Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis

A readily available source for renewable fuels and chemicals is corn stover, which consists of the leftover stalks, leaves, husks, and cobs from the corn plant and makes up nearly half of the yield of a corn crop. Common practice is to pretreat it with sulfuric acid to break down the hemicellulose,...

Full description

Bibliographic Details
Main Authors: Andrew Kohler, Wayne Seames, Cassandra Shaffer, Cara Bjerke, Jacob Dahl
Format: Article
Language:English
Published: MDPI AG 2021-02-01
Series:Processes
Subjects:
Online Access:https://www.mdpi.com/2227-9717/9/3/436
id doaj-445410b0140d4db99d6aeb272f80aded
record_format Article
spelling doaj-445410b0140d4db99d6aeb272f80aded2021-03-01T00:02:36ZengMDPI AGProcesses2227-97172021-02-01943643610.3390/pr9030436Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta CatalysisAndrew Kohler0Wayne Seames1Cassandra Shaffer2Cara Bjerke3Jacob Dahl4Iowa State University, Ames, IA 50011, USADepartment of Chemical Engineering, University of North Dakota, Grand Forks, ND 58202, USADepartment of Chemical Engineering, University of North Dakota, Grand Forks, ND 58202, USADepartment of Chemical Engineering, University of North Dakota, Grand Forks, ND 58202, USADepartment of Chemical Engineering, University of North Dakota, Grand Forks, ND 58202, USAA readily available source for renewable fuels and chemicals is corn stover, which consists of the leftover stalks, leaves, husks, and cobs from the corn plant and makes up nearly half of the yield of a corn crop. Common practice is to pretreat it with sulfuric acid to break down the hemicellulose, releasing xylose, followed by enzymatic hydrolysis to convert the cellulose into glucose. Using a Sn-Beta catalyst, it is possible to convert these monomeric sugars into lactic, levulinic, formic, and acetic acids. This paper presents the results of a techno-economic analysis (TEA) of the commercial feasibility of producing these acids from corn stover. Two preliminary process designs were evaluated which represent two separate reaction yields: a balanced yield of both lactic and levulinic acids and the yields from a co-catalysis with CaSO<sub>4</sub> to produce primarily lactic acid. Both process designs are scaled to process 230,000 MT/y of corn stover. An AACS Class 4 factored broad capital cost estimate and comparable estimates of operating costs and revenues were used to generate cash flow sheets to evaluate the economic feasibility of both options. The balanced product process has an estimated NPV@20% = 3.3 million USD ± 40%, while the CaSO<sub>4</sub>-facilited process has an NPV@20% = 110 million USD ± 40% (January 2019 basis). A major hurdle for both processes is the demand for levulinic acid. The balanced product process will produce 135% of the expected global demand and the CaSO<sub>4</sub>-facilitated alternative will meet 31% of the demand. For the demand to meet production, advances in levulinic acid applications are needed. However, the attractive economics suggest that these technologies warrant further development towards commercialization.https://www.mdpi.com/2227-9717/9/3/436renewable fuelsrenewable chemicalslactic acidlevulinic acidtechno-economic analysis
collection DOAJ
language English
format Article
sources DOAJ
author Andrew Kohler
Wayne Seames
Cassandra Shaffer
Cara Bjerke
Jacob Dahl
spellingShingle Andrew Kohler
Wayne Seames
Cassandra Shaffer
Cara Bjerke
Jacob Dahl
Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis
Processes
renewable fuels
renewable chemicals
lactic acid
levulinic acid
techno-economic analysis
author_facet Andrew Kohler
Wayne Seames
Cassandra Shaffer
Cara Bjerke
Jacob Dahl
author_sort Andrew Kohler
title Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis
title_short Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis
title_full Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis
title_fullStr Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis
title_full_unstemmed Techno-Economic Analysis of a Process for the Aqueous Conversion of Corn Stover into Lactic and Levulinic Acid through Sn-Beta Catalysis
title_sort techno-economic analysis of a process for the aqueous conversion of corn stover into lactic and levulinic acid through sn-beta catalysis
publisher MDPI AG
series Processes
issn 2227-9717
publishDate 2021-02-01
description A readily available source for renewable fuels and chemicals is corn stover, which consists of the leftover stalks, leaves, husks, and cobs from the corn plant and makes up nearly half of the yield of a corn crop. Common practice is to pretreat it with sulfuric acid to break down the hemicellulose, releasing xylose, followed by enzymatic hydrolysis to convert the cellulose into glucose. Using a Sn-Beta catalyst, it is possible to convert these monomeric sugars into lactic, levulinic, formic, and acetic acids. This paper presents the results of a techno-economic analysis (TEA) of the commercial feasibility of producing these acids from corn stover. Two preliminary process designs were evaluated which represent two separate reaction yields: a balanced yield of both lactic and levulinic acids and the yields from a co-catalysis with CaSO<sub>4</sub> to produce primarily lactic acid. Both process designs are scaled to process 230,000 MT/y of corn stover. An AACS Class 4 factored broad capital cost estimate and comparable estimates of operating costs and revenues were used to generate cash flow sheets to evaluate the economic feasibility of both options. The balanced product process has an estimated NPV@20% = 3.3 million USD ± 40%, while the CaSO<sub>4</sub>-facilited process has an NPV@20% = 110 million USD ± 40% (January 2019 basis). A major hurdle for both processes is the demand for levulinic acid. The balanced product process will produce 135% of the expected global demand and the CaSO<sub>4</sub>-facilitated alternative will meet 31% of the demand. For the demand to meet production, advances in levulinic acid applications are needed. However, the attractive economics suggest that these technologies warrant further development towards commercialization.
topic renewable fuels
renewable chemicals
lactic acid
levulinic acid
techno-economic analysis
url https://www.mdpi.com/2227-9717/9/3/436
work_keys_str_mv AT andrewkohler technoeconomicanalysisofaprocessfortheaqueousconversionofcornstoverintolacticandlevulinicacidthroughsnbetacatalysis
AT wayneseames technoeconomicanalysisofaprocessfortheaqueousconversionofcornstoverintolacticandlevulinicacidthroughsnbetacatalysis
AT cassandrashaffer technoeconomicanalysisofaprocessfortheaqueousconversionofcornstoverintolacticandlevulinicacidthroughsnbetacatalysis
AT carabjerke technoeconomicanalysisofaprocessfortheaqueousconversionofcornstoverintolacticandlevulinicacidthroughsnbetacatalysis
AT jacobdahl technoeconomicanalysisofaprocessfortheaqueousconversionofcornstoverintolacticandlevulinicacidthroughsnbetacatalysis
_version_ 1724247248355721216