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A central composite design involving oil fraction and gum content was used.
As a result, both the Europeans and Japanese generally crack a naphtha or light gas oil fraction to produce a full range of olefin products.
Raw rapeseed bio-oil, bio-oil fraction boiling at the temperature over 120 °C and bio-oil blend with non-desulfurized light gas oil fraction were submitted to hydrorefining studies.
Gas liquid phase mass transport and equilibrium are considered by simulating the petroleum gas oil fraction with five pseudocomponents.
We also investigated model extensibility for changes in the oil fraction, emulsion flow rate and rotor speed.
The procedure followed to determine the oil fraction and a summary of advantages and disadvantages of each method are given.
The effects of shear rate, surfactant species and concentration, temperature and oil fraction on emulsion inversion were studied.
The supports effect was examined by comparing thiophene conversion and sulphur or nitrogen contents in diesel oil fraction.
In this study, we compare four approaches to determine the volume of the collected oil fraction in core flooding effluents.
Hydrorefining products of bio-oil and light gas oil fraction blend fulfilled majority of fuel oil commercial requirements.
In this work the system (propane + carbon dioxide + water) has been chosen as a model (light oil fraction + carbon dioxide + water) mixture.
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