Biobased acrylic acid production in a sugarcane biorefinery: A techno-economic assessment using lactic acid, 3-hydroxypropionic acid and glycerol as intermediates

被引:14
作者
Brobbey, Mensah S. [1 ]
Louw, Jeanne [1 ]
Goergens, Johann F. [1 ]
机构
[1] Stellenbosch Univ, Dept Proc Engn, Private Bag X1, ZA-7602 Matieland, South Africa
基金
新加坡国家研究基金会;
关键词
Acrylic acid; Techno-economic assessment; Greenhouse gas emission; Biorefinery; LIQUID; FERMENTATION; DEHYDRATION; SEPARATION;
D O I
10.1016/j.cherd.2023.03.034
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Acrylic acid (AA) is a versatile platform chemical of immense global demand. Today, the biorefinery is among the most promising initiatives of sustainably producing this commodity from bio-derived precursors. This study evaluated the economic and environmental performance of three production pathways to biobased acrylic acid using sugarcane A-molasses as feedstock. The 3 intermediates were lactic acid (LA), 3-hydroxypropionic acid (3-HP) and glycerol. Production scenarios were simulated in Aspen Plus (R) software and resultant mass and energy flows provided inputs for subsequent estimation of the minimum selling price (MSP) and greenhouse gas (GHG) emissions. The MSP in US $/kgAA and the net GHG in kgCO2/kgAA were the key metrics against which the performance of the developed scenarios were compared. Accordingly, the scenario using LA as intermediate emerged superior with an MSP that was 11 % higher than the actual market price for fossil-based AA. The same had an estimated net GHG emissions of 4.4 kgCO2/kgAA. 3-HP was the second best performing intermediate with an MSP of 2425 US t-1 and green premium of 30 %. The 3-HP pathway, however, had a fairly low yield at fermentation of about 0.51 g LA/g glucose compared to the 1 g LA/gram glucose recorded by the LA pathway. Ultimately, glycerol proved to be an unattractive intermediate owing to a dismal product yield (0.50 g GLY/g glucose) as well as the cost and complexity of glycol recovery from the fermentation soup. (c) 2023 The Author(s). Published by Elsevier Ltd on behalf of Institution of Chemical Engineers. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
引用
收藏
页码:367 / 382
页数:16
相关论文
共 46 条
[1]  
Adkesson D.M., 2005, Patent No. [20050069997, 2005/0069997]
[2]  
Alibaba, 2021, SIL GEL HIGH GRAD ME
[3]   Evaluation of liquid-liquid extraction process for separating acrylic acid produced from renewable sugars [J].
Alvarez, M. E. T. ;
Moraes, E. B. ;
Machado, A. B. ;
Maciel Filho, R. ;
Wolf-Maciel, M. R. .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2007, 137 (1-12) :451-461
[4]   Sustainable Production of Acrylic Acid via 3-Hydroxypropionic Acid from Lignocellulosic Biomass [J].
Bhagwat, Sarang S. ;
Li, Yalin ;
Cortes-Pena, Yoel R. ;
Brace, Emma C. ;
Martin, Teresa A. ;
Zhao, Huimin ;
Guest, Jeremy S. .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2021, 9 (49) :16659-16669
[5]   Gas phase dehydration of lactic acid to acrylic acid over alkaline-earth phosphates catalysts [J].
Blanco, E. ;
Delichere, P. ;
Millet, J. M. M. ;
Loridant, S. .
CATALYSIS TODAY, 2014, 226 :185-191
[6]   ECONOMIC ANALYSIS AND TECHNICALITIES OF ACRYLIC ACID PRODUCTION FROM CRUDE GLYCEROL [J].
Braga, Eduardo Ramos ;
Mustafa, George de Souza ;
Pontes, Danilo de Aguiar ;
Magalhaes Pontes, Luiz Antonio .
CHEMICAL INDUSTRY & CHEMICAL ENGINEERING QUARTERLY, 2020, 26 (01) :59-69
[7]   Process Designs for Converting Propylene Glycol to Acrylic Acid via Lactic Acid and Allyl Alcohol [J].
Buitelaar, M. M. ;
van Daatselaar, E. ;
van Teijlingen, D. G. ;
Stokvis, H., I ;
Wendt, J. D. ;
De Sousa Ribeiro, R. J. ;
Brooks, A. M. M. ;
Kamphuis, E. C. ;
Lopez Montoya, S. ;
van Putten, J. C. ;
van der Ham, A. G. J. ;
van den Berg, H. ;
Lange, J-P .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2020, 59 (03) :1183-1192
[8]   Single-Crystalline-Phase Mo3VOx: An Efficient Catalyst for the Partial Oxidation of Acrolein to Acrylic Acid [J].
Chen, Chen ;
Kosuke, Nakatani ;
Murayama, Toru ;
Ueda, Wataru .
CHEMCATCHEM, 2013, 5 (10) :2869-2873
[9]   Metabolic engineering of Corynebacterium glutamicum for the production of 3-hydroxypropionic acid from glucose and xylose [J].
Chen, Zhen ;
Huang, Jinhai ;
Wu, Yao ;
Wu, Wenjun ;
Zhang, Ye ;
Liu, Dehua .
METABOLIC ENGINEERING, 2017, 39 :151-158
[10]   Techno-Economic Analysis of a Glycerol Biorefinery [J].
D'Angelo, Sebastiano C. ;
Dall'Ara, Agostino ;
Mondelli, Cecilia ;
Perez-Ramirez, Javier ;
Papadokonstantakis, Stavros .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2018, 6 (12) :16563-16572