Biobased propylene and acrylonitrile production in a sugarcane biorefinery: Identification of preferred production routes via techno-economic and environmental assessments

被引:2
作者
Rode, Lukhanyo [1 ]
Bosman, Catharine Elizabeth [1 ]
Louw, Jeanne [1 ]
Petersen, Abdul [1 ]
Ghods, Nosaibeh Nosrati [1 ]
Gorgens, Johann Ferdinand [1 ]
机构
[1] Stellenbosch Univ, Dept Chem Engn, Private Bag X1, ZA-7602 Matieland, South Africa
基金
新加坡国家研究基金会;
关键词
Bio-based propylene; Bio-based acrylonitrile; Ethanol intermediate; Techno-economic analysis; Greenhouse gas emission; 3-HYDROXYPROPIONIC ACID; LACTIC-ACID; PATHWAYS;
D O I
10.1016/j.biombioe.2024.107399
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Four alternative, sugar-derived chemical intermediates were compared for the production of propylene and acrylonitrile in energy self-sufficient biorefineries, annexed to an existing sugarcane mill, to assess economic feasibility and environmental sustainability. Aspen Plus (R) process simulations considered ethanol and isopropanol produced from A-molasses as intermediates for propylene production, while propylene and 3-hydroxypropionic acid (3-HP) from A-molasses were compared for acrylonitrile production. The minimum selling prices (MSPs) for propylene-from-ethanol (3634 $/t), propylene-from-isopropanol (8151 $/t), acrylonitrile-from propylene (4698 $/t), and acrylonitrile-from-3-HP (5957 $/t) were 280 %, 752 %, 302 % and 409 % above the market prices of fossil-based equivalents. Nonetheless, the propylene biorefineries achieved up to 97 % reduction in greenhouse gas (GHG) emissions, whilst acrylonitrile biorefineries had up to 43 % reduction compared to fossil-based production processes. Based on process yields, energy demand and GHG emissions, ethanol was identified as the preferred intermediate route for all four biorefinery scenarios, while substantial price-premiums will be required for industrial production.
引用
收藏
页数:14
相关论文
共 49 条
[1]  
Alexandre C.S.B., 2008, Acrylonitrile by PropeneAmmoxidation, P313, DOI [10.1002/9783527621583.ch11, DOI 10.1002/9783527621583.CH11]
[2]  
Australian Cane Farmers Association, 2020, Sugar Mills
[3]  
Berg L., 1998, Separation of Ethanol, Isopropanol and Water Mixtures by Extractive Distillation, V5, P800
[4]  
BlueWeave Consulting, 2022, Global Propylene Market to Boost in Coming Years - Projected to Reach 132.1 Metric Tons in 2028, at a CAGR of 6.1% during Forecast Period
[5]  
Bratu MG, 2008, SCI STUDY RES-CHEM C, V9, P109
[6]   Biobased acrylic acid production in a sugarcane biorefinery: A techno-economic assessment using lactic acid, 3-hydroxypropionic acid and glycerol as intermediates [J].
Brobbey, Mensah S. ;
Louw, Jeanne ;
Goergens, Johann F. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2023, 193 :367-382
[7]  
ChemAnalyst, 2022, Chemical Prices
[8]   Kinetics of aqueous-phase hydrogenation of organic acids and their mixtures over carbon supported ruthenium catalyst [J].
Chen, Yuqing ;
Miller, Dennis J. ;
Jackson, James E. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (10) :3334-3340
[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]  
Coupard V., 2015, Process for Dehydration of Ethanol into Ethylene with Low Energy Consumption, V9, P85