Thermocatalytic routes and reactor strategies for valorization of biodiesel-derived glycerol to fuels

被引:11
作者
Okoye, P. U. [1 ]
Arias, D. M. [1 ]
Hameed, B. H. [2 ]
Sebastian, P. J. [1 ]
Li, Sanxi [3 ]
Song, Wang [3 ]
机构
[1] Inst Energias Renovables IER UNAM, Privada Xochicalco Col Ctr Temixco s n, Morelos 62580, Mexico
[2] Qatar Univ, Coll Engn, Dept Chem Engn, POB 2713, Doha, Qatar
[3] Shenyang Univ Technol, Sch Sci, Shenyang 110870, Liaoning, Peoples R China
关键词
Glycerol; Supercritical water reforming; Catalyst; Fuels; Gasification; Pyrolysis; SUPERCRITICAL WATER GASIFICATION; CONTINUOUS HYDROTHERMAL GASIFICATION; LIFE-CYCLE ASSESSMENT; CRUDE GLYCEROL; HYDROGEN-PRODUCTION; BY-PRODUCT; SUSTAINABILITY ANALYSIS; CATALYTIC CONVERSION; BIOMASS GASIFICATION; ACTIVITY MAINTENANCE;
D O I
10.1016/j.applthermaleng.2022.118901
中图分类号
O414.1 [热力学];
学科分类号
摘要
Glycerol is an oversupplied commodity from biodiesel production with beneficial properties for the synthesis of versatile utility biochemicals. The functional properties of glycerol with three hydroxyl groups could be tailored toward producing fuels such as hydrogen, syngas, C-1-C-3 hydrocarbon fuel, bio-oil and methane. This study elucidates the reported thermochemical pathways such as pyrolysis, gasification, combustion, steam and aqueous reforming, and supercritical water gasification for fuel production from biodiesel-derived glycerol. The mechanism of these pathways, process conditions, catalytic integration, and limitations were investigated. Also, reactor strategies such as fixed bed reactors, fluidized bed, and solar reactor strategies used for the thermochemical valorization of glycerol was discussed. The studies revealed that hydrogen up to 70% yield could be generated from glycerol using noble metals and nickel-based catalysts. Catalyst deactivation due to coking could be minimized by the addition of alkaline metals, which discourages methanation reaction. Reaction parameters such as temperature, catalyst amount, time on stream, and glycerol/water or steam ratio influence the product distribution. The glycerol steam reforming is more energy-intensive and requires temperatures in the range of 450-1000 ?, whereas the aqueous reforming is propagated in the range of 180-250 ?. The circulating fluidized bed reactors limit coking due to self-regeneration of the catalysts in situ , however, they are cost-intensive. Life cycle assessment analysis revealed that supercritical water reforming (SCWR) of glycerol offers a sustainable pathway to reduce CO2 by 95% and integration of SCWR in biodiesel plants to produce hydrogen for heating can realize a net present value between 7.70 and 15.70 million USD. Further studies to analyze the economic impact of the individual pathways to optimize the production of fuels from glycerol are required. It is hoped that this study will engage industries and researchers to increasingly use glycerol as a substrate for the production of fuels for transportation.
引用
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页数:17
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