Abubakar Ibrahim

Surfactants are amphiphilic compounds that enable the mixing of immiscible substances like oil and water by reducing interfacial tension. However, their application in Enhanced Oil Recovery (EOR) is limited by issues such as toxicity, poor biodegradability, and dependence on edible oils, which can compromise food security. This study focused on synthesizing a non-ionic surfactant from neem (Azadirachta indica) seed oil—a non-edible, biodegradable alternative. Neem seeds were collected from Bayero University Kano, dried for six weeks, and subjected to proximate and Fourier Transform Infrared Spectroscopy (FTIR) analyses. Proximate analysis revealed 28.76% moisture, 14.44% oil/fat, 16.67% protein, and 5.1% ash. FTIR analysis identified key functional groups such as O-H, C-H, and C?N stretching. Oil extraction was carried out using Soxhlet apparatus with 800 ml of n-hexane at 65°C for 1.2 hours, yielding 23% oil, consistent with literature values. The extracted oil showed an acid value of 1.88 mg KOH/g and a saponification value of 184.8 mg KOH/g, indicating suitability for surfactant synthesis. Further FTIR analysis confirmed the presence of functional groups like C-H, C=O, CH2, CH3, C-O, and -(CH2)-n. A non-ionic surfactant was synthesized by reacting 10 ml of neem oil with 5 g NaOH at 80 °C for 2.5 hours, along with 50 ml of distilled water under continuous stirring. FTIR analysis of the product revealed characteristic O-H, COO?, and C-O functional groups, confirming successful surfactant formation. The findings support neem oil as a viable, sustainable surfactant source for EOR applications.

Oil shale kerogen pyrolysis is typically crucial for optimizing production efficiency. This research investigates the thermal degradation behavior of Bida oil shale kerogen using thermogravimetric analysis (TGA) at varying heating rates (10, 20, 30, and 40 °C/min) . This study employs kinetic analysis methods including Kissinger (K), Flynn–wall–Ozawa (FWO), Kissinger-Akahira-Sunose, (KAS) and Distributed Activation Energy Model (DAEM) to elucidate the complex decomposition behavior. The research provides novel insights into the temperature-dependent variations in oil shale pyrolysis, revealing significant impacts of heating rates on decomposition temperatures and kinetics. Notably, increasing heating rates led to a shift in decomposition temperatures, attributed to differences in heat transfer efficiencies within the sample. Distinct stages of decomposition were observed, with devolatilization initiating around 260°C and progressing rapidly until approximately 526 °C, followed by a gradual decline in decomposition rate. Kinetic analysis using KAS, and FWO provided valuable insights into activation energies (Ea) and pre-exponential factors (A). Ea ranged from 64.945 to 86.94 kJ/mol, indicating a complex decomposition mechanism influenced by varying conversion levels. The DAEM further elucidated the kinetics of oil shale decomposition, highlighting the heterogeneity of pyrolytic processes under different heating rates. The average Ea and frequency factor calculated using the DAEM method were 64.95 kJ mol-1 and 1.87 × 105 min-1. It was observed that the results obtained from the methods differed from each other due to the complex mechanism of reaction occurring during the pyrolysis process and the effect of different heating rates. The findings contribute to refining kinetic models for oil shale pyrolysis, shedding light on critical factors shaping thermal degradation behavior.