The design and techno economic analysis of a succinic acid production facility
Succinic acid is an industrially important commodity chemical that acts as a precursor to numerous other chemicals. This article explores an alternative biochemical route (as opposed to the traditional route from petroleum), by modeling a succinic acid production plant using Actinobacillus succinoge...
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| Published in: | Frontiers in sustainability (Lausanne) Vol. 3 |
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| Main Authors: | , , , , , |
| Format: | Journal Article |
| Language: | English |
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Frontiers Media S.A
16-08-2022
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| Abstract | Succinic acid is an industrially important commodity chemical that acts as a precursor to numerous other chemicals. This article explores an alternative biochemical route (as opposed to the traditional route from petroleum), by modeling a succinic acid production plant using
Actinobacillus succinogenes
, to convert the renewable sugars of corn stover feedstock. The model developed with SuperPro Designer v9.0 was used to evaluate the feasibility of this approach. This design is on par with the throughput of currentlarge scale manufacturers, by achieving an annual production rate of 11.5 US kilotons of succinic acid. The plant's economic standing is very attractive with a payback time of just under 5 years and return on investment of 20.4%. This article shows a facility design that maximizes profitability for a feasible and sustainable solution for bio-based succinic acid production. |
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| AbstractList | Succinic acid is an industrially important commodity chemical that acts as a precursor to numerous other chemicals. This article explores an alternative biochemical route (as opposed to the traditional route from petroleum), by modeling a succinic acid production plant using
Actinobacillus succinogenes
, to convert the renewable sugars of corn stover feedstock. The model developed with SuperPro Designer v9.0 was used to evaluate the feasibility of this approach. This design is on par with the throughput of currentlarge scale manufacturers, by achieving an annual production rate of 11.5 US kilotons of succinic acid. The plant's economic standing is very attractive with a payback time of just under 5 years and return on investment of 20.4%. This article shows a facility design that maximizes profitability for a feasible and sustainable solution for bio-based succinic acid production. Succinic acid is an industrially important commodity chemical that acts as a precursor to numerous other chemicals. This article explores an alternative biochemical route (as opposed to the traditional route from petroleum), by modeling a succinic acid production plant using Actinobacillus succinogenes, to convert the renewable sugars of corn stover feedstock. The model developed with SuperPro Designer v9.0 was used to evaluate the feasibility of this approach. This design is on par with the throughput of currentlarge scale manufacturers, by achieving an annual production rate of 11.5 US kilotons of succinic acid. The plant's economic standing is very attractive with a payback time of just under 5 years and return on investment of 20.4%. This article shows a facility design that maximizes profitability for a feasible and sustainable solution for bio-based succinic acid production. |
| Author | Shaikh, Faisal Tomczyk, Sarah Ozturk, Serdar Wawrzyniak, Thomas Tessman, Monica Ehrlich, Christopher |
| Author_xml | – sequence: 1 givenname: Sarah surname: Tomczyk fullname: Tomczyk, Sarah – sequence: 2 givenname: Serdar surname: Ozturk fullname: Ozturk, Serdar – sequence: 3 givenname: Thomas surname: Wawrzyniak fullname: Wawrzyniak, Thomas – sequence: 4 givenname: Monica surname: Tessman fullname: Tessman, Monica – sequence: 5 givenname: Christopher surname: Ehrlich fullname: Ehrlich, Christopher – sequence: 6 givenname: Faisal surname: Shaikh fullname: Shaikh, Faisal |
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| Cites_doi | 10.1016/j.wasman.2021.04.013 10.1128/aem.57.10.3013-3019.1991 10.1007/s00253-012-4214-x 10.1016/j.jclepro.2016.08.104 10.1007/s10098-016-1309-6 10.1099/00207713-49-1-207 10.1016/j.seppur.2010.02.021 10.1128/AEM.71.11.6651-6656.2005 10.1186/1754-6834-7-23 10.1016/j.fuproc.2009.05.018 10.1016/j.biortech.2011.02.093 10.1016/j.fbp.2013.09.001 10.1002/bbb.1427 10.1016/j.biortech.2010.05.016 10.3390/pr9060958 10.1039/b913021g 10.1002/bbb.269 10.1016/j.jclepro.2019.05.180 10.1016/j.seppur.2014.09.034 10.1186/s13068-015-0363-3 |
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| References | Li (B16); 102 B21 B25 Li (B17); 72 B26 Guettler (B13) 1999; 49 Lin (B18) 2010; 12 Cok (B8) 2013; 8 Cheng (B6) 2012; 95 Biddy (B4) 2016 Gadkari (B10) 2021; 126 Moussa (B20) 2016; 139 Gu (B12) 2014; 138 Dickinson (B9) 2017; 19 Bradfield (B5) 2015; 8 McKinlay (B19) 2005; 71 Simchick (B24) 2021; 9 Hallac (B14) 2011; 5 Zhao (B27) 2009; 90 Clark (B7) 2014 Samuelov (B22) 1991; 57 B1 B2 B3 Zheng (B28) 2010; 101 Shekiro (B23) 2014; 7 Lam (B15) 2014; 92 Ghayur (B11) 2019; 230 |
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