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Frontiers in Energy

ISSN 2095-1701

ISSN 2095-1698(Online)

CN 11-6017/TK

Postal Subscription Code 80-972

2018 Impact Factor: 1.701

Front. Energy    2023, Vol. 17 Issue (5) : 635-653    https://doi.org/10.1007/s11708-023-0878-4
REVIEW ARTICLE
Selective preparation for biofuels and high value chemicals based on biochar catalysts
Hui LI1(), Changlan HOU2, Yunbo ZHAI2, Mengjiao TAN1, Zhongliang HUANG1, Zhiwei WANG3, Lijian LENG4, Peng LIU5, Tingzhou LEI5, Changzhu LI1
1. State Key Laboratory of Utilization of Woody Oil Resource, Hunan Academy of Forestry, Changsha 410004, China
2. College of Environmental Science and Engineering, Hunan University, Changsha 410082, China
3. School of Environmental Engineering, Henan University of Technology, Zhengzhou 450001, China
4. School of Energy Science and Engineering, Central South University, Changsha 410083, China
5. National-Local Joint Engineering Research Center of Biomass Refining and High-Quality Utilization, Institute of Urban and Rural Mining, Changzhou University, Changzhou 213164, China
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Abstract

The reuse of biomass wastes is crucial toward today’s energy and environmental crisis, among which, biomass-based biochar as catalysts for biofuel and high value chemical production is one of the most clean and economical solutions. In this paper, the recent advances in biofuels and high chemicals for selective production based on biochar catalysts from different biomass wastes are critically summarized. The topics mainly include the modification of biochar catalysts, the preparation of energy products, and the mechanisms of other high-value products. Suitable biochar catalysts can enhance the yield of biofuels and higher-value chemicals. Especially, the feedstock and reaction conditions of biochar catalyst, which affect the efficiency of energy products, have been the focus of recent attentions. Mechanism studies based on biochar catalysts will be helpful to the controlled products. Therefore, the design and advancement of the biochar catalyst based on mechanism research will be beneficial to increase biofuels and the conversion efficiency of chemicals into biomass. The advanced design of biochar catalysts and optimization of operational conditions based on the biomass properties are vital for the selective production of high-value chemicals and biofuels. This paper identifies the latest preparation for energy products and other high-value chemicals based on biochar catalysts progresses and offers insights into improving the yield of high selectivity for products as well as the high recyclability and low toxicity to the environment in future applications.

Keywords biomass      biochar catalysts      biofuels      high chemicals     
Corresponding Author(s): Hui LI   
About author:

Peng Lei and Charity Ngina Mwangi contributed equally to this work.

Online First Date: 16 June 2023    Issue Date: 09 November 2023
 Cite this article:   
Hui LI,Changlan HOU,Yunbo ZHAI, et al. Selective preparation for biofuels and high value chemicals based on biochar catalysts[J]. Front. Energy, 2023, 17(5): 635-653.
 URL:  
https://academic.hep.com.cn/fie/EN/10.1007/s11708-023-0878-4
https://academic.hep.com.cn/fie/EN/Y2023/V17/I5/635
Fig.1  Selective preparation for biofuels and high value chemicals based on biochar catalysts.
Fig.2  Ethanol and steam process on Ni/biochar derived species on various active sites in reforming reaction (adapted with permission from Ref. [11]).
Fig.3  SEM images of Ni-doped biochar catalysts (adapted with permission from Ref. [16]).
Caforlytic performance Feedstock Preparation for product Synthesis condition Reagent and dosage Catalytic performance Ref.
Metal compound modified biochar catalysts Reed straws Methane-rich gas Pyrolyzed at 500–700 °C with10 °C/min 1.23 g/g Ni(NO3)2·6H2O 188.38 L/kg [14]
Corn cobs Phenol-rich bio-oil Microwave pyrolysis was performed at 600 °C for 1 h 0.4 mol/L Fe(NO3)3 16.45% [25]
Vine shoot and crystalline cellulose Hydrogen production from formic acid Pyrolyzed at 800 °C in CO2 flow (200 mL/min) for 2 h and reduced at 300 °C for 2 h in N2/H2 (1:1) flow (300 mL/min) Pd (II) acetate (purity = 47.14%) dissolved in 0.001 mol/L acetone 100% in 150 min [37]
Cladophora glomerata macroalgae Aromatic compounds of bio-oil Carbonized at 600 °C for 120 min in 30 mL/min ZnCl2 with impregnation ratios of 1.5 47.86% in 120 min [36]
Acid and alkali modified biochar catalysts Pinewood sawdust Glucose and 5-hydroxymethylfurfural Pyrolyzed at 600 °C and 10 °C/min for 2 h Impregnation ratios (2 mass ratios of 85% (w/w) H3PO4) Glucose (86.5 C mol% at 150 °C, for 20 min) HMF (30.2 C mol% at 180 °C, for 20 min) [38]
Peanut shell Algal biodiesel production Pyrolyzed at 400 °C 1 g BC with 10 mL 98% H2SO4 94.91% in 4h [41]
Sargassum tenerrimum Phenol conversion to cyclohexanol Pyrolyzed at 700 °C for 2 h 1:2 KOH impregnation ratio ≥ 99.9% in 4h [42]
Nitrogen-doped biochar catalysts Bamboo wastes Phenols products (mainly 4-vinyl phenol and 4-ethyl phenol) Pyrolyzed at 600 °C for 30 min with mixture atmosphere of Ar (99.999%) and NH3 (99.999%) NH3 concentrations (30%, volume fraction) Phenols (82%) including 31% 4-vinyl phenol and 16% 4-ethyl phenol [52]
Pinus sylvestris CO2 methanation Pyrolyzed at 600 °C for 1 h (400 mL/min) with 5 °C/min Pinus sylvestris powder, urea and NaHCO3 were mixed according to the mass ratio of 1:4:3 99.7% [46]
Tab.1  Catalytic performance of different modification of catalysts with biomass
Fig.4  Sulfonation reaction (adapted with permission from Ref. [44]).
Fig.5  Calculated reaction energy for the electroreduction of CO2 to ethanol over pyridinic and pyrrolic N sites (adapted with permission from Ref. [54]).
Modification of biochar catalysts Selectivity for product Ref.
Metal compound modified biochar catalysts Ni-modified biochar Methane [16]
Ni-modified biochar H2 production, 64.3% [19]
Ni-modified biochar Alkanes, 94% [23]
Pd-modified biochar Hydrogen production, 100% [39]
Zn-modified biochar Aromatic compounds of bio-oil, 47.86% [38]
Fe-modified biochar Phenol, 16.45 area% [25]
Fe-modified biochar CO, 23.07 mmol/g [34]
Acid and alkali modified biochar catalysts H3PO4-activated biochar HMF, 30.2 C mol%, glucose (86.5 C mol%) [40]
H2SO4 (30% w/v)-activated biochar Glucose, 85% [41]
H2SO4-activated biochar Biodiesel, 94.91% [43]
KOH activated biochar Cyclohexanol, 99.9% [45]
KOH activated biochar Biodiesel, 81.6% [46]
Nitrogen-doped biochar catalysts Nitrogen-doped biochar CH4, 99% [49]
Nitrogen-doped biochar Phenol, 82% [55]
Nitrogen-doped biochar (E)-1,2-bis (4-chlorophenyl) diazene, 96% [56]
Tab.2  Selectivity for product using different catalysts
Fig.6  Hydrodeoxygenation of vanillin depicting a plausible mechanism (adapted with permission from Ref. [72]).
Catalyst Feedstock Product Catalyst/% (mass fraction) Reported active sites Mechanism Ref.
BC Chicken manure Biodiesel 4.71 Ca species in catalyst imparts a strong basicity Pseudo-catalytic transesterification [61]
CaO/K2CO3 BC Brown algae of Sargassum oligocystum Biodiesel 4 CaO and K Transesterification process [63]
Solid acid BC Oil palm empty fruit bunch Biodiesel 20 S-O and S-O3H sulfonic groups Esterification [57]
Magnetic BC Palm kernel shell Biodiesel 3.66 Comparable magnetisation saturation of 8.458 emu/g and high acid density of 1.92 mmol/g Transesterification process [56]
Ni BC Mallee wood Ethanol steam reforming Alkali and alkaline earth metallic species and the O-containing functional groups C2H6 species associatively desorb with available hydrogen dehydrogenation and decomposition steps [11]
Poultry litter biochar (PLBC) Poultry litter Ethanol and butanol 10 Highest pH buffering capacity, CEC and total amount of cations Clostridium carboxidivorans syngas fermentation [71]
BC Rice straw (RB) and manure (MB) Methanogenesis Redox-active properties or charging and discharging capacities, quinones Quantitative polymerase chain reaction, electron transfer [75]
BC Corn straw Methane 1 –CH3, –CH2, C=C bonds or C=O bonds, higher porosity, surface biological phosphorus content Hydrogenotrophic methanogens biocarrier [80]
Fe-rich BC Corn stalk Methane (95%) 10 Less in situ carbon consumption and a minor change of porous structure Microwave methane reforming [81]
Pd BC Vine shoot and crystalline cellulose Hydrogen 10 Pd size and dispersion and its interaction, chars and textural properties Deoxygenation [37]
Ni-BC Wheat straw Hydrogen 15 Interaction between Ni, biochar and volatiles Steam gasification [88]
BC Sugarcane bagasse Hydrogen 15 At low temperature with redox activity, at high temperature via cell growth enhancement Ethanol-type fermentation [92]
BC Bamboo wastes and microalgae Bio-oil (aromatics and phenols) Long-chain fatty acids and O-species Deoxygenation [94]
BC Nanocellulose Phenolic monomers and hydrogen 3 Free, bound, or produced water, cellulose Demethoxylation, the transalkylation reaction [95]
Pd-Al2O3-BC Plastic and biomass C9 monomeric phenol 5 Hydrogenation of Cα = Cβ or dehydroxylation of Cγ, dehydroxylation at Cγ-OH Lignin hydrogenolysis, decarboxylation and demethoxylation [96]
BC Pine Caproate production 20 Extracellular polymer substances (EPS), methanogens Chain elongation, electron efficiency process [97]
BC Hardwood (80%, mass fraction) and coniferous wood (20%, mass fraction) Ethanol and caproic acid 10 Cell retention, decouple the growth of C. kluyveri and its caproic acid production Secondary fermentation of syngas fermentation effluent, energy intensive distillation [98]
Tab.3  Active sites and mechanisms of different biochar in selective preparation of biofuels and high chemicals
Fig.7  Process for furan production from lignocellulosic biomass (adapted with permission from Ref. [111]).
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