Modeling of thermal cracking reaction of kerosene range hydrocarbons

Author(s):  
Namrata Upreti ◽  
Himavarsha Pakala ◽  
Vikranth K. Surasani ◽  
Srikanta Dinda
2019 ◽  
Vol 58 (36) ◽  
pp. 16417-16430
Author(s):  
Andre Guerra ◽  
Robert Symonds ◽  
Samantha Bryson ◽  
Christopher Kirney ◽  
Barbara Di Bacco ◽  
...  

2009 ◽  
Vol 23 (12) ◽  
pp. 6156-6162 ◽  
Author(s):  
Tomoaki Namioka ◽  
Young-il Son ◽  
Masayuki Sato ◽  
Kunio Yoshikawa

2021 ◽  
Vol 22 (2) ◽  
pp. 7-16
Author(s):  
ABIMBOLA GEORGE OLAREMU ◽  
Ezekiel Oluyemi ODEBUNMI ◽  
Jim A ANDERSON

The increasing population growth resulting in the tremendous increase in consumption of fuels, energy, and petrochemical products and coupled with the depletion in conventional crude oil reserves and production make it imperative for Nigeria to explore her bitumen reserves so as to meet her energy and petrochemicals needs. Samples of Agbabu bitumen were subjected to thermal cracking in a tubular steel reactor operated at 10 bar pressure to investigate the effect of temperature on the cracking reaction. The gas produced was analyzed in a Gas Chromatograph while the liquid products were subjected to Gas Chromatography-Mass Spectrometry (GC-MS) analysis. Heptane was the dominant gas produced in bitumen cracking at all temperatures and the reaction products show a distribution of lighter hydrocarbons most of which are in the gasoline range. The product distribution of bitumen conversion depends strongly on the cracking temperature and the oil produced contains the valuable liquid fractions. The products of thermal cracking of bitumen can be classified into the following groups; alkanes, alkenes, amines, aromatics, alkanoic acids, alkanols, esters, ethers, ketones, sulphur compounds, and nitrogen compounds. The activation energies of the products formed were determined. The LNG produced all have unusually low values activation energy (hence easily converted) pointing to the high quality of Agbabu crude      The conversion process was affected by the reaction time and suggests that the transformation of bitumen into smaller fractions follows a definite reaction scheme in which the heavy oil transformed to lower fractions and was subsequently converted to smaller liquid fractions and gases.


2014 ◽  
Vol 77 ◽  
pp. 7-12 ◽  
Author(s):  
Linhua Song ◽  
Mingming Hu ◽  
Dong Liu ◽  
Daoxiang Zhang ◽  
Cuiyu Jiang

2021 ◽  
Vol 35 (4) ◽  
pp. 3295-3306
Author(s):  
Hailing Sun ◽  
Liyuan Cao ◽  
Yuhao Zhang ◽  
Liang Zhao ◽  
Jinsen Gao ◽  
...  

Author(s):  
Andrew Z. Boeckmann ◽  
Zakaria El-tayash ◽  
J. Erik Loehr

Some U.S. transportation agencies have recently applied mass concrete provisions to drilled shafts, imposing limits on maximum temperatures and maximum temperature differentials. On one hand, temperatures commonly observed in large-diameter drilled shafts have been observed to cause delayed ettringite formation (DEF) and thermal cracking in above-ground concrete elements. On the other, the reinforcement and confinement unique to drilled shafts should provide resistance to thermal cracking, and the provisions that have been applied are based on dated practices for above-ground concrete. This paper establishes a rational procedure for design of drilled shafts for durability requirements in response to hydration temperatures, which addresses both DEF and thermal cracking. DEF is addressed through maximum temperature differential limitations that are based on concrete mix design parameters. Thermal cracking is addressed through calculations that explicitly consider the thermo-mechanical response of concrete for predicted temperatures. Results from application of the procedure indicate consideration of DEF and thermal cracking potential for drilled shafts is prudent, but provisions that have been applied to date are overly restrictive in many circumstances, particularly the commonly adopted 35°F maximum temperature differential provision.


2020 ◽  
Author(s):  
Heri Soedarmanto ◽  
Sudjito ◽  
Widya Wijayanti ◽  
Nurkholis Hamidi ◽  
Evy Setiawati

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