11.-Correlations for Predicting Vapour – Solid Equilibrium Constants

The reliability of prediction models in determining hydrate forming temperatures adequately is of
paramount importance. Most correlations have been found to vary significantly from experimental
hydrate forming temperature data. This study is focused on developing correlations for predicting
vapour solid constants for methane, ethane, propane, iso – butane, normal – butane, carbon IV
oxide and hydrogen sulphide by extracting over 2000 data points from the GPSA chart. The
correlations developed in this study were used to develop a computer program for predicting
natural gas hydrate formation temperatures for mitigating the challenges posed by natural gas
hydrate formation in process installations. The correlations gave correlation coefficients between
0.9 and 0.99. The computer model developed gave an average relative error of -3.73%, coefficient
of correlation of 0.94 and a standard deviation of 5.9%.

12.-Evaluation of Steady and Unsteady Flow Phenomena Using Computational Fluid Dynamics (CFD) Modelling Methodology in Circulating Fluidised Bed (CFB)/Fluid Catalytic Cracking (FCC) Reactor Systems.

The simulation framework was developed from the licensed computational fluid dynamics
(CFD15) software to simulate the hydrodynamics of gas-solid flow in CFB/FCC riser
reactors. The predictions from the commercial CFD code (CFX and fluent) were based on
the Eulerian-Eulerian multiphase model using k-ε model. A validation using published
experimental data from the open literature was conducted. The flow model is based on an
Eulerian-Eulerian description of the phases where the kinetic theory for granular flow
(KTGF) forms the basis for the turbulence modelling in the solid phases. In addition, for
constant diametre and particle density, better understanding of the hydrodynamics of the gassolid flow, under
various loading of gas and solid flux were achieved. Within the limit of the computational error, it was found that the choice of the ANSYS Fluent solver provide the best understanding on the gas-solid hydrodynamics in CFB/FCC riser systems. In addition, the availability of transport KTGF in Fluent solver was a focus reason why the concluded choices of establishing a better understanding of the gas-solid hydrodynamics in riser reactors were deduced.

13.-A Review of 3G Data on The Nigerian Benue Trough in View Of Renewed Hydrocarbon Exploration Campaigns

The Nigerian National Petroleum Corporation (NNPC) has commenced another round of
exploration campaigns for possible hydrocarbon deposits in the Nigerian Benue Trough. The
Benue Trough, divided into lower, middle and upper portions, is a SW-NE trending intracratonic
basin containing Cretaceous-Tertiary sediment fill of up to 6,000 m. Appreciable volumes of 3G 1
data had been generated on the basin by several previous attempts by NNPC and its joint venture
partners. Geological profiles juxtaposed against geophysical data have delineated more
prospective areas in the basin where sediment thicknesses vis-à-vis depths to basement are
relatively large. Organic geochemical data have been interpreted in terms of organic matter
maturation, hydrocarbon generation, expulsion, and migration culminating in the understanding
of the volume and stratigraphy of potential source rocks. Consequently, in the Middle Benue
Trough, source rock facies have been identified in the carbonaceous shales of the Keana-Awe,
Ezeaku and Awgu Formations, with most prospective parts covering the areas within and around
Lafia, Loko, Dedere, Doma and Shabu where the Lafia Formation has added to the sediment
thickness. In the Upper Benue Trough, source rock facies comprise the carbonaceous intervals
within the Gongila, Pindiga and Fika Formations with more prospective areas covering the areas
within and around Gombe, Gombe-Aba, Dukku, and Akko where the Kerri-Kerri Formation has
added to the sediment thickness. Previous efforts by Shell (SNEPCO) has tested little oil and more
gas in the Kolmani River-1 well drilled at Futuk near Alkaleri, spudding on the Kerri-Kerri and
bottoming on the Yolde. Considered against analogs in similar rifted basins in Chad Republic,
Sudan, Uganda and Kenya, there are possibilities for commercial oil and gas discoveries in the
Benue Trough.

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6.-Synthesis and Characterization of Organo-bentonites for possible Use in the Removal of PAHs from Petrochemical Industries Wastewater Effluents

Organo-bentonites have been synthesized through ion-exchange reaction using benzyl dimethyl dodecyl ammonium (BDMDA), dioctadecyl dimethyl ammonium (DODMA) chloride; tetraphenyl phosphonium (TPP) and hexadecyl pyridinium (HDP) bromides. The unmodified and modified samples were studied with Fourier transform infrared (FT-IR) spectroscopy, Xray diffraction (XRD) technique, and Scanning electron microscopy (SEM). The
basal spacing of the unmodified bentonite was 17.123Å and after modification it increased to 22.071Å and 20.066Å
at 1.0CEC for BDMDA and DODMA respectively. With 1.5CEC of TPP and 2.0CEC of HDP the basal spacing
increased to 20.250Å and 18.205Å respectively. The FT-IR studies also revealed structural differences between
the modified and unmodified bentonite samples. The IR spectra of the modified bentonite showed C-H asymmetric stretching at 2928cm -1 for BDMD 2920cm-1 for DODMA and 2918cm-1 for HDP, symmetric stretching at 853cm-1 for BDMD, 2851cm-1 for DODMA and 2851cm-1 HDP and bending vibrations at 1460cm -1 for BDMDA, 469cm-1 for DODMA and 1469cm-1 for HDP with respect to long alkyl chains in BDMDA, DODMA and HDP. The vibration associated with pyridinium was observed at 1490cm-1 in HDP modified bentonite. The C=C stretching vibrations in the phenyl ring were at 1587cm-1 and 1441cm-1 while attachment of the phenyl rings to phosphonium ion were observed at 1587cm-1 , 1441cm-1 , and 1438cm-1 with respect to TPP modified sample. Results
of the SEM revealed a tendency towards flakes/grain like formation and agglomeration.

7.-Optimization of Transesterification of Castor Oil through Response Surface Methodology

This study was aimed at optimizing the yield of transesterification of castor oil methyl ester (COME)
from castor oil using response surface methodology (RSM). RSM was used to analyse and optimize
the operating variables for the transesterification process. Box – Behnken design (BBD) was employed to study the effects of reaction temperature (oC), time (min), catalyst concentration (wt.%) and methanol to oil ratio (v/v) on the yield of COME. A total of 29 experimental runs which were generated by BBD were carried out. The results of RSM analysis indicated that reaction temperature, catalyst concentration and methanol to oil volume ratio were significant variables on the yield of COME. The coefficient of determination obtained (R2 = 0.9713) showed a fitness of a second order model. The interactive effect of catalyst concentration and methanol to oil volume ratio exhibited a positive effect on the COME yield. The optimum conditions for the transesterification reaction based
on the second – order quadratic model was found to be; temperature 46.88oC, reaction time 107.41
min, catalyst concentration 1.03 wt.% and methanol to oil ratio 0.44 v/v. The second order quadratic
model developed provides a statistical approach to predicting the optimum yield of COME.

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