Evaluating industrial drying of cellulosic feedstock for bioenergy: A systems approach
Abstract
Here, a large portion of herbaceous and woody biomass must be dried following harvest. Natural field drying is possible if the weather cooperates. Mechanical drying is a certain way of reducing the moisture content of biomass. This paper presents an engineering analysis applied to drying of 10 Mg h–1 (exit mass flow) of biomass with an initial moisture content ranging from 25% to 70% (wet mass basis) down to 10% exit moisture content. The requirement for hog fuel to supply heat to the dryer increases from 0.5 dry Mg to 3.8 dry Mg h–1 with the increased initial moisture of biomass. The capital cost for the entire drying system including equipment for biomass size reduction, pollution control, dryer, and biomass combustor sums up to more than $4.7 million. The operating cost (electricity, labor, repair, and maintenance) minus fuel cost for the dryer alone amount to 4.05 Mg–1 of dried biomass.
- Authors:
-
- Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States)
- Publication Date:
- Research Org.:
- Oak Ridge National Laboratory (ORNL), Oak Ridge, TN (United States)
- Sponsoring Org.:
- USDOE Office of Energy Efficiency and Renewable Energy (EERE)
- OSTI Identifier:
- 1327646
- Alternate Identifier(s):
- OSTI ID: 1327755
- Grant/Contract Number:
- AC05-00OR22725
- Resource Type:
- Accepted Manuscript
- Journal Name:
- Biofuels, Bioproducts & Biorefining
- Additional Journal Information:
- Journal Volume: 10; Journal Issue: 1; Journal ID: ISSN 1932-104X
- Publisher:
- Wiley
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 09 BIOMASS FUELS; bioenergy feedstocks; biomass dryers; biomass burners; moisture content; humidity ratio; heat energy; drying costs; heat recycling
Citation Formats
Sokhansanj, Shahab, and Webb, Erin. Evaluating industrial drying of cellulosic feedstock for bioenergy: A systems approach. United States: N. p., 2016.
Web. doi:10.1002/bbb.1619.
Sokhansanj, Shahab, & Webb, Erin. Evaluating industrial drying of cellulosic feedstock for bioenergy: A systems approach. United States. https://doi.org/10.1002/bbb.1619
Sokhansanj, Shahab, and Webb, Erin. Thu .
"Evaluating industrial drying of cellulosic feedstock for bioenergy: A systems approach". United States. https://doi.org/10.1002/bbb.1619. https://www.osti.gov/servlets/purl/1327646.
@article{osti_1327646,
title = {Evaluating industrial drying of cellulosic feedstock for bioenergy: A systems approach},
author = {Sokhansanj, Shahab and Webb, Erin},
abstractNote = {Here, a large portion of herbaceous and woody biomass must be dried following harvest. Natural field drying is possible if the weather cooperates. Mechanical drying is a certain way of reducing the moisture content of biomass. This paper presents an engineering analysis applied to drying of 10 Mg h–1 (exit mass flow) of biomass with an initial moisture content ranging from 25% to 70% (wet mass basis) down to 10% exit moisture content. The requirement for hog fuel to supply heat to the dryer increases from 0.5 dry Mg to 3.8 dry Mg h–1 with the increased initial moisture of biomass. The capital cost for the entire drying system including equipment for biomass size reduction, pollution control, dryer, and biomass combustor sums up to more than $4.7 million. The operating cost (electricity, labor, repair, and maintenance) minus fuel cost for the dryer alone amount to 4.05 Mg–1 of dried biomass.},
doi = {10.1002/bbb.1619},
journal = {Biofuels, Bioproducts & Biorefining},
number = 1,
volume = 10,
place = {United States},
year = {Thu Jan 21 00:00:00 EST 2016},
month = {Thu Jan 21 00:00:00 EST 2016}
}
Web of Science
Figures / Tables:
Works referenced in this record:
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journal, May 2010
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Works referencing / citing this record:
Use of Alternative Types of Fuel for Grain Drying
book, January 2019
- Osokina, Nina; Tkachenko, Hennadii; Yevchuk, Yana
- Modern Development Paths of Agricultural Production
Figures / Tables found in this record: