Journal
JOURNAL OF INDUSTRIAL MICROBIOLOGY & BIOTECHNOLOGY
Volume 27, Issue 5, Pages 292-297Publisher
OXFORD UNIV PRESS
DOI: 10.1038/sj.jim.7000123
Keywords
Clostridium beijerinckii BA101; acetone-butanol-ethanol (ABE); yield; capital cost; plant; corn steep liquor (CSL); fermentation
Categories
Ask authors/readers for more resources
This article details an economic assessment of butanol production from corn using the newly developed hyperbutanol-producing strain of Clostridium beijerinckii BA101. Butanol is produced in batch reactors and recovered by distillation. For a plant with 153,000 metric tons of acetone, butanol, and ethanol (ABE) production capacity, the production equipment cost and total working capital cost is US$33.47. x 10(6) and US$110.46 x 10(6), respectively. Based on a corn price (C-p) of US$79.23 ton(-1) (US$2.01 bushel(-1)), an ABE yield of 0.42 (g ABE/g glucose) butanol price is projected to be US$0.34 kg(-1). An improved yield of 0.50 will reduce this price to US$0.29 kg(-1). Assumptions, such as by-product credit for gases and complete conversion of corn steep liquor (CSL) to fermentation by-products, have been taken into consideration. An increased price of corn to US$197.10 ton(-1) would result in a butanol price of US$0.47 kg(-1). A grass-rooted plant would result in a butanol price of US$0.73 kg(-1) (C-p US$79.23 ton(-1)). In a worst case scenario, the price of butanol would increase to US$1.07 kg(-1) (C-p 197.10 ton(-1) for a grass-rooted plant and assuming no credit for gases). This is based on the assumption that corn price would not increase to more than US$197.10 ton(-1).
Authors
I am an author on this paper
Click your name to claim this paper and add it to your profile.
Reviews
Recommended
No Data Available