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Anaerobic Digestion of Agri-food Processing By-Products

Anaerobic Digestion of Agri-food Processing By-Products

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Presented <strong>By</strong>: Keith Wilson, President, EEC Energy Corp.<br />

April 13, 2007


‣ Introduction<br />

‣ <strong>Agri</strong>-<strong>food</strong> <strong>Processing</strong> <strong>By</strong>-<strong>Products</strong> in Ontario – an Untapped<br />

Energy Source<br />

‣ The ADvantage System <strong>Anaerobic</strong> Digester – Overview<br />

‣ EEC Energy Grain Handling <strong>By</strong>-products Test


According to a study by the Ontario Ministry <strong>of</strong> <strong>Agri</strong>culture and Rural<br />

Affairs (OMAFRA), there is almost 2,300,000 tonnes <strong>of</strong> organic waste<br />

produced by agri-<strong>food</strong> companies in Ontario annually. The potential energy<br />

value <strong>of</strong> that organic waste processed by AD translates into:<br />

‣ Over 3.6 Million Megawatts <strong>of</strong> Electricity Annually<br />

‣ Over 5 Million Megawatts <strong>of</strong> Thermal Energy Annually (using CHP units)<br />

EEC Energy estimates that today’s energy value <strong>of</strong> the Biogas from that waste<br />

is almost 100,000 Gigajoules annually.


Types <strong>of</strong> organic material for AD Systems:<br />

Food <strong>Processing</strong>:<br />

Fruit & Vegetable <strong>Processing</strong><br />

Brewery Waste<br />

Malt Plant Waste<br />

Abattoirs<br />

Sugar <strong>Processing</strong><br />

<strong>Agri</strong>cultural:<br />

Dairy<br />

Poultry<br />

Crop & Crop Residuals<br />

Municipal/Industrial:<br />

Sewage Sludge (after treatment)<br />

Organic Landfill Waste<br />

Restaurant Waste (fats/oils)<br />

Grain Elevators<br />

Dairy/Cheese <strong>Processing</strong><br />

Corn & Potato <strong>Processing</strong><br />

Fish <strong>Processing</strong><br />

Beef<br />

Swine<br />

Silage<br />

“Wet” Kitchen Waste<br />

Lagoon Treatment


Unique Features and Benefits:<br />

‣ Modular Design<br />

‣ Easily expandable to handle increased waste volumes<br />

‣ Processes different waste streams in separate digesters<br />

‣ Completely automated – on or <strong>of</strong>f-site control and monitoring<br />

‣ Flexible design – digesters are<br />

standard, complete flexibility to<br />

integrate front & back-end<br />

processing into current operations<br />

‣ Indoor operation – mitigate odours<br />

associated with digestate handling


Unique Features and Benefits:<br />

‣ High Temperature Operation - 55° to 60° Celsius<br />

‣ Shorter Hydraulic Retention Time (HRT) – typically 4-7 days<br />

‣ Complete Pathogen Destruction Rate (99.999%)<br />

‣ 2/3 Less Digester Volume required compared to Mesophilic systems<br />

‣ Increased biogas yields – typically 20-25% higher than Mesophilic<br />

‣ Increased biogas quality at 650-750 BTU’s/ft3


In 2005, EEC Energy<br />

began the R & D<br />

Project to test the<br />

energy potential and<br />

business case for<br />

operating an AD<br />

System on grain dust<br />

from the local grain<br />

handling industry


TEST PURPOSE:<br />

To determine the latent energy potential (in Therms/Ton) through anaerobic digestion<br />

<strong>of</strong> pelletized barley dust as a sole substrate, as supplied by a local grain-handling<br />

facility<br />

TEST PARAMETERS:<br />

The following tests were performed and recorded:<br />

‣ Temperature, pressure and PH <strong>of</strong> blend tank, digester and biogas<br />

‣ Quantity, quality and BTU value <strong>of</strong> biogas production<br />

‣ Solids recovery from digestate<br />

TEST TIMELINE:<br />

The barley substrate was first introduced into the digester on Sept. 11/05. The<br />

digester was gradually weaned <strong>of</strong>f manure and onto the new substrate over the<br />

next few weeks.


OBSERVATIONS:<br />

‣ The digestion <strong>of</strong> the infeed was immediate and very fast<br />

‣ In the 2 hour period following the batch infeed, excess biogas was generated<br />

‣ Also, during this time, the boiler could not consume all the biogas being<br />

generated and the excess was vented to atmosphere through the safety stack.<br />

‣ During this first 2 hours, the boiler temperature did not rise relative to the extra<br />

gas being consumed and in fact, it occasionally dropped.<br />

‣ There was little recoverable solids from the digester.<br />

‣ Even though there was a large recycled digestate component to the infeed, the<br />

pH <strong>of</strong> the digester remained stable.


Biogas Production (cu.ft./# Infeed)<br />

(8.66 Avg.)<br />

Cu. Ft. Biogas<br />

14<br />

12<br />

10<br />

8<br />

6<br />

4<br />

2<br />

0<br />

1 3 5 7 9 11 13 15 17 19 21 23<br />

Hours from Infeed


Biogas Production (BTU's/Cu.Ft.)<br />

(692 Avg.)<br />

BTU's/Cu.Ft.<br />

900<br />

800<br />

700<br />

600<br />

500<br />

400<br />

300<br />

200<br />

100<br />

0<br />

1 3 5 7 9 11 13 15 17 19 21 23<br />

Hours from Infeed


Biogas Production (Therms/Ton)<br />

(122 Avg.)<br />

Therms/Ton Infeed<br />

250<br />

200<br />

150<br />

100<br />

50<br />

0<br />

1 3 5 7 9 11 13 15 17 19 21 23<br />

Hours from Infeed


The results <strong>of</strong><br />

our research<br />

demonstrate a<br />

strong case for<br />

grain waste as a<br />

feedstock for AD<br />

Systems!

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