Operational optimization of Co-processing of heavy oil and bio-oil based on the coordination of desulfurization and deoxygenation

Energy ◽  
2021 ◽  
pp. 122558
Author(s):  
Le Wu ◽  
Ting Yan ◽  
Qingyu Lei ◽  
Shuai Zhang ◽  
Yuqi Wang ◽  
...  
2014 ◽  
Vol 554 ◽  
pp. 332-336
Author(s):  
Murtala Musa Ahmed ◽  
Noor Shawal Nasri ◽  
Rahmat Mohsin ◽  
Usman Dadum Hamza ◽  
Jibril Mohammed

Identification and assessment of phenol and phenolic rich components of heavy oil fractions of biomass pyrolytic oil were conducted. The original bio-oil used for this study was derived from the pyrolysis of empty fruit bunch (EFB). It was separated into water soluble (light oil) and water insoluble (heavy oil) components by mixing it with water at 2:1 V/V ratio under ambient condition with vigorous stirring using centrifuge for 30mins. The raw bio-oil and the heavy oil fractions were later characterized using Fourier Transform Infra-Red (FTIR) and Gas chromatography-Mass spectroscopy (GC-MS) techniques in order to identify the function groups present and their compositions. The GC-MS results for the heavy oil indicated a high concentration of phenol and phenolic components, which was strongly supported by the presence of OH group (characteristic of phenol) from FTIR analysis. Utilization of bio-oil which was known to have a significant amount of phenol and phenolic rich components for phenolic, novolac or epoxy resin manufacture would significantly reduce the cost and negative environmental effects of the fossil-based resins.


2014 ◽  
Vol 695 ◽  
pp. 114-117
Author(s):  
Noor Shawal Nasri ◽  
Murtala Musa Ahmed ◽  
Mariam Amruddin ◽  
Usman Dadum Hamza ◽  
Jibril Mohammed ◽  
...  

Bio-oil derived from the pyrolysis of a sustainable palm biomass has great potential as a suitable replacement to the conventional source of fuels and chemicals. However, the bio-oil produced is highly acidic and corrosive due to presence of acids that can leads to operational difficulties. As such, purification of the bio-oil for the targeted application as chemicals or fuel source needs to be conducted. This study is aimed at conducting further study on the isolation of insoluble fractions (heavy oil) of bio-oil and at the same time assesses the corrosiveness of the insoluble fractions and compare with that of raw bio-oil. This was done in order see whether the corrosive properties of the raw bio-oil are associated with these fractions or not. It was later upgraded using various ratio of zero valence aluminium metal as corrosion inhibitor. The raw bio-oil and the upgraded heavy oil fractions samples were characterized using various techniques. The results indicate significant improvement on the various properties tested on the side of upgraded heavy oil fractions than the raw bio-oil. Thus, realization of bio-oil quality for its subsequent application as fuel can significantly reduce operational difficulties in engines and other processing equipment.


Author(s):  
Seongmin Kang ◽  
Jiyun Woo ◽  
Eui-Chan Jeon

In order to cope with recent climate change, Korea is reducing the use of heavy oil in petroleum-fired power plants and mixing bio-oils. Accordingly, this must be taken into account when calculating the emissions of air pollutants. However, in the case of Korea, when calculating NH3 emissions, the United States Environmental Protection Agency (EPA) emission factor is applied as it is to calculate emissions, and for petroleum power plants, the heavy oil emission factor proposed by EPA is used as it is to calculate emissions. In petroleum power plants, bio-oil is not mixed in a certain amount and used at a different ratio depending on the situation of the power plant. Therefore, in this study, the NH3 emission factor according to the mixing ratio of bio-heavy oil is calculated and the mixing ratio is calculated. As a result of the analysis, the emission factor according to bio-oil and the mixed ratio was found to be in the range of 0.010~0.033 kg NH3/kL, and it was lower than the heavy oil emission factor 0.096 kg NH3/kL of EPA currently used in Korea. This is because the amount of NH3 through the slip is also small since the use of NH3 for reduction is also low because the NOx emission from the use of bio-oil is low. Considering all of these points, we have statistically analyzed whether emission factors should be developed and applied. As a result of the confirmation, the difference according to the mixed consumption rate was not large.


2020 ◽  
Author(s):  
Idoia Hita ◽  
Tomas Cordero-Lanzac ◽  
Francisco J. Garcia-Mateos ◽  
Jose Rodriguez-Mirasol ◽  
Tomas Cordero ◽  
...  

2020 ◽  
Author(s):  
Idoia Hita ◽  
Tomas Cordero-Lanzac ◽  
Francisco J. Garcia-Mateos ◽  
Jose Rodriguez-Mirasol ◽  
Tomas Cordero ◽  
...  

1918 ◽  
Vol 86 (2222supp) ◽  
pp. 78-80
Author(s):  
Charles E. Lucke
Keyword(s):  

2018 ◽  
Vol 14 (1) ◽  
pp. 31-60 ◽  
Author(s):  
M. Y. Guida ◽  
F. E. Laghchioua ◽  
A. Hannioui

This article deals with fast pyrolysis of brown algae, such as Bifurcaria Bifurcata at the range of temperature 300–800 °C in a stainless steel tubular reactor. After a literature review on algae and its importance in renewable sector, a case study was done on pyrolysis of brown algae especially, Bifurcaria Bifurcata. The aim was to experimentally investigate how the temperature, the particle size, the nitrogen flow rate (N2) and the heating rate affect bio-oil, bio-char and gaseous products. These parameters were varied in the ranges of 5–50 °C/min, below 0.2–1 mm and 20–200 mL. min–1, respectively. The maximum bio-oil yield of 41.3wt% was obtained at a pyrolysis temperature of 600 °C, particle size between 0.2–0.5 mm, nitrogen flow rate (N2) of 100 mL. min–1 and heating rate of 5 °C/min. Liquid product obtained under the most suitable and optimal condition was characterized by elemental analysis, 1H-NMR, FT-IR and GC-MS. The analysis of bio-oil showed that bio-oil from Bifurcaria Bifurcata could be a potential source of renewable fuel production and value added chemicals.


Sign in / Sign up

Export Citation Format

Share Document