Elemental nitrogen balance, reaction kinetics and the effect of ethanol on the hydrothermal liquefaction of soy protein

被引:19
作者
Chacon-Parra, Andres [1 ]
Lewis, David [1 ]
van Eyk, Philip [1 ]
机构
[1] Univ Adelaide, Sch Chem Engn & Adv Mat, Adelaide, SA 5005, Australia
基金
澳大利亚研究理事会;
关键词
Hydrothermal liquefaction; Soy protein; Reaction mechanism and kinetics; Elemental nitrogen balance; Nitrogen migration and transformation post-HTL treatment; WATER; MICROALGAE; PRODUCTS; BIOCRUDE; MODEL;
D O I
10.1016/j.cej.2021.130576
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Hydrothermal liquefaction (HTL) is a thermochemical method to convert wet biomass and bio-waste into renewable crude and other valuable products. During HTL, water near critical point acts as a reaction medium and as a catalyst, breaking and hydrolysing bio-macromolecules into smaller compounds which interact and recondense into different components and phases. Proteins as one of the key components in biomass plays a crucial role in the HTL process and products. Proteins are the source of nitrogen content in the HTL renewable crude, which generates environmental problems because of potential NOx emissions from combustion. Proteins also increases the pH of the aqueous phase, as over 60% of contained nitrogen is recovered in the aqueous phase as ammonia, nitrate, and soluble organic nitrogen compounds. However, the nitrogen reaction mechanism and equilibrium under HTL conditions have not been fully understood. In this study, the reaction kinetics for the product phases and nitrogen migration/transformation are elucidated by examining the yields and composition of the renewable crude and aqueous phases of HTL experiments run with a model compound soy protein, in a batch reactor at 250, 300 and 350 degrees C with 15% by mass feedstock. Furthermore, a co-solvent/homogeneous catalyst system has been included as a fully renewable solution to enhance the renewable crude yield, energy recovery, nitrogen content, and clarify the reaction mechanism and kinetic effects.
引用
收藏
页数:12
相关论文
共 32 条
[1]  
Beers KJ, 2007, NUMERICAL METHODS FOR CHEMICAL ENGINEERING: APPLICATIONS IN MATLAB, P1
[2]  
Biller P, 2016, WOODHEAD PUBL SER EN, P509, DOI 10.1016/B978-0-08-100455-5.00017-5
[3]  
Burton F.L., 2013, Wastewater Engineering: Treatment and Resource Recovery
[4]   The effect of ethanol as a homogeneous catalyst on the reaction kinetics of hydrothermal liquefaction of lipids [J].
Chacon-Parra, Andres ;
Lewis, David ;
van Eyk, Philip .
CHEMICAL ENGINEERING JOURNAL, 2021, 414
[5]  
Chen W.-T, 2017, HYDROTHERMAL LIQUEFA
[6]  
Denbigh K., 1981, PRINCIPLES CHEM EQUI, DOI 0.1017/CBO9781139167604
[7]   Strategies for using hydrogen-bond donor/acceptor solvent pairs in developing green chemical processes with supercritical fluids [J].
Duereh, Alif ;
Smith, Richard Lee, Jr. .
JOURNAL OF SUPERCRITICAL FLUIDS, 2018, 141 :182-197
[8]  
Fogler HS, 2020, Elements of chemical reaction engineering
[9]   Hydrogen donor solvents in liquefaction of biomass: A review [J].
Isa, Khairuddin Md ;
Abdullah, Tuan Amran Tuan ;
Ali, Umi Fazara Md .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 81 :1259-1268
[10]   Two-stage hydrothermal liquefaction of a high-protein microalga [J].
Jazrawi, Christopher ;
Biller, Patrick ;
He, Yaya ;
Montoya, Alejandro ;
Ross, Andrew B. ;
Maschmeyer, Thomas ;
Haynes, Brian S. .
ALGAL RESEARCH-BIOMASS BIOFUELS AND BIOPRODUCTS, 2015, 8 :15-22