The oil industry is divided into two sectors: the upstream sector, which involves exploration and production, and the. The downstream sector of the oil industry, comprising refining and distribution, plays a key role in converting crude oil into economically valuable products. Oil refining involves a range of processes that transform crude oil into fuels (LPG, gasoline, diesel), combustibles (fuel oils), and specialty products (waxes, paraffins), all of which must meet regularly updated standards. These operations are conducted in refineries, which are classified as either simple (few units) or complex (many units, allowing for more efficient and diverse output). The refining process produces various fractions, including combustible gases (C1-C2), LPG, gasoline fractions (C5-C10), kerosene (C10-C13), gas oils (C13-C25), and heavier products (C20-C50) that undergo cracking to yield lighter products. This study focuses on evaluating the physicochemical properties of premium gasoline sold in Brazzaville, Republic of Congo. The analysis of multiple samples showed that fuel sold by private vendors is of lower quality than that sold at official service stations. Key parameters assessed include density, specific gravity, viscosity, and pH.
Published in | World Journal of Applied Chemistry (Volume 10, Issue 4) |
DOI | 10.11648/j.wjac.20251004.12 |
Page(s) | 101-108 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2025. Published by Science Publishing Group |
Physicochemical Properties, Super Fuel, Refining
Property | Value | Units |
---|---|---|
Mass | 0.1849 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 739.76 | kg/m3 |
Dynamic Viscosity | 0.064 | Pa·s |
Kinematic Viscosity | 8.65 × 10⁻5 | m2/s |
Specific Gravity | 0.739 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Yellow | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.1847 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 738.96 | kg/m3 |
Dynamic Viscosity | 0.070 | Pa·s |
Kinematic Viscosity | 9.47 × 10⁻5 | m2/s |
Specific Gravity | 0.738 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Yellow | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.185 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 740.12 | kg/m3 |
Dynamic Viscosity | 0.056 | Pa·s |
Kinematic Viscosity | 7.56 × 10⁻5 | m2/s |
Specific Gravity | 0.740 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Red | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.184 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 736.68 | kg/m3 |
Dynamic Viscosity | 0.078 | Pa·s |
Kinematic Viscosity | 1.05 × 10⁻4 | m2/s |
Specific Gravity | 0.736 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Dark Yellow | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.18586 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 743.44 | kg/m3 |
Dynamic Viscosity | 0.074 | Pa·s |
Kinematic Viscosity | 9.95 × 10⁻5 | m2/s |
Specific Gravity | 0.743 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Yellow | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.1899 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 759.96 | kg/m3 |
Dynamic Viscosity | 0.071 | Pa·s |
Kinematic Viscosity | 9.34 × 10⁻5 | m2/s |
Specific Gravity | 0.759 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Red | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.18618 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 744.72 | kg/m3 |
Dynamic Viscosity | 0.067 | Pa·s |
Kinematic Viscosity | 8.99 × 10⁻5 | m2/s |
Specific Gravity | 0.759 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Yellow | - |
Temperature | 20 | °C |
pH | 5 | - |
Property | Value | Units |
---|---|---|
Mass | 0.18509 | kg |
Volume | 2.5 × 10⁻4 | m3 |
Density | 740.36 | kg/m3 |
Dynamic Viscosity | 0.088 | Pa·s |
Kinematic Viscosity | 1.189 × 10⁻4 | m2/s |
Specific Gravity | 0.759 | - |
Density of Water (4°C) | 1000 | kg/m3 |
Color | Light Yellow | - |
Temperature | 20 | °C |
pH | 5 | - |
Sample Origin | Density (kg/m3) | Specific Gravity | Kinematic Viscosity (m2/s) | pH | Color |
---|---|---|---|---|---|
Puma station – Batignolles | 739.76 | 0.73976 | 8.65 × 10⁻5 | 5 | Light Yellow |
TotalEnergies station – Mazala (Mfilou) | 738.96 | 0.73896 | 9.47 × 10⁻5 | 5 | Light Yellow |
Afric station – Mouhoumi (L’Ombre) | 740.12 | 0.74012 | 7.56 × 10⁻5 | 5 | Light Red |
SNPC station – Marché Total | 736.68 | 0.73668 | 1.05 × 10⁻4 | 5 | Dark Yellow |
X-OIL station – Patte d’Oie | 743.44 | 0.74344 | 9.95 × 10⁻5 | 5 | Light Yellow |
Private seller – Mpila | 759.96 | 0.75996 | 9.34 × 10⁻5 | 5 | Light Red |
Private seller – Talangai (Dragage area) | 744.72 | 0.75972 | 8.99 × 10⁻5 | 5 | Light Yellow |
Private seller – Mouhoumi | 740.36 | 0.75936 | 1.189 × 10⁻4 | 5 | Light Yellow |
pH | Hydrogen Potential |
[1] | Christine Travers and Olivier Clause (2002), Refining Crude Oil: Producing Gasoline through Catalytic Reforming, L’Actualité Chimique – May-June 2002, pp. 1, 16. |
[2] |
Christine Boust (2013). Petroleum Solvents. National Institute for Research and Safety for the Prevention of Occupational Accidents and Diseases, 2nd Edition, Paris, 2013, p. 1. Available at:
https://www.connaissancedesenergies.org/fiche-pedagogique/raffinage-petrolier |
[3] |
Technology of Water, Oils & Fuels. Available at:
https://www.ispm.ac.ma/wp-content/uploads/2020/03/S80-Technologie-des-huiles-combustibles.pdf |
[4] | Stephen J. Hawkes (2004): The concept viscosity, Journal of Chemical Education. Vol 81. N°1. January 2004. p. 14-15. |
[5] | Fleur Longuetaud, Frédéric Mothe, Philippe Santenoise, Mickaël M. Rivoire, Mériem Fournier, et al. (2014). Exploratory Study of Density: Influence of the "Water Saturation Level" in Fresh Wood. Technical Meetings of the National Forests Office, No. 44, pp. 65–72. hal-02629454. |
[6] | Berry, U., Ndzessou, W. B., Nkeletela, L. B., Samba, R. E. J. and Makaya Poaty, E. (2025) Study of the Viscosity of Petroleum Products Using Hoppler’s Method. Advances in Materials Physics and Chemistry, 15, 91-100. |
[7] | Kouassi, K. E., Abollé, A., Yao, B., and Boa, D. (2015). Comparative Transesterification Tests by Methanolysis and Ethanolysis of Palm Oil: Measurement of Density and Viscosity in Relation to Molecular Structure. International Journal of Innovation and Applied Studies, 12, 918–930. |
[8] | Kouassi, K. E., Abollé, A., Kouakou, K. O.-M., Boa, D., Kré, N. R. and Yao, K. B. (2024) Optimization of Biofuel Formulation by Mixture Design. Advances in Chemical Engineering and Science, 14, 48-56. |
[9] | R. Byron Bird, Warren E. Stewart Edwin, N. Lightfoot (2002): Transport Phenomena, Chemical Engineering Department University of Wisconsin-Madison, John Wiley & Sons, Inc, p. 13. |
[10] | Stanislas Ulrich Berry Moukila, Laurette Brigelia Nkeletela, René Samba, Olivier Mabiala Mikanou, Roger Makosso Voula and Dherland Sandrel Kiesse. (2025). Contribution to the Production and Physicochemical Characterization of Pyrolytic Oil from Used Inner Tubes for The Production of Conventional Fuels in Congo Republic (RC), International Journal of Current Advanced Research, 14(06), pp. 289-292. |
[11] | François-Xavier Merlin (2008). Unleaded Gasoline. Chemical Intervention Guide, p. 12. |
[12] | Christine Boust, Rodolphe Lebreton, and Cosmin Patrascu (2019). Petroleum Fuels and Combustibles. National Institute for Research and Safety (INRS), p. 6. |
[13] |
International Standard Project I: Petroleum Products-Transparent and Opaque Liquids-Determination of Kinematic Viscosity and Calculation of Dynamic Viscosity, ISO/DIS 3104: 2017 (F), (09/20/2025). Available at:
https://cdn.standards.iteh.ai/samples/67965/52db83f8a3434b9790166c0b8a6b4001/ISO-3104-2020.pdf |
[14] | W. Wazer, J. W. Lyons, K. J. Kim et R. E. Kolwell; Viscosity and Flow Measurement, Laboratory handbook of Rheology, Inst. Publ. New York - Londres, 1963. |
[15] |
Sofrazer (2025). The Crucial Role of the Viscosity of Petroleum Product Residues, June 2025. Available at:
https://www.sofraser.com/fr/actualites/petrole-energie/le-role-de-la-viscosite-des-residus-de-produits-petroliers/ (accessed on 20/09/2025). |
APA Style
Berry, U., Motoula, S. M. E., Samba, R. E. J., Nkeletela, L. B., Poaty, E. M. (2025). Comparative Studies of the Physicochemical Properties of Super Fuels Sold in the City of Brazzaville. World Journal of Applied Chemistry, 10(4), 101-108. https://doi.org/10.11648/j.wjac.20251004.12
ACS Style
Berry, U.; Motoula, S. M. E.; Samba, R. E. J.; Nkeletela, L. B.; Poaty, E. M. Comparative Studies of the Physicochemical Properties of Super Fuels Sold in the City of Brazzaville. World J. Appl. Chem. 2025, 10(4), 101-108. doi: 10.11648/j.wjac.20251004.12
@article{10.11648/j.wjac.20251004.12, author = {Ulrich Berry and Smael Magloire Elombo Motoula and Rene Evrard Josue Samba and Laurette Brigelia Nkeletela and Ermelan Makaya Poaty}, title = {Comparative Studies of the Physicochemical Properties of Super Fuels Sold in the City of Brazzaville }, journal = {World Journal of Applied Chemistry}, volume = {10}, number = {4}, pages = {101-108}, doi = {10.11648/j.wjac.20251004.12}, url = {https://doi.org/10.11648/j.wjac.20251004.12}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.wjac.20251004.12}, abstract = {The oil industry is divided into two sectors: the upstream sector, which involves exploration and production, and the. The downstream sector of the oil industry, comprising refining and distribution, plays a key role in converting crude oil into economically valuable products. Oil refining involves a range of processes that transform crude oil into fuels (LPG, gasoline, diesel), combustibles (fuel oils), and specialty products (waxes, paraffins), all of which must meet regularly updated standards. These operations are conducted in refineries, which are classified as either simple (few units) or complex (many units, allowing for more efficient and diverse output). The refining process produces various fractions, including combustible gases (C1-C2), LPG, gasoline fractions (C5-C10), kerosene (C10-C13), gas oils (C13-C25), and heavier products (C20-C50) that undergo cracking to yield lighter products. This study focuses on evaluating the physicochemical properties of premium gasoline sold in Brazzaville, Republic of Congo. The analysis of multiple samples showed that fuel sold by private vendors is of lower quality than that sold at official service stations. Key parameters assessed include density, specific gravity, viscosity, and pH. }, year = {2025} }
TY - JOUR T1 - Comparative Studies of the Physicochemical Properties of Super Fuels Sold in the City of Brazzaville AU - Ulrich Berry AU - Smael Magloire Elombo Motoula AU - Rene Evrard Josue Samba AU - Laurette Brigelia Nkeletela AU - Ermelan Makaya Poaty Y1 - 2025/10/17 PY - 2025 N1 - https://doi.org/10.11648/j.wjac.20251004.12 DO - 10.11648/j.wjac.20251004.12 T2 - World Journal of Applied Chemistry JF - World Journal of Applied Chemistry JO - World Journal of Applied Chemistry SP - 101 EP - 108 PB - Science Publishing Group SN - 2637-5982 UR - https://doi.org/10.11648/j.wjac.20251004.12 AB - The oil industry is divided into two sectors: the upstream sector, which involves exploration and production, and the. The downstream sector of the oil industry, comprising refining and distribution, plays a key role in converting crude oil into economically valuable products. Oil refining involves a range of processes that transform crude oil into fuels (LPG, gasoline, diesel), combustibles (fuel oils), and specialty products (waxes, paraffins), all of which must meet regularly updated standards. These operations are conducted in refineries, which are classified as either simple (few units) or complex (many units, allowing for more efficient and diverse output). The refining process produces various fractions, including combustible gases (C1-C2), LPG, gasoline fractions (C5-C10), kerosene (C10-C13), gas oils (C13-C25), and heavier products (C20-C50) that undergo cracking to yield lighter products. This study focuses on evaluating the physicochemical properties of premium gasoline sold in Brazzaville, Republic of Congo. The analysis of multiple samples showed that fuel sold by private vendors is of lower quality than that sold at official service stations. Key parameters assessed include density, specific gravity, viscosity, and pH. VL - 10 IS - 4 ER -