Viscosity Variation of Model Compounds during Hydrothermal Liquefaction under Subcritical Conditions of Water

Author(s):  
Sylvia Y. Edifor ◽  
Quoc D. Nguyen ◽  
Philip van Eyk ◽  
Patrick Biller ◽  
Tony Hall ◽  
...  
Processes ◽  
2021 ◽  
Vol 9 (7) ◽  
pp. 1172
Author(s):  
Leonard Moser ◽  
Christina Penke ◽  
Valentin Batteiger

One of the more promising technologies for future renewable fuel production from biomass is hydrothermal liquefaction (HTL). Although enormous progress in the context of continuous experiments on demonstration plants has been made in the last years, still many research questions concerning the understanding of the HTL reaction network remain unanswered. In this study, a unique process model of an HTL process chain has been developed in Aspen Plus® for three feedstock, microalgae, sewage sludge and wheat straw. A process chain consisting of HTL, hydrotreatment (HT) and catalytic hydrothermal gasification (cHTG) build the core process steps of the model, which uses 51 model compounds representing the hydrolysis products of the different biochemical groups lipids, proteins, carbohydrates, lignin, extractives and ash for modeling the biomass. Two extensive reaction networks of 272 and 290 reactions for the HTL and HT process step, respectively, lead to the intermediate biocrude (~200 model compounds) and the final upgraded biocrude product (~130 model compounds). The model can reproduce important characteristics, such as yields, elemental analyses, boiling point distribution, product fractions, density and higher heating values of experimental results from continuous experiments as well as literature values. The model can be applied as basis for techno-economic and environmental assessments of HTL fuel production, and may be further developed into a predictive yield modeling tool.


2020 ◽  
Vol 22 (23) ◽  
pp. 8210-8232
Author(s):  
Chuang Yang ◽  
Shuzhong Wang ◽  
Jianqiao Yang ◽  
Donghai Xu ◽  
Yanhui Li ◽  
...  

Catalytic hydrotreatment of HTL biocrude oil, SCWG of biomass, and hydrothermal conversion of model compounds are reviewed.


2016 ◽  
Vol 30 (12) ◽  
pp. 10470-10483 ◽  
Author(s):  
René B. Madsen ◽  
Patrick Biller ◽  
Mads M. Jensen ◽  
Jacob Becker ◽  
Bo B. Iversen ◽  
...  

Fuel ◽  
2019 ◽  
Vol 240 ◽  
pp. 169-178 ◽  
Author(s):  
Aisha Matayeva ◽  
Daniele Bianchi ◽  
Stefano Chiaberge ◽  
Fabrizio Cavani ◽  
Francesco Basile

2016 ◽  
Vol 54 ◽  
pp. 1632-1652 ◽  
Author(s):  
Maxime Déniel ◽  
Geert Haarlemmer ◽  
Anne Roubaud ◽  
Elsa Weiss-Hortala ◽  
Jacques Fages

2022 ◽  
Vol 6 (1) ◽  
pp. 2
Author(s):  
Morgane Briand ◽  
Geert Haarlemmer ◽  
Anne Roubaud ◽  
Pascal Fongarland

Hydrothermal liquefaction has proven itself as a promising pathway to the valorisation of low-value wet food residues. The chemistry is complex and many questions remain about the underlying mechanism of the transformation. Little is known about the heat of reaction, or even the thermal effects, of the hydrothermal liquefaction of real biomass and its constituents. This paper explores different methods to evaluate the heat released during the liquefaction of blackcurrant pomace and brewers’ spent grains. Some model compounds have also been evaluated, such as lignin, cellulose and glutamic acid. Exothermic behaviour was observed for blackcurrant pomace and brewers’ spent grains. Results obtained in a continuous reactor are similar to those obtained in a batch reactor. The heat release has been estimated between 1 MJ/kg and 3 MJ/kg for blackcurrant pomace and brewers’ spent grains, respectively. Liquefaction of cellulose and glucose also exhibit exothermic behaviour, while the transformation of lignin and glutamic acid present a slightly endothermic behaviour.


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