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温度、水负荷和 Ru/C 催化剂对水热液化藻类生成的水不溶性和水溶性生物油馏分的影响。

Effect of temperature, water loading, and Ru/C catalyst on water-insoluble and water-soluble biocrude fractions from hydrothermal liquefaction of algae.

机构信息

Key Laboratory of Thermo-Fluid Science & Engineering, Ministry of Education, School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an, Shaanxi Province 710049, China; Department of Chemical Engineering, University of Michigan, Ann Arbor, MI 48109, United States.

Department of Chemical Engineering, University of Michigan, Ann Arbor, MI 48109, United States; Department of Chemical Engineering, Pennsylvania State University, University Park, PA 16802, United States.

出版信息

Bioresour Technol. 2017 Sep;239:1-6. doi: 10.1016/j.biortech.2017.04.127. Epub 2017 May 4.

Abstract

Hydrothermal liquefaction (HTL) converts algal biomass into a crude bio-oil (biocrude) and aqueous-phase products. The effect of temperature, water loading, and added H and/or Ru/C catalyst on the properties of the biocrude that spontaneously separates from the aqueous phase post reaction and also the biocrude that is extractable from the aqueous phase by dichloromethane is explored herein. This report is the first to elucidate how the yields, compositions, heating values, and energy recoveries of the two biocrudes vary with the processing conditions above. Increasing temperature from 350 to 400°C increased the yield of water-insoluble biocrude (38.1-42.5wt%) and its hexane-soluble subfraction (63.7-85.6wt%) while decreasing the yield of extractable, water-soluble biocrude (6.6-2.5wt%). The Ru/C catalyst had the same effect. Reaction temperature and catalysts could be used to manipulate the proportions of water-soluble and water-insoluble biocrude from algae HTL and thereby manipulate biocrude quantity and quality.

摘要

水热液化(HTL)将藻类生物质转化为粗生物油(生物原油)和水相产物。本文探讨了温度、水负荷以及添加 H 和/或 Ru/C 催化剂对反应后自发从水相分离的生物原油和通过二氯甲烷从水相可提取的生物原油性质的影响。本报告首次阐明了两种生物原油的产率、组成、发热值和能量回收率如何随上述加工条件而变化。将温度从 350°C 升高到 400°C,增加了水不溶性生物原油(38.1-42.5wt%)及其正己烷可溶亚组分(63.7-85.6wt%)的产率,而降低了可提取的水溶性生物原油(6.6-2.5wt%)的产率。Ru/C 催化剂也有同样的效果。反应温度和催化剂可用于操纵藻类 HTL 中水溶性和水不溶性生物原油的比例,从而操纵生物原油的数量和质量。

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