation from food processing wastes to date: Confectionary (jellies and beverages) Bean processing Waste dairy (milk processing) products Prepared meals / kitchen food waste Potato processing Salad dressing / BBQ sauce production wastes Any other strong, concentrated wastes would be applicable. Food Production/Processing Wastes

Municipal Garbage

Garbage to energy Nishi-Tenboku Sanitation Center, Hokkaido, Japan

Influent streams to facility: 1.Night soil and septic tank sludge (5,300 gpd) 2.Waste activated sludge from nearby POTW (3 ton/d) 3.Municipal garbage (5 ton/d) Organic municipal garbage is anaerobically digested for energy generation ; high energy substrate (250,000mg/l COD; 20% solids) Garbage to energy

Basic process: 1.Break open bags, separate inorganic material from organic 2.Solubilize solid waste to facilitate fast anaerobic digestion; remove r remaining inorganic materials 3.Anaerobic digestion using AnMBR process 4.Collect, scrub, and store biogas 5.Polish liquid anaerobic effluent in aerobic MBR and discharge 6.Process waste sludge and reclaim as soil additive Garbage to energy

Crush/bag separator (break open and remove bags) Garbage to energy Mix separator (solubilization + inorganics removal)

Anaerobic reactor operates at thermophilic temperatures to maximize solids destruction and biogas production Biogas is utilized to heat reactor and buildings at facility Permeate is polished in aerobic MBR and discharged Aerobic WAS also digested in AnMBR Anaerobic reactor below floor Garbage to energy

Garbage to energy

Garbage to energy

Industrial Wastewater

Anaerobic Reactor ADI- BVF EQ Tank Salad Dressing/BBQ Sauce Manufacturer

AnMBR SBR (now SO tank) First Full-Scale AnMBR in North America and Largest in the World!

Membrane Unit Installation Installed Membranes

Biogas Scour Blowers and SMTs

Ken s s Foods AnMBR Operating Results (First 12 months) Parameter Raw Wastewater Permit Discharge Limits Actual AnMBR Effluent Actual Removals (%) Flow rate (avg), m 3 /d 475 475 -- -- Flow rate (peak), m 3 /d 530 530 -- -- BOD, mg/l BOD, kg/d 18,000 8,600 -- 180 16 5 99.9 COD, mg/l COD, kg/d 39,000 18,500 -- -- 190 62 99.5 99.5 TSS, mg/l TSS, kg/d 12,000 5,700 -- 230 < 1 < 1 100 - FOG, mg/l 1,500 100 < 5 100 ph -- 6-9 7.1 --

High Quality Anaerobic Effluent Effluent Biomass AnMBR Effluent < 25 mg/l BOD < 2 mg/l TSS Biomass 2.0 4.5 % solids 75% volatility

Biogas Production and Utilization AnMBR produces biogas (methane) from the anaerobic digestion process Biogas is utilized in a dual fuel boiler (natural gas + biogas) to produce hot water supply excess biogas is flared at an enclosed flare hot water used for reactor heating (controlled at 35 C), as well as building heat, hot water supply for other in-plant uses Average biogas production: 5,800 m 3 /d biogas produced CH 4 = 60 % CO 2 = 35%, ~ 1% O 2, and 50 ppm H 2 S

Municipal Sewage Sludge

Primary sludge, TS ~ 80% degradable 1) Conventional municipal digester Highly-biodegradable substrate TS = 5% TS = 1% Digested sludge TS = 1% 2) AnMBR system Highly-biodegradable substrate TS = 5% TS = 5% Digested sludge TS = 5% Much smaller reactor; great advantage Solids-free permeate

AnMBR technology holds great promise for some new applications as well: Cellulosic ethanol stillage Stable thermophilic operation allows for digestion of lignins Destruction of designer enzymes before discharge Other fuel ethanol production stillages and syrup (corn/wheat/milo/etc.) Separated MSW (food and garden wastes) Modular, packaged systems (already in use) Many others New Applications

Kubota received the gold medal New Energy Award in 2003, a prize given by the Japanese New Energy Foundation, an extra-departmental body of the Japanese Ministry of Economy, Trade and Industry. Biomass fuel manufacturing Methane fermentation system using submerged membrane Kubota AnMBR technology received the Japanese New Energy Award

Questions or Discussion?