Mechanism study of the conversion of esters to high-octane-number aromatics over HZSM-5

2019 ◽  
Vol 33 (3) ◽  
pp. e4673 ◽  
Author(s):  
Navid Habibi ◽  
Hossein A. Dabbagh
2018 ◽  
Author(s):  
Marcus Lundgren ◽  
Alexios Matamis ◽  
Zhenkan Wang ◽  
Pablo Garcia Valladolid ◽  
Mattias Richter ◽  
...  

2015 ◽  
Vol 17 (2) ◽  
pp. 1065-1070 ◽  
Author(s):  
Jiayu Xin ◽  
Dongxia Yan ◽  
Olubunmi Ayodele ◽  
Zhan Zhang ◽  
Xingmei Lu ◽  
...  

Biomass-derived γ-valerolactone was converted into high octane number gasoline with SiO2/Al2O3 and [CF3CH2OH2][CF3CH2OBF3] as efficient catalysts.


2012 ◽  
Vol 2012 ◽  
pp. 1-9 ◽  
Author(s):  
Toshiyuki Kimura ◽  
Chen Liu ◽  
Xiaohong Li ◽  
Takaaki Maekawa ◽  
Sachio Asaoka

In order to produce petroleum alternatives from biomass, a significant amount of research has been focused on oils from microalgae due to their origin, which would not affect food availability. Nanoporous hybrid catalysts composed ofnsAl2O3and zeolites have been proven to be very useful compared to traditional catalysts in hydrotreating (HT), hydrocracking (HC), and catalytic cracking (CC) of large molecules. To evaluate the reaction scheme and products from model isoprenoid compounds of microalgae oil, nanoporous hybrid catalyst technologies (CC:nsAl2O3/H-USY andnsAl2O3/H-GaAlMFI; HC: [Ni-Mo/γ-Al2O3]/nsAl2O3/H-beta) were studied. The major product from CC onnsAl2O3/H-USY was highly aromatic gasoline, while the product from HC was half-isoparaffinic/olefinic kerosene. Although more than 50 wt% of the products from HT/CC on the USY catalyst was liquefied petroleum gas due to overcracking, the product from HT/CC on the MFI catalyst was high-octane-number gasoline. Delightfully, the product from HT/HC was kerosene and its average number was 11, with more than 80 wt% being isoparaffinic. As a result, it was demonstrated that hydrotreating may convert isoprenoid oil from microalgae over nanoporous hybrid catalysts into a variety of products.


Fuel ◽  
2012 ◽  
Vol 97 ◽  
pp. 585-594 ◽  
Author(s):  
J.E. Anderson ◽  
D.M. DiCicco ◽  
J.M. Ginder ◽  
U. Kramer ◽  
T.G. Leone ◽  
...  

2019 ◽  
Vol 25 (5) ◽  
pp. 37-51
Author(s):  
Alaa D. Jawad Al-Bayati ◽  
Abdul Hussain Hurraija Rufaish ◽  
Hussein Shaheed Fadhil

To decrease the dependency of producing high octane number gasoline on the catalytic processes in petroleum refineries and to increase the gasoline pool, the effect of adding a suggested formula of composite blending octane number enhancer to motor gasoline composed of a mixture of oxygenated materials (ethanol and ether) and aromatic materials (toluene and xylene) was investigated by design of experiments made by Mini Tab 15 statistical software. The original gasoline before addition of the octane number blending enhancer has a value of (79) research octane number (RON). The design of experiments which study the optimum volumetric percentages of the four variables, ethanol, toluene, and ether and xylene materials leads to 30 experiments. The results obtained show that RON can reach a value of 103.1 (30.5% RON improvement) when a formula of composite octane number blending enhancer containing a volumetric percentage of 15, 25, 25 volumetric percent of ethanol, toluene and xylene respectively. The cost study in comparison with the price of high octane number gasoline sold in Iraq show that this formula has a high cost of 2050 Iraqi Dinar (IQD)/liter gasoline, while  the formula of composite octane number blending enhancer containing 15% volumetric percentage of Ethanol only leading to gasoline of 89.6 RON (13.4 % ON improvement) gave minimum cost of 300 IQD / liter gasoline for the blend of octane number enhancer making the total price of the gasoline to be competitive with the high ON gasoline imported from outside Iraq.  While the formula of 7.5, 12.5, 37.5 and 5% volumetric percentage of ethanol, toluene, xylene, and ether respectively have a maximum cost of 2525 IQD of produced gasoline of 101.3 RON (octane number improved by 28.23%).  


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