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通过水热液化和慢速热解转化原始和脱脂藻类生物质的热化学转化。

Thermochemical conversion of raw and defatted algal biomass via hydrothermal liquefaction and slow pyrolysis.

机构信息

Dept. of Civil and Environmental Engineering, University of Illinois at Urbana-Champaign, 205 N. Mathews Ave., Urbana, IL 61801, United States.

出版信息

Bioresour Technol. 2012 Apr;109:178-87. doi: 10.1016/j.biortech.2012.01.008. Epub 2012 Jan 10.

Abstract

Thermochemical conversion is a promising route for recovering energy from algal biomass. Two thermochemical processes, hydrothermal liquefaction (HTL: 300 °C and 10-12 MPa) and slow pyrolysis (heated to 450 °C at a rate of 50 °C/min), were used to produce bio-oils from Scenedesmus (raw and defatted) and Spirulina biomass that were compared against Illinois shale oil. Although both thermochemical conversion routes produced energy dense bio-oil (35-37 MJ/kg) that approached shale oil (41 MJ/kg), bio-oil yields (24-45%) and physico-chemical characteristics were highly influenced by conversion route and feedstock selection. Sharp differences were observed in the mean bio-oil molecular weight (pyrolysis 280-360 Da; HTL 700-1330 Da) and the percentage of low boiling compounds (bp<400 °C) (pyrolysis 62-66%; HTL 45-54%). Analysis of the energy consumption ratio (ECR) also revealed that for wet algal biomass (80% moisture content), HTL is more favorable (ECR 0.44-0.63) than pyrolysis (ECR 0.92-1.24) due to required water volatilization in the latter technique.

摘要

热化学转化是从藻类生物质中回收能量的一种很有前途的途径。两种热化学过程,水热液化(HTL:300°C 和 10-12 MPa)和慢速热解(以 50°C/min 的速率加热至 450°C),被用于从 Scenedesmus(原始和脱脂)和螺旋藻生物质中生产生物油,并与伊利诺伊州页岩油进行了比较。尽管这两种热化学转化途径都产生了能量密集型生物油(35-37MJ/kg),接近页岩油(41MJ/kg),但生物油的产率(24-45%)和理化特性受到转化途径和原料选择的高度影响。在生物油的平均分子量(热解 280-360Da;HTL 700-1330Da)和低沸点化合物的百分比(bp<400°C)(热解 62-66%;HTL 45-54%)方面观察到了明显的差异。对能源消耗比(ECR)的分析也表明,对于湿藻类生物质(80%水分含量),由于后者技术中需要蒸发水分,HTL 比热解(ECR 0.92-1.24)更有利(ECR 0.44-0.63)。

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