Results 31 to 40 of about 12,867 (222)
Decarbonisation of olefin processes using biomass pyrolysis oil [PDF]
, 1973 An imperative step toward decarbonisation of current industrial processes is to substitute their petroleum-derived feedstocks with biomass and biomass-derived feedstocks.
Sharifzadeh, M, Wang, L, Shah, NG
core +5 more sources
Aromatization of Heavy Naphtha using Modified Zeolite Supported Catalyst
International Journal of Engineering & Technology, 2019 Growing population has increased the dependency toward sustainable energy sources. Research industries have groomed their facilities to find alternative sources of energy. Heavy naphtha can be converted to value added fuel such as gasoline via catalytic conversion.
A Fakruldin, A Ramli, M I. Abdul Mutalib
openaire +2 more sources
Thermal Cracking of Jatropha Oil with Hydrogen to Produce Bio-Fuel Oil
Energies, 2016 This study used thermal cracking with hydrogen (HTC) to produce bio-fuel oil (BFO) from jatropha oil (JO) and to improve its quality. We conducted HTC with different hydrogen pressures (PH2; 0–2.07 MPa or 0–300 psig), retention times (tr; 40–780 min ...
Yi-Yu Wang +11 more
doaj +1 more source
Adsorption Desulfurization Of Iraqi Heavy Naphtha Using Zeolite 13x
Association of Arab Universities Journal of Engineering Sciences, 2019 This work was conducted to study the effect of selective adsorption on removal of sulfur compounds from Iraqi heavy naphtha from Al-Dura refinery by using molecular sieve (13X) in a fixed-bed column and it was be run out at 1.5–6.0h-1 LHSV, 15–30 gr weight of molecular sieve (13X), 600–1650ppm sulfur concentration in the feedstock , the ...
Hussein Qasim Hussein +1 more
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Crystal structure of the yellow 1:2 molecular complex lumiflavin–bisnaphthalene-2,3-diol [PDF]
, 1971 In the first molecular complex of the physiologically active neutral form of isoalloxazine studied, lumiflavin–bisnaphthalene-2,3-diol, each flavin is sandwiched between two naphthalenediol molecules with extensive overlap but a moderately large (3·44 Å)
Fritchie, Charles J., Jun. +4 more
core +1 more source
The Canadian Journal of Chemical Engineering, EarlyView.Abstract Acid catalyzed conversion of durene by isomerization, disproportionation, and transalkylation is of interest to the development of a methanol‐to‐jet process to reduce the amount of durene in the kerosene. It was of interest to determine whether durene conversion could be performed at a temperature lower than 350°C.
Aida G. Velasco Ortiz +2 more
wiley +1 more source
Advances of two-stage riser catalytic cracking of heavy oil for maximizing propylene yield (TMP) process [PDF]
, 2014 Two-stage riser catalytic cracking of heavy oil for maximizing propylene yield (TMP) process proposed by State Key Laboratory of Heavy oil Processing, China University of Petroleum, can remarkably enhance the propylene yield and minimize the dry gas and ...
Chen Xiaobo +4 more
core +1 more source
Polyethylene waste co-processing in fluid catalytic cracking plants
Cleaner Engineering and TechnologyPlastics pollution is an overwhelming environmental problem that must be solved as soon as possible. Refining processes such as the Fluidized Catalytic Cracking (FCC) process with a global capacity of 14 million barrels per day, may help to solve it in ...
Felipe de Jesús Ortega García +1 more
doaj +1 more source
Modeling and Optimizing a Vacuum Gas Oil Hydrocracking Plant using an Artificial Neural Network
International Journal of Technology, 2018 In this research, based on actual data gathered from an industrial scale vacuum gas oil (VGO) hydrocracker and artificial neural network (ANN) method, a model is proposed to simulate yields of products including light gases, liquefied petroleum gas (LPG),
Sepehr Sadighi +2 more
doaj +1 more source
Characterization of naphtha produced from coprocessing coal-heavy oil
Fuel Processing Technology, 1988 Abstract Capillary gas chromatography proved useful for characterizing naphtha produced from coprocessing coal and heavy oil at various conditions. Increasing the coal concentration in the feedstock resulted in higher contents of phenols, indan and cyclohexanes in the naphtha product. Increasing the reaction temperature resulted in higher contents of
B.A. Farnand, P.M. Rahimi, S.A. Fouda
openaire +1 more source