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Biotechnology for Biofuels · 2018 ·Vol. 11 ·期 1 ·1-16 · IF 5.497

Liquid fuel generation from algal biomass via a two-step process: effect of feedstocks

Xu Yu-Ping,Duan Pei-Gao,Wang Feng,Guan Qing-Qing

Background In this study, a two-step processing method (hydrothermal liquefaction followed by catalytic upgrading) was used to produce upgraded bio-oil. A comprehensive screening analysis of algal species, including four microalgae and four macroalgae, was conducted to bridge the gap between previous accounts of microalgae and macroalgae hydrothermal liquefaction and the upgrading process of the resulting crude bio-oils. Results Hydrothermal liquefaction using eight algal biomasses was performed at 350 °C for 1 h. The microalgae always produced a higher crude bio-oil yield than the macroalgae due to their high lipid content, among which Schizochytrium limacinum provided the maximum crude bio-oil yield of 54.42 wt%. For microalgae, higher amounts of N in the biomass resulted in higher amounts of N in the crude bio-oil; however, contrary results were observed for the macroalgae. The crude bio-oils generated from both the microalgae and macroalgae were characterized as having a high viscosity, total acid number, and heteroatom content, and they were influenced by the biochemical compositions of the feedstocks. Next, all eight-crude bio-oils were treated at 400 °C for 2 h with 10 wt% Ru/C using tetralin as the hydrogen donor. The hydrogen source was provided after tetralin was transformed to naphthalene. All the upgraded bio-oils had higher energy densities and significantly lower N, O, and S contents and viscosities than their corresponding crude bio-oils. However, the H/C molar ratio of the upgraded bio-oils decreased due to the absence of external hydrogen relative to the crude bio-oils. The S content of the upgraded bio-oil produced from upgrading the Schizochytrium limacinum crude bio-oil was even close to the 50 ppm requirement of China IV diesel. Conclusions Microalgae are better feedstocks than macroalgae for liquid fuel production. Biochemical components have a significant impact on the yield and composition of crude bio-oil. Tetralin does not perform as well as external hydrogen for controlling coke formation. The S content of the upgraded bio-oil can be reduced to 76 ppm for the crude bio-oil produced from Schizochytrium limacinum . Upgraded bio-oils have similar properties to those of naphtha and jet fuel.

CAS / MDL: 75-09-2 119-64-2
研究领域: 能源生物学 · 生物化学工程
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FUEL PROCESSING TECHNOLOGY · 2021 · IF 7.033

Hydro-upgrading of algal bio-oil in tetralin for the production of high-quality liquid fuel: Process intensification

Lei Chen,Zhi-Cong Wang,Dabo Chen,Lin-Xin Yin,Pei-Gao Duan

We report a new process to realize the deep removal of N, O, and S from the bio-oil when using a batch reactor to do the hydro-upgrading experiments. That is, within a fixed reaction time, hydro-upgrading of the bio-oil was carried out in several stages. After each stage reaction was finished, the reactor was cooled, and the gas in the reactor was replaced with fresh hydrogen, and then the reaction continued until the total reaction time was complete. A bio-oil produced from hydrothermal liquefaction of microalgae mixed with tetralin at a mass ratio of 1:1 was used as the feedstock . The experiments were performed at different temperatures (300–480 °C) and time (1–8 h) with fixed addition of 10 wt% Pt/C and 8 MPa H 2 . Higher treated bio-oil yield was always achieved if the reaction was performed in several stages. The N-, O-, and S- containing compounds in the gaseous products mainly consisted of C 2 H 4 N, C 3 H 7 N, C 6 H 7 N, NH 3 , (SCN) 2 , SO 2 , and H 2 O. The removal of these gas products avoided their secondary reactions with the bio-oil and slowed down the catalyst poisoning , and thus breaking through the equilibrium limitations of denitrogenation, desulfurization , and deoxygenation and prolonging the activity of the catalyst.

CAS / MDL: 119-64-2
研究领域: 能源生物学 · 化学工程
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