Biomass pyrolysis-gasification over Zr promoted CaO-HZSM-5 catalysts for hydrogen and bio-oil co-production with CO 2 capture

2017 ◽  
Vol 42 (25) ◽  
pp. 16031-16044 ◽  
Author(s):  
Zhao Sun ◽  
Sam Toan ◽  
Shiyi Chen ◽  
Wenguo Xiang ◽  
Maohong Fan ◽  
...  
Keyword(s):  
Author(s):  
Junmeng Cai ◽  
Md. Maksudur Rahman ◽  
Shukai Zhang ◽  
Manobendro Sarker ◽  
Xingguang Zhang ◽  
...  
Keyword(s):  

Fuel ◽  
2022 ◽  
Vol 312 ◽  
pp. 122959
Author(s):  
Soheil Valizadeh ◽  
Daejun Oh ◽  
Jungho Jae ◽  
Sumin Pyo ◽  
Hoyeon Jang ◽  
...  

Author(s):  
Manuel Garcia-Peréz ◽  
Jesus Alberto Garcia-Nunez ◽  
Manuel Raul Pelaez-Samaniego ◽  
Chad Eugene Kruger ◽  
Mark Raymond Fuchs ◽  
...  

The objective of this chapter is to review and discuss sustainability and techno-economic criteria to integrate pyrolysis, biochar activation, and bio-oil refining into sustainable business models. Several business models such as the production of biochar with heat recovery and bio-oil refining are discussed. Cost data needed by engineering practitioners to conduct enterprise-level financial analyses of different biomass pyrolysis economy models are presented. This chapter also reviews life cycle assessments of pyrolysis business models. If the feedstock used is produced sustainably and if the pyrolysis vapors are used for bio-oil or heat production, both, the production of biochar through slow pyrolysis and its use as a soil amendment to sequester carbon, and the production and refining of fast pyrolysis oils to produce transportation fuels could have a positive environmental impact.


Author(s):  
Quang Thang Trinh ◽  
Arghya Banerjee ◽  
Khursheed B. Ansari ◽  
Duy Quang Dao ◽  
Asmaa Drif ◽  
...  

Author(s):  
Adewale George Adeniyi ◽  
Kevin Shegun Otoikhian ◽  
Joshua O. Ighalo

Abstract The steam reforming of biomass pyrolysis oil is a well-established means of producing the more useful bio-hydrogen. Bio-oil has a comparatively low heating value, incomplete volatility and acidity, hence upgrading to a more useful product is required. Over the years, the experimental conditions of the process have been studied extensively in the domain of catalysis and process variable optimisation. Sorption enhancement is now being applied to the system to improve the purity of the hydrogen stream. Lifecycle analyses has revealed that bio-hydrogen offers considerable reductions in energy consumption compared to fossil fuel-derived hydrogen. Also, green-house-gas savings from the process can also be as high as 54.5 %. Unfortunately, techno-economic analyses have elucidated that bio-hydrogen production is still hampered by high production costs. Research endeavours in steam reforming of biomass bio-oil is done with an eye for developing added value products that can complement, substitute (and one day replace) fossil fuels whilst ameliorating the global warming menace.


ChemSusChem ◽  
2019 ◽  
Author(s):  
Héctor Hernando ◽  
Ana M. Hernández‐Giménez ◽  
Santiago Gutiérrez‐Rubio ◽  
Tomaz Fakin ◽  
Andrej Horvat ◽  
...  
Keyword(s):  

2018 ◽  
Vol 61 ◽  
pp. 00018
Author(s):  
Murlidhar Gupta ◽  
Jacques Monnier ◽  
Eric Turriff ◽  
Mark Boyd

Biomass pyrolysis liquids (also known as bio-oil), are derived from renewable lignocellulosic biomass residues by fast pyrolysis process. These second-generation oxygenated hydrocarbon resources have the potential to partially substitute for petroleum-derived feedstocks and thus enhance the economic and environmental sustainability of our natural resources. However, in contrast to petroleum fuels, biomass-derived pyrolysis liquids contain a large amount of oxygen, usually 40-50% wt% (wet basis). This undesirable high oxygen content in pyrolysis liquids is considered as the primary reason for its high polarity, high acidity, lower stability, lower energy density and very low miscibility with conventional crude refining feedstocks. There are two major pathways for upgrading the pyrolysis liquids. While hydrodeoxygenation route is one of the most explored options, it requires production and supply of large amounts of expensive hydrogen at high pressures, mandating large and centralized upgrading plants, and thus large capital investment. In this paper, we discuss an alternative method of pyrolysis liquid upgrading, using cheap and affordable hydrogen donor additives and catalysts to promote partial deoxygenation at near atmospheric pressure. This approach is preferably to be used as a pre-treatment and stabilizing method for pyrolysis liquids in the close vicinity of remote biomass pyrolysis plants. The pre-treated oil, then can be shipped for further hydrocracking process in a centralized co-processing facility. Preliminary results from the initial proof of concept experiments involving a 200 g/h gas-phase continuous fast catalytic cracking system with continuous coke removal to enhance deoxygenation performance are presented. These results indicate positive impact of catalyst bed on quality and yield of the upgraded bio-oil product in terms of pH, viscosity, degree of deoxygenation, oil yield and concentration of hydrogen in the off gases.


2018 ◽  
Vol 129 ◽  
pp. 134-149 ◽  
Author(s):  
Raquel Escrivani Guedes ◽  
Aderval S. Luna ◽  
Alexandre Rodrigues Torres

Sign in / Sign up

Export Citation Format

Share Document