Profitability in Digester Gas: The 16-mgd James A. Loughlin, Jr., WWTP
Client: Cape Fear Public Utility Authority
Location: Wilmington, NC
Of the 16,000 centralized wastewater treatment facilities in the United States, approximately 3,500 utilize anaerobic digestion for residuals stabilization, and only about two percent (~70) use digester gas to produce electricity. A Hazen and Sawyer study revealed that, using the appropriate equipment, the Cape Fear Public Utility Authority’s (CFPUA) 16-mgd James A. Loughlin, Jr., WWTP could turn digester gas into electrical energy at a profit - creating $2.40 of present value with each dollar of invested capital – while simultaneously reducing greenhouse gases by tapping a readily available renewable energy resource.
Project Outcomes and Benefits
- The recommended process configuration offers CFPUA an incremental benefit-to-cost ratio of 2.40 (i.e., each dollar of invested capital would create $2.40 of present value).
- Utilization of digester gas as a renewable energy power source for electrical power production results in reduced greenhouse gas emissions.
Increasing public demands for “green energy,” combined with and economic and regulatory actions in some regions to enact mandatory renewable energy portfolio standards (REPS) are now helping to make waste-to-energy projects increasingly attractive for many facilities. These projects can offer both environmental and economic benefits, compared to the current and most common practice of only capturing biogas energy for process heating and flaring surplus biogas when process heating demands have been meet.
We developed a Lifecycle Cost Analysis (LCA) for two energy recovery alternatives for the purpose of determining which option, energy generation with heat recovery (CHP) or energy generation without heat recovery (non-CHP), would provide the greatest return on investment for CFPUA. The LCA includes an assessment of the following components:
- Facility Capital Cost
- Net Present Operation and Maintenance Costs
- Net Present Value Created
Net present value and benefits were developed for both alternatives, with consideration given to estimating average seasonal heating demands for the anaerobic digestion unit process and the available digester gas production for operation at flows ranging from 10-mgd to 16-mgd. Operating costs and benefits were estimated for both energy recovery system configurations, based on a 20-year straight line increase in flow to the CFPUA James A. Loughlin WWTP.
Both process configurations, non-CHP and CHP, will generate positive economic value based on the lifecycle cost assessment and have an internal rate of return greater than the Owner’s estimated cost of capital (5.5%). Estimated GHG emissions reductions would range from approximately 890 ton CO2 equivalents (tCO2e) per year under current capacity conditions (10 mgd), for a system configured to operate in the non-CHP mode, to approximately 2,670 tCO2e per year under future operating conditions (16 mgd) in a full combined heat and power configuration.
Results of this analysis clearly demonstrated that installation of a full CHP digester gas to energy recovery project would have the higher return on invested capital and simultaneously result in a greater reduction in greenhouse gas emissions than the non-CHP alternative.
For more information on this project, or to discuss a similar project in your area, contactC. Michael Bullard, P.E. at email@example.com