Co‐processing of rapeseed oil — straight run gas oil mixture: Comparative study of sulfide CoMo/Al2O3-SAPO-11 and NiMo/Al2O3-SAPO-11 catalysts

2020 ◽  
Author(s):  
E.N. Vlasova ◽  
A.A. Porsin ◽  
P.V. Aleksandrov ◽  
A.L. Nuzhdin ◽  
G.A. Bukhtiyarova
Molecules ◽  
2020 ◽  
Vol 25 (16) ◽  
pp. 3732
Author(s):  
José Miguel Hidalgo Herrador ◽  
Jakub Fratczak ◽  
Zdeněk Tišler ◽  
Hector de Paz Carmona ◽  
Romana Velvarská

The use of renewable local raw materials to produce fuels is an important step toward optimal environmentally friendly energy consumption. In addition, the use of these sources together with fossil fuels paves the way to an easier transition from fossil to renewable fuels. The use of simple organic acids as hydrogen donors is another alternative way to produce fuel. The present work reports the use of oxalic acid as a hydrogen donor for the catalytic hydrodesulfurization of atmospheric gas oil and the deoxygenation of rapeseed oil at 350 °C. For this process, one commercial NiW/SiO2–Al2O3 solid and two NiW/modified phonolite catalysts were used, namely Ni (5%) W (10%)/phonolite treated with HCl, and Ni (5%) W (10%)/phonolite treated with oxalic acid. The fresh phonolite catalysts were characterized by Hg porosimetry and N2 physisorption, ammonia temperature programmed desorption (NH3-TPD), X-ray diffraction (XRD), and X-ray fluorescence (XRF). The sulfided metal phonolite catalysts were characterized by XRD and XRF. Hydrodesulfurization led to a decrease in sulfur content from 1 to 0.5 wt% for the phonolite catalysts and to 0.8 wt% when the commercial catalyst was used. Deoxygenation led to the production of 15 and 65 wt% paraffin for phonolite and commercial solids, respectively. The results demonstrate the potential of using oxalic acid as a hydrogen donor in hydrotreating reactions.


2018 ◽  
Vol 173 ◽  
pp. 153-164 ◽  
Author(s):  
Anton L. Esipovich ◽  
Anton E. Rogozhin ◽  
Artem S. Belousov ◽  
Evgeny A. Kanakov ◽  
Sergey M. Danov

2021 ◽  
Vol 198 ◽  
pp. 108175
Author(s):  
Seyed Hamidreza Yousefi ◽  
Fariborz Rashidi ◽  
Mohammad Sharifi ◽  
Mohammad Soroush ◽  
Ashkan Jahanbani Ghahfarokhi

2012 ◽  
Vol 57 ◽  
pp. 22-28 ◽  
Author(s):  
Md. Nurun Nabi ◽  
Richard J. Brown ◽  
Zoran Ristovski ◽  
Johan Einar Hustad

2019 ◽  
Vol 92 (12) ◽  
pp. 1797-1804
Author(s):  
A. A. Porsin ◽  
E. N. Vlasova ◽  
A. L. Nuzhdin ◽  
P. V. Aleksandrov ◽  
G. A. Bukhtiyarova
Keyword(s):  
Gas Oil ◽  

ACS Omega ◽  
2021 ◽  
Vol 6 (11) ◽  
pp. 7680-7692
Author(s):  
Héctor de Paz Carmona ◽  
Eliška Svobodová ◽  
Zdeněk Tišler ◽  
Uliana Akhmetzyanova ◽  
Kateřina Strejcová
Keyword(s):  

Catalysts ◽  
2021 ◽  
Vol 11 (4) ◽  
pp. 442
Author(s):  
Petr Straka ◽  
Josef Blažek ◽  
Daria Toullis ◽  
Tomáš Ihnát ◽  
Pavel Šimáček

This study compares the hydrotreating of the mixture of petroleum middle distillates and the same mixture containing 20 wt % of rapeseed oil. We also study the effect of the temperature and the weight hourly space velocity (WHSV) on the co-hydrotreating of gas oil and rapeseed oil mixture. The hydrotreating is performed over a commercial hydrotreating Ni-Mo/Al2O3 catalyst at temperatures of ca. 320, 330, 340, and 350 °C with a WHSV of 0.5, 1.0, 1.5, and 2.0 h−1 under a pressure of 4 MPa and at a constant hydrogen flow of 28 dm3·h−1. The total conversion of the rapeseed oil is achieved under all the tested reaction conditions. The content of the aromatic hydrocarbons in the products reached a minimum at the lowest reaction temperature and WHSV. The content of sulphur in the products did not exceed 10 mg∙kg−1 at the reaction temperature of 350 °C and a WHSV of 1.0 h−1 and WHSV of 0.5 h−1 regardless of the reaction temperature. Our results show that in the hydrotreating of the feedstock containing rapeseed oil, a large amount of hydrogen is consumed for the dearomatisation of the fossil part and the saturation of the double bonds in the rapeseed oil and its hydrodeoxygenation.


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