ABE production from corn: a recent economic evaluation

被引:132
作者
Qureshi, N [1 ]
Blaschek, HP [1 ]
机构
[1] Univ Illinois, Dept Food Sci & Human Nutr, Biotechnol & Bioengn Grp, Urbana, IL 61801 USA
关键词
Clostridium beijerinckii BA101; acetone-butanol-ethanol (ABE); yield; capital cost; plant; corn steep liquor (CSL); fermentation;
D O I
10.1038/sj.jim.7000123
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
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).
引用
收藏
页码:292 / 297
页数:6
相关论文
共 27 条
[1]   Acetate enhances solvent production and prevents degeneration in Clostridium beijerinckii BA101 [J].
Chen, CK ;
Blaschek, HP .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1999, 52 (02) :170-173
[2]   Enhanced butanol production by Clostridium beijerinckii BA101 grown in semidefined P2 medium containing 6 percent maltodextrin or glucose [J].
Formanek, J ;
Mackie, R ;
Blaschek, HP .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 1997, 63 (06) :2306-2310
[3]   ACETONE-BUTANOL FERMENTATION REVISITED [J].
JONES, DT ;
WOODS, DR .
MICROBIOLOGICAL REVIEWS, 1986, 50 (04) :484-524
[4]   FERMENTATION-DERIVED BUTANOL AND SCENARIOS FOR ITS USES IN ENERGY-RELATED APPLICATIONS [J].
LADISCH, MR .
ENZYME AND MICROBIAL TECHNOLOGY, 1991, 13 (03) :280-283
[6]   PRICE SENSITIVITY OF BIOETHANOL PRODUCED IN NEW ZEALAND FROM PINUS-RADIATA WOOD [J].
MANDERSON, GJ ;
SPENCER, K ;
PATERSON, AHJ ;
QURESHI, N ;
JANSSEN, DE .
ENERGY SOURCES, 1989, 11 (03) :135-150
[7]   ACETONE-BUTANOL FERMENTATION PROCESS-DEVELOPMENT AND ECONOMIC-EVALUATION [J].
MARLATT, JA ;
DATTA, R .
BIOTECHNOLOGY PROGRESS, 1986, 2 (01) :23-28
[8]  
MISTRY A, 1991, THESIS U ILLINOIS UR
[9]  
MOREIRA AR, 1983, ORGANIC CHEM BIOMASS, P385
[10]  
NELSON DL, 1979, KIRKOTHMER ENCY CHEM, V1, P179