Energy, carbon dioxide and water use implications of hydrous ethanol production
- 1. Department of Engineering, University of Cambridge, Trumpington Street, Cambridge CB2 1PZ (United Kingdom)
- 2. Department of Mechanical Engineering, University of Minnesota, 111 Church St. SE, Minneapolis, MN 55455 (United States)
- 3. Department of Civil, Environmental and Geo-Engineering, University of Minnesota, 500 Pillsbury Drive, Minneapolis, MN 55455 (United States)
Description
Highlights: • We use a chemical refinery model and exergy analysis to determine the impact of hydrous ethanol. • The process is 70% efficient with 86% of the losses from fermentation, steam generation and drying. • We found that producing 86 wt% ethanol is optimal for thermal energy consumption. • Hydrous ethanol production can reduce energy costs and emissions by ∼8%. • Hydrous ethanol reduces water use by decreasing evaporation in cooling towers. - Abstract: Sub-azeotropic hydrous ethanol has been demonstrated as an effective diesel fuel replacement when used in dual-fuel compression ignition engines. Previous studies have also suggested that hydrous ethanol may be more efficient to produce from corn than anhydrous ethanol. In this study, we investigate corn ethanol production from a dry-mill, natural gas-fired corn ethanol refinery, producing ethanol with a range of ethanol concentrations from 58 wt% to 100 wt% to determine the effect on energy use, water consumption and greenhouse gas (GHG) emissions in the refining stage of the corn ethanol lifecycle. A second law (exergy) analysis of anhydrous ethanol refining revealed the overall process to be 70% efficient, whereby 86% of the exergy losses could be accounted for by three processes: fermentation (34%), steam generation (29%) and distiller's grains and solubles drying (23%). We found that producing 86 wt% ethanol is optimal as thermal energy consumption decreases by a maximum of 10% (from 7.7 MJ/L to 6.9 MJ/L). These savings have the potential to reduce energy costs by approximately 8% ($0.34/L) and reduce refinery emissions by 8% (2 g CO2e/MJ). Production of hydrous ethanol reduced refinery water use due to decreased evaporative losses in the cooling towers, leading to water savings of between 3% and 6% at 86 wt% ethanol.
Availability note (English)
Available from http://dx.doi.org/10.1016/j.enconman.2015.08.039Additional details
Identifiers
- DOI
- 10.1016/j.enconman.2015.08.039;
- PII
- S0196-8904(15)00793-1;
Publishing Information
- Journal Title
- Energy Conversion and Management
- Journal Volume
- 105
- Journal Page Range
- p. 900-907
- ISSN
- 0196-8904
- CODEN
- ECMADL
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 48002788
- Subject category
- S29: ENERGY PLANNING, POLICY AND ECONOMY;
- Descriptors DEI
- CARBON; CARBON DIOXIDE; COMPRESSION; CONCENTRATION RATIO; COOLING TOWERS; DIESEL FUELS; ECONOMICS; ENERGY ACCOUNTING; ENERGY CONSUMPTION; ETHANOL; EXERGY; GAS TURBINES; GREENHOUSE GASES; HEAT; HEAT RECOVERY; NATURAL GAS; NET ENERGY; STEAM GENERATION; STEAM GENERATORS; WATER
- Descriptors DEC
- ACCOUNTING; ALCOHOLS; BOILERS; CARBON COMPOUNDS; CARBON OXIDES; CHALCOGENIDES; DIMENSIONLESS NUMBERS; DISTILLATES; ELEMENTS; ENERGY; ENERGY ANALYSIS; ENERGY RECOVERY; ENERGY SOURCES; EQUIPMENT; FLUIDS; FOSSIL FUELS; FUEL GAS; FUELS; GAS FUELS; GAS OILS; GASES; HYDROGEN COMPOUNDS; HYDROXY COMPOUNDS; LIQUID FUELS; MACHINERY; NONMETALS; ORGANIC COMPOUNDS; OXIDES; OXYGEN COMPOUNDS; PETROLEUM; PETROLEUM DISTILLATES; PETROLEUM FRACTIONS; PETROLEUM PRODUCTS; TURBINES; TURBOMACHINERY; VAPOR GENERATORS
Optional Information
- Copyright
- Copyright (c) 2015 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.