The Bamiléké Plateau represents a key domain in the understanding of the geodynamics associated with the central Cameroon shear. The study aimed to highlight the subsurface architecture of the plateaus basem...The Bamiléké Plateau represents a key domain in the understanding of the geodynamics associated with the central Cameroon shear. The study aimed to highlight the subsurface architecture of the plateaus basement setting with focus on high potential areas for hydrogeological and mining development projects. To this end, geological field observations were carried out. Since the structures sought were near-surface, a separation approach based on the upward continuation method was applied to the Bouguer anomaly grid. A set of processing techniques, including vertical derivative or DZ, analytical signal or SA and categorization of gravity signatures, was applied to generate the residual map. The synthesis geological model, obtained from analysis and interpretation of the various transformed maps and 2.5D modeling of two gravity profiles P1 and P2 highlights the following features: 1) intrusions of steep-sided granitic batholiths from Dschang to Bandjoun (profile P1), increasing in width from NW (Dschang) to SE (Bandjoun);2) larger volume batholiths with moderate sides located at Bafang and Bangangté (profile P1). These plutonic massifs were weakened by brittle deformation, which favored the emplacement of phonolite or anorthosite dykes within them. The emplacement of these dykes was accompanied by compressional faults with high dip between Dschang and Bandjoun and extensional faults with medium dip between Bafang and Bangangté. These fault zones (trending N85E to N95E) are ideal for hydrogeological investigations in a basement setting, as well as a series of dyke networks that could potentially be preferred zones for the circulation and accumulation of useful substances. The resulting geological sections P1 and P2 highlight the influence of granitic intrusions in the geological system of the study area, as well as the structural control associated with the various dyke intrusions. All the models obtained can serve as fundamental references for hydrogeological and mining exploration project on the Bamiléké Plateau.展开更多
In this paper, we propose an efficient adaptive iteratively reweighted l<sub>1</sub> algorithm (A-IRL1 algorithm) for solving the elastic l<sub>q</sub> regularization problem. We prove that the...In this paper, we propose an efficient adaptive iteratively reweighted l<sub>1</sub> algorithm (A-IRL1 algorithm) for solving the elastic l<sub>q</sub> regularization problem. We prove that the sequence generated by the A-IRL1 algorithm is convergent for any rational and the limit is a critical point of the elastic l<sub>q</sub> regularization problem. Under certain conditions, we present an error bound for the limit point of convergent sequence.展开更多
<div style="text-align:justify;"> The rate of Methanol synthesis over a Cu/ZnO/Al<sub><span style="font-family:Verdana;">2</span></sub><span style="font-family...<div style="text-align:justify;"> The rate of Methanol synthesis over a Cu/ZnO/Al<sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">O</span><sub><span style="font-family:Verdana;">3</span></sub><span style="font-family:Verdana;"> (60:30:10) catalyst has been measured using CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> (10:90) and CO/CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> (10:10:80) streams at 433, 443, 453, 463 and 473 K. Using the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream, it requires 12 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s to achieve </span><span style="font-family:Verdana;">steady</span><span style="font-family:Verdana;">-</span><span style="font-family:Verdana;">state</span><span "=""><span style="font-family:Verdana;"> performance;this time reduces to 5.4 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s on increasing the temperature to 463 K. Using the CO/CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream, steady State performance is not achieved even after 14.4 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s at 433 K but is achieved after 9 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s at 463 K. Significant deviations from </span><span style="font-family:Verdana;">steady state</span><span style="font-family:Verdana;"> behavior (~40% of </span><span style="font-family:Verdana;">steady state</span><span style="font-family:Verdana;">) are observed only at 453 K and only using the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> feed when gas chromatography (GC) is the analysis system. When the reactor output is connected directly into a flame ionization detector (FID), </span><span style="font-family:Verdana;">oscillation</span> </span><span style="font-family:Verdana;">is</span><span "=""><span style="font-family:Verdana;"> observed at all temperatures studied using a CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream. Injection of CO into the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream, which is synthesizing methanol at 473 K, produces a sharply spiked increase in the rate of methanol synthesis followed by an oscillatory relaxation to </span><span style="font-family:Verdana;">steady state</span><span style="font-family:Verdana;"> behavior. At 433 and 443</span><span style="font-family:Verdana;"> K</span></span><span style="font-family:Verdana;">,</span><span "=""> </span><span "=""><span style="font-family:Verdana;">the injection of CO into the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream again </span><span style="font-family:Verdana;">produce</span></span><span style="font-family:Verdana;">s</span><span style="font-family:Verdana;"> the sharply spiked increase in the rater of methanol synthesis, which returns to the baseline value without oscillations.</span> </div>展开更多
MoO<sub>3</sub> and 5% MoO<sub>3</sub>/ZnO were prepared by impregnation method using (NH<sub>4</sub>)<sub>6</sub>Mo<sub>7</sub>O<sub>24</sub>, 4...MoO<sub>3</sub> and 5% MoO<sub>3</sub>/ZnO were prepared by impregnation method using (NH<sub>4</sub>)<sub>6</sub>Mo<sub>7</sub>O<sub>24</sub>, 4H<sub>2</sub>O as precursor and ZnO as support. The prepared samples were characterized by X-ray diffraction (XRD), scanning electronic microscopy (SEM), infra red (FTIR) <span style="font-family:;" "="">and</span><span style="font-family:;" "=""> UV-Vis diffuse reflectance (DRS)</span><span> </span><span style="font-family:;" "="">spectroscopies and pho<span>to-electrochemistry. The XRD pattern showed that the MoO<sub>3</sub> powder treated at 700°C is a single-phase crystallizing in an orthorhombic structure with a direct optical transition </span></span><span style="font-family:;" "="">(</span><span style="font-family:;" "="">2.70 eV</span><span style="font-family:;" "="">)</span><span style="font-family:;" "="">. The hetero-junction 5% MoO<sub>3</sub>/ZnO</span><span style="font-family:;" "=""> was photo-electrochemically characterized to assess its feasibility for H<sub>2</sub> production under visible light. The capacitance potential (<i>C<sup>-</sup></i><sup>2</sup><i> f</i>(<i>E</i>)) characteristic of MoO<sub>3</sub> plotted in Na<sub>2</sub>SO<sub>4</sub>, (0.1 M) electrolyte indicates <i>n-</i>type conduction with a flat band potential of -</span><span style="font-family:;" "=""><span>0.54 V<i><sub>SCE</sub></i>. The photocatalytic activity was performed for the photoreduction of water to hydrogen under visible light illumination. The best performance occurs at pH ~ 7 with an evolved volume of 5.9 mL.</span></span>展开更多
文摘The Bamiléké Plateau represents a key domain in the understanding of the geodynamics associated with the central Cameroon shear. The study aimed to highlight the subsurface architecture of the plateaus basement setting with focus on high potential areas for hydrogeological and mining development projects. To this end, geological field observations were carried out. Since the structures sought were near-surface, a separation approach based on the upward continuation method was applied to the Bouguer anomaly grid. A set of processing techniques, including vertical derivative or DZ, analytical signal or SA and categorization of gravity signatures, was applied to generate the residual map. The synthesis geological model, obtained from analysis and interpretation of the various transformed maps and 2.5D modeling of two gravity profiles P1 and P2 highlights the following features: 1) intrusions of steep-sided granitic batholiths from Dschang to Bandjoun (profile P1), increasing in width from NW (Dschang) to SE (Bandjoun);2) larger volume batholiths with moderate sides located at Bafang and Bangangté (profile P1). These plutonic massifs were weakened by brittle deformation, which favored the emplacement of phonolite or anorthosite dykes within them. The emplacement of these dykes was accompanied by compressional faults with high dip between Dschang and Bandjoun and extensional faults with medium dip between Bafang and Bangangté. These fault zones (trending N85E to N95E) are ideal for hydrogeological investigations in a basement setting, as well as a series of dyke networks that could potentially be preferred zones for the circulation and accumulation of useful substances. The resulting geological sections P1 and P2 highlight the influence of granitic intrusions in the geological system of the study area, as well as the structural control associated with the various dyke intrusions. All the models obtained can serve as fundamental references for hydrogeological and mining exploration project on the Bamiléké Plateau.
文摘In this paper, we propose an efficient adaptive iteratively reweighted l<sub>1</sub> algorithm (A-IRL1 algorithm) for solving the elastic l<sub>q</sub> regularization problem. We prove that the sequence generated by the A-IRL1 algorithm is convergent for any rational and the limit is a critical point of the elastic l<sub>q</sub> regularization problem. Under certain conditions, we present an error bound for the limit point of convergent sequence.
文摘<div style="text-align:justify;"> The rate of Methanol synthesis over a Cu/ZnO/Al<sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">O</span><sub><span style="font-family:Verdana;">3</span></sub><span style="font-family:Verdana;"> (60:30:10) catalyst has been measured using CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> (10:90) and CO/CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> (10:10:80) streams at 433, 443, 453, 463 and 473 K. Using the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream, it requires 12 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s to achieve </span><span style="font-family:Verdana;">steady</span><span style="font-family:Verdana;">-</span><span style="font-family:Verdana;">state</span><span "=""><span style="font-family:Verdana;"> performance;this time reduces to 5.4 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s on increasing the temperature to 463 K. Using the CO/CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream, steady State performance is not achieved even after 14.4 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s at 433 K but is achieved after 9 × 10</span><sup><span style="font-family:Verdana;">3</span></sup><span style="font-family:Verdana;"> s at 463 K. Significant deviations from </span><span style="font-family:Verdana;">steady state</span><span style="font-family:Verdana;"> behavior (~40% of </span><span style="font-family:Verdana;">steady state</span><span style="font-family:Verdana;">) are observed only at 453 K and only using the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> feed when gas chromatography (GC) is the analysis system. When the reactor output is connected directly into a flame ionization detector (FID), </span><span style="font-family:Verdana;">oscillation</span> </span><span style="font-family:Verdana;">is</span><span "=""><span style="font-family:Verdana;"> observed at all temperatures studied using a CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream. Injection of CO into the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream, which is synthesizing methanol at 473 K, produces a sharply spiked increase in the rate of methanol synthesis followed by an oscillatory relaxation to </span><span style="font-family:Verdana;">steady state</span><span style="font-family:Verdana;"> behavior. At 433 and 443</span><span style="font-family:Verdana;"> K</span></span><span style="font-family:Verdana;">,</span><span "=""> </span><span "=""><span style="font-family:Verdana;">the injection of CO into the CO</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;">/H</span><sub><span style="font-family:Verdana;">2</span></sub><span style="font-family:Verdana;"> stream again </span><span style="font-family:Verdana;">produce</span></span><span style="font-family:Verdana;">s</span><span style="font-family:Verdana;"> the sharply spiked increase in the rater of methanol synthesis, which returns to the baseline value without oscillations.</span> </div>
文摘MoO<sub>3</sub> and 5% MoO<sub>3</sub>/ZnO were prepared by impregnation method using (NH<sub>4</sub>)<sub>6</sub>Mo<sub>7</sub>O<sub>24</sub>, 4H<sub>2</sub>O as precursor and ZnO as support. The prepared samples were characterized by X-ray diffraction (XRD), scanning electronic microscopy (SEM), infra red (FTIR) <span style="font-family:;" "="">and</span><span style="font-family:;" "=""> UV-Vis diffuse reflectance (DRS)</span><span> </span><span style="font-family:;" "="">spectroscopies and pho<span>to-electrochemistry. The XRD pattern showed that the MoO<sub>3</sub> powder treated at 700°C is a single-phase crystallizing in an orthorhombic structure with a direct optical transition </span></span><span style="font-family:;" "="">(</span><span style="font-family:;" "="">2.70 eV</span><span style="font-family:;" "="">)</span><span style="font-family:;" "="">. The hetero-junction 5% MoO<sub>3</sub>/ZnO</span><span style="font-family:;" "=""> was photo-electrochemically characterized to assess its feasibility for H<sub>2</sub> production under visible light. The capacitance potential (<i>C<sup>-</sup></i><sup>2</sup><i> f</i>(<i>E</i>)) characteristic of MoO<sub>3</sub> plotted in Na<sub>2</sub>SO<sub>4</sub>, (0.1 M) electrolyte indicates <i>n-</i>type conduction with a flat band potential of -</span><span style="font-family:;" "=""><span>0.54 V<i><sub>SCE</sub></i>. The photocatalytic activity was performed for the photoreduction of water to hydrogen under visible light illumination. The best performance occurs at pH ~ 7 with an evolved volume of 5.9 mL.</span></span>