dc.description.abstract |
Crude oil after preliminary treatments is subjected to refining so as to get
marketable products like naphtha, gasoline, kerosene, diesel fuel, lubricating oil feed
stock, furnace oil, etc. A large amount of asphalt/bitumen is left over as residue. Owing
to its high viscosity, density and contamination by sediments as well as high asphaltene
and resin contents, the residue cannot be directly used as a boiler fuel and instead used
for non-fuel purposes. The global demand for energy continues and will increase over
the next few decades as the world's energy consumption will increase phenomenally in
the next few decades. Alternative energy sources like nuclear and renewable energy
have attracted much attention in the recent years, however, the main role of these
sources, will be to supplant, rather than to substitute the fossil fuels. Therefore, major
breakthroughs in the oil industry's core science and engineering are needed so as to
meet with the World's growing energy demand for petro-fuels. The high yields of
residue/residuum is an ongoing challenge at a refinery and economic & strategic
reasons demands the exploitation of residual streams. Accordingly, the selection of
proper processes may play a key role so as to cope with the challenge.
The objective of the present thesis was to employ atmospheric distillation
process using three crude oils dispersed with chemical surfactants in order to get lighter
fuel fractions in high yields in comparison with the plain crudes (control). The thesis
summarizes the characterization of the crude oils with respect to their key physicochemical
properties including density (kg/m3), viscosity (mPa·s), API gravity, total acid
number (mg KOH/g), and asphaltene contents (wt %). Chemical dispersants i.e. sodium
dodecyl sulfate (SDS); a anionic surfactant, hexa decyltrimethylammonium bromide as
cationic surfactant, and Triton-X as neutral surfactant were used. The crude oils
investigated included paraffinic (denoted as RCP-I), naphthenic (denoted as RCN-II)
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and aromatic (denoted as RCA-III) Pakistani crudes. Each crude oil was spiked with
the varying dispersant –to-oil ratios (5:100, 10:100, 15:100, 20:100, 25:100 and 30:100)
and then subjected to atmospheric distillation. The distillation of each surfactantdispersed
crude oil was carried out in comparative experiments with the plain crude oil
so as to investigate the effect of each dispersant on the yield, chemical composition and
fuel properties of the derived distillate fractions (F1, F2 and F3). The Gas
Chromatographic-Mass Spectrometric analysis (GC-MS) was carried out in order to
ascertain compositional stability of the distillate fractions. The desired fuel properties
of the light fractions were also determined as per ASTM standards and compared with
the generic gasoline and diesel fuel samples.
Looking at the results, we conclude that using chemically dispersed crudes
enabled to obtain better yields of the light distillate fractions in comparison with the
control without disturbing the key fuel properties. Among the three crudes used, the
SDS-dispersed RCA-III, CTAB-dispersed RCN-II andTriton-X-100-dispersed RCN-II
crudes were more effective which gave significant increase in the yields of light
distillate fractions and reduced the residues without disturbing the fuel quality criteria. |
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