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Objective of this study was the investigation on the up-scaling of base-catalyzed depolymerization (BCD) of lignin to pilot plant dimension. The cleavage process was carried out in dilute alkaline solution at temperatures up to 340°C and a pressure of 25 MPa in a continuously operated tubular flow reactor with throughputs up to 20 kg/h. Investigations included the proof of the feasibility of the scale-up as well as a parameter study on the cleavage of hardwood Organosolv lignin and softwood Kraft lignin within the established pilot plant. Yields and molecular compositions of the isolated product fractions BCD-oil (liquid phenolic fraction) and BCD-oligomers (solid phenolic fraction) are similar to those described in technical lab scale, showing a good scalability. Here, BCD-oils rich in phenolic monomers such as guaiacol, catechol and/or syringol were obtained with a content of up to 13.3 wt% and 14.5 wt% from Organosolv lignin and Kraft lignin, respectively. Formation of BCD-oligomers strongly depends on temperature and residence times within the reactor.
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篇名 Production of Bio-Phenols for Industrial Application: Scale-Up of the Base-Catalyzed Depolymerization of Lignin
来源期刊 绿色与可持续化学(英文) 学科 化学
关键词 LIGNIN Base-Catalyzed DEPOLYMERIZATION PHENOLIC Monomers PHENOLIC Oligomers
年,卷(期) 2017,(3) 所属期刊栏目
研究方向 页码范围 193-202
页数 10页 分类号 O6
字数 语种
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研究主题发展历程
节点文献
LIGNIN
Base-Catalyzed
DEPOLYMERIZATION
PHENOLIC
Monomers
PHENOLIC
Oligomers
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绿色与可持续化学(英文)
季刊
2160-6951
武汉市江夏区汤逊湖北路38号光谷总部空间
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188
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