Abstract
As CO2 plays a central role in the economics of microalgae cultivation, an accurate estimate of its cost is essential. Toward this end, an economic model was developed for CO2 recovery from power-plant flue gas and its delivery to microalgae ponds. A design basis was devised for recovering CO2 from flue gas emitted by a typical 500 MW power plant located in the Southwestern United States. For thestandard process, which included monoethanolamine (MEA) extraction, compression, dehydration, and evaluate the efficacy of directly uising the flue gas, however, this option was found to be more expensive. The economics of microalgae cultivation using power-plant flue gas can be evaluated by integrating this model for CO2 recovery with a previously developed model for microalgae cultivation. Themodel predictions for a long-term process are : a lipid cost of $1.4/gal (unextracted) ane a mitigation cost of $30/t CO2 (CO2 avoided basis). These costs are economically attractive and demonstrate the promise of microalgae technology.
Original language | American English |
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Pages (from-to) | S505-S510 |
Journal | Energy Conversion and Management |
Volume | 38 |
Issue number | Suppl. |
DOIs | |
State | Published - 1997 |
NREL Publication Number
- NREL/JA-427-21536