Hydrodeoxygenation (HDO) Upgrading of Whole Pyrolysis Oil by Using Ru Supported Catalyst
2014
- 110Usage
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Example: if you select the 1-year option for an article published in 2019 and a metric category shows 90%, that means that the article or review is performing better than 90% of the other articles/reviews published in that journal in 2019. If you select the 3-year option for the same article published in 2019 and the metric category shows 90%, that means that the article or review is performing better than 90% of the other articles/reviews published in that journal in 2019, 2018 and 2017.
Citation Benchmarking is provided by Scopus and SciVal and is different from the metrics context provided by PlumX Metrics.
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- Usage110
- Abstract Views107
- Downloads3
Thesis / Dissertation Description
Fossil fuels have been major energy sources for decades. Although easily accessible petroleum is limited, continued use of fossil fuels is causing serious environmental issues, one of which is the greenhouse effect, providing incentives for development of alternative energy sources. Biomass is one of the most important sources of renewable liquid fuels. One process for conversion of biomass is fast pyrolysis. However, the biooil produced by the fast pyrolysis process has several disadvantages, such as high oxygen and water content, high viscosity and low pH, which decrease its quality as a transportation fuel. Hydrodeoxygenation (HDO) processes are needed to upgrade and improve the quality of pyrolysis oil. This thesis will review progress in the development of hydrodesulfurization, precious metal, and reducible metal oxide catalysts for HDO. Development of catalysts that are effective as well as robust is critical to the ultimate commercial success of the pyrolysis route.In this thesis, a detailed study of the stabilization effect was done by using different reaction conditions and the product chemical composition was analyzed using NMR and GCMS techniques. The whole pyrolysis oil HDO reaction was done using a 2-step procedure; a mild reaction condition was used during the 1st step of the reaction to stabilize the pyrolysis oil, before increasing the temperature and hydrogen pressure for the 2nd HDO step. The product oil from each step was analyzed using NMR and GCMS to determine the compounds being produced and removed during the reaction. The second part of the research in this thesis focused on the effect of water on the product oil quality of the HDO reaction. The H2 consumption during the reaction was calculated based on a self-designed calibration system and an accurate mass balance calculation was done for each phase of the product oil. The results showed a dramatic decrease of the product oil yield when more than 50% of water was added to the reaction, which could possibly be caused by the aqueous reforming of the OH-containing compounds.
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