Economic Risk Assessment of Early Stage Designs for Glycerol Valorization in Biorefinery Concepts

被引:38
作者
Gargalo, Carina L. [1 ]
Cheali, Peam [1 ]
Posada, John A. [2 ]
Gernaey, Krist V. [1 ]
Sin, Gurkan [1 ]
机构
[1] Tech Univ Denmark, Dept Chem & Biochem Engn, CAPEC PROC Res Ctr, Bldg 229, DK-2800 Lyngby, Denmark
[2] Delft Univ Technol, Fac Sci Appl, Dept Biotechnol, Sect Biotechnol & Soc, Julianalaan 67, NL-2628 BC Delft, Netherlands
关键词
POLY(3-HYDROXYBUTYRATE) PRODUCTION; TECHNOECONOMIC ANALYSIS; ESCHERICHIA-COLI; CRUDE GLYCEROL; LACTIC-ACID; BY-PRODUCT; FERMENTATION; CONVERSION; BIOENERGY; BIOMASS;
D O I
10.1021/acs.iecr.5b04593
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A systematic methodology to critically assess and screen among early stage design alternatives was developed for the use of glycerol. Through deterministic sensitivity analysis it was found that variations in the product and feedstock prices, total production cost, fixed capital investment, and discount rate, among others, have high impact on the project's profitability analysis. Therefore, the profitability was tested under uncertainties by using NPV and MSP as economic metrics. The robust ranking of solutions is presented with respect to minimum economic risk of the project being nonprofitable (failure to achieve a positive NPV times the consequential profit loss). It was found that the best potential options for glycerol valorization is through the the production of either (0 lactic acid (9 MM$ economic risk with 63% probability of failure to achieve a positive NPV); (ii) succinic acid (14 MM$ economic risk with 76% probability of failure to achieve a positive NPV); or finally, (iii) 1,2-propanediol (16 MM$ economic risk with 68% probability of failure to achieve a positive NPV). As a risk reduction strategy, a multiproduct biorefinery is suggested which is capable of switching between the production of lactic acid and succinic acid. This solution comes with increased capital investment; however, it leads to more robust NPV and decreased economic risk by approximately 20%, therefore creating a production plant that can continuously adapt to market forces and thus optimize profitability.
引用
收藏
页码:6801 / 6814
页数:14
相关论文
共 64 条
  • [31] A Comparative Review of Petroleum-Based and Bio-Based Acrolein Production
    Liu, Lu
    Ye, X. Philip
    Bozell, Joseph J.
    [J]. CHEMSUSCHEM, 2012, 5 (07) : 1162 - 1180
  • [32] Molel E, 2015, 1 2 PROPANEDIOL CRUD
  • [33] Metabolic engineering for the microbial production of 1,3-propanediol
    Nakamura, CE
    Whited, GM
    [J]. CURRENT OPINION IN BIOTECHNOLOGY, 2003, 14 (05) : 454 - 459
  • [34] Nguyen N., 2013, J. Sustain. Bioenergy Syst, V3, P209, DOI DOI 10.4236/JSBS.2013.33029
  • [35] Techno-economics of carbon preserving butanol production using a combined fermentative and catalytic approach
    Nilsson, Robert
    Bauer, Fredric
    Mesfun, Sennai
    Hulteberg, Christian
    Lundgren, Joakim
    Wannstrom, Sune
    Rova, Ulrika
    Berglund, Kris Arvid
    [J]. BIORESOURCE TECHNOLOGY, 2014, 161 : 263 - 269
  • [36] Peters M. S., 2003, PLANT DESIGN EC CHEM, V4
  • [37] Analysis of the Production Process of Optically Pure D-Lactic Acid from Raw Glycerol Using Engineered Escherichia coli Strains
    Posada, John A.
    Cardona, Carlos A.
    Gonzalez, Ramon
    [J]. APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2012, 166 (03) : 680 - 699
  • [38] Reinhardt A, 2012, SUST INTERNET ICT
  • [39] Roland-Holst David., 2013, Bioplastics in California
  • [40] The role of biomass and bioenergy in a future bioeconomy: Policies and facts
    Scarlat, Nicolae
    Dallemand, Jean-Francois
    Monforti-Ferrario, Fabio
    Nita, Viorel
    [J]. ENVIRONMENTAL DEVELOPMENT, 2015, 15 : 3 - 34