Official Journal of the College of Engineering, AlNoor University

Distinguish among the specific gravity of petroleum products (gasoline, kerosene, and gasoil, lubricating oils)

Document Type : Original Article

Author

Oil Production and Distribution Company (OPDC), Salhuldeen Branch, Tikrit, Iraq

10.69513/jnog.v2.i2.a5
Abstract
Abstract
Density, specific gravity, and the American Petroleum Institute (API) grade of petroleum products are considered in identification tests to express the product's identity and determine subsequent laboratory tests. This research aims to differentiate the specific gravity (Sp.gr), and American Petroleum Institute gravity (API) of gasoline, kerosene, gasoil, and lubricating oils, then what is different among them. This research dealt with four different oil products (gasoline, kerosene, gas oil, and lubricating oils) these samples were brought from Oil Products Distribution Company (OPDC), Salahuldeen Branch. Moreover, the results of the laboratory test showed that the specific gravity and American Petroleum Institute gravity of these samples were close to them. The results showed the specific gravity of gasoline ranges between 0.700 to 0.750, the specific gravity of kerosene ranges from 0.750 to 0.800, while Sp.gr of gasoil from 0.800 to 0.850, and lastly, the range of specific gravity of lubricating oils is from 0.850 to 0.900. In conclusion, this work will help the workers in the oil sector and engineering students who study in this field avoid mistakes in their work.

Keywords

Subjects

 

 

Al-Noor Journal for Oil and Gas Studies

 

https://jnog.alnoor.edu.iq/

 

 

 

Comparative among the specific gravity of petroleum products (gasoline, kerosene, and gasoil, lubricating oils)

 

                             

 

Ibrahim Abed Hasan 1   , Mahmod A. Abdulqader 1,2 *     , T.H. Al-Salim 2, Rawandooz A. Goran 2

 

1 Oil Products Distribution Company (OPDC), Salahuldeen Branch, Tikrit, Ministry of Oil, Iraq

 2 Department of Petroleum Engineering, College of Engineering, Alnoor University, Mosul, Iraq

 

 

 

 

 

Article information

 

Abstract

 

Article history:

Received 15 October, 2024

Revised 11 December, 2024

Accepted 11 April, 2025

 

 

   Density, specific gravity, and the American Petroleum Institute (API) grade of petroleum products are considered in identification tests to express the product's identity and determine subsequent laboratory tests. This research aims to differentiate the specific gravity (Sp.gr), and American Petroleum Institute gravity (API) of gasoline, kerosene, gasoil, and lubricating oils, then what is different among them. This research dealt with four different oil products (gasoline, kerosene, gas oil, and lubricating oils) these samples were brought from Oil Products Distribution Company (OPDC), Salahuldeen Branch, Tikrit, Ministry of Oil, Iraq . Moreover, the results of the laboratory test showed that the specific gravity and American Petroleum Institute gravity of these samples were close to them. The results showed the specific gravity of gasoline ranges between 0.700 to 0.750, the specific gravity of kerosene ranges from 0.750 to 0.800, while Sp.gr of gasoil from 0.800 to 0.850, and lastly, the range of specific gravity of lubricating oils  is from 0.850 to 0.900. In conclusion, this work will help the workers in the oil sector and engineering students who study in this field avoid mistakes in their work. will be presented and discussed as a road map for future research in the field.

 

Keywords:

Specific gravity, American Petroleum Institute,

Gasoline,

Kerosene,

Gasoil,

 Lubricating oil

 

Correspondence:

 

M A. Abdulqader

[email protected]

 

 

 

 

 

DOI:  https://doi.org/10.69513/jnog.v2.i2.a5 ©Authors, 2026, College of Engineering, Alnoor University.

This is an open-access article under the CC BY 4.0 license (http://creativecommons.org/licenses/by/4.0/).

 

           

 

 

1. Introduction

Specific gravity (Sp.gr) is a key physical property used to distinguish petroleum products by measuring their density relative to water [1]. Since petroleum is a complex mixture of hydrocarbons, its specific gravity is directly related to the mixture's molecular weight and size, which generally increase as the product becomes heavier and has a higher boiling point during crude oil distillation [2] [3]. This property is an important factor in quality control, in determining transport and storage methods, and in converting volumes to mass in commercial transactions [4]. In the same vein as specific gravity and distinguishing petroleum products, the products mentioned are derived from different stages of crude oil refining, resulting in a clear trend in their approximate specific gravity ranges (at standard conditions) [5].

The key distinction is gasoline has the lowest specific gravity (it is the "lightest") because it contains the smallest,

most volatile molecules [6]. The specific gravity (Sp.gr) increases sequentially from gasoline to kerosene to gasoil, as the average molecular size and boiling point increase [7]. Lubricating oils have the highest specific gravity (the "heaviest") and are highly viscous because they contain the largest, least-volatile hydrocarbon molecules [8]. The Role of American Petroleum Institute (API) Gravity: in the petroleum industry, it is often used instead of specific gravity (Sp.gr) [9]. It is an inverse measure of Sp.gr [10]. A higher Sp. gr means a lower API gravity (heavier product) [11]. A lower me Sp. gr and a higher API gravity (lighter product) [12]. Therefore, the trend in API gravity for these products is the opposite of that for SP. gr trend; take, for instance, gasoline has the highest API gravity, and lubricating oils have the lowest API gravity [13].

The challenge in this study was the convergence of laboratory test results for specific gravity (Sp.gr). For example, the specific gravity of gasoline is between 0.700 and 0.750, while kerosene is between 0.750 and 0.800. This indicates that 0.750 is the maximum value for gasoline, while the same value is the minimum value for kerosene. On the other hand, 0.850 is the maximum value for kerosene products, the same as the minimum value for gas oil, and the same applies to lubricating oils and gas oil products. However, this research focused on the specific gravity (Sp. gr.) of gasoline, kerosene, gas oil, and lubricating oils, and on what differentiates them. Then to distinguish among these products via specific gravity.

2. Materials and methods

2.1Fuel samples

Eight samples of oil products, obtained from the Oil Products Distribution Company (OPDC), Salahuldeen Branch Laboratory, Tikrit, Ministry of Oil, were used in this study. These samples include two samples of gasoline, two of kerosene, two of gas oil, and two of lubricating oil, sent to the Al-Noor University College of Engineering, Department of Petroleum Engineering laboratory, for the porosity study. The tests of these samples were Sp. gr , temperature, and American Petroleum Institute (API) calculated as in equation 1 [14]. Figure 1 shows four types of fuel, which are (gasoline, kerosene, gas oil, and lubricating oil).

 

 

 

 

 Figure 1: Four types of fuel: gasoline, kerosene, gas oil, and lubricating oil

2.2 Procedures

The specific gravity (Sp.gr) was determined according to ASTM D1298 [15], while the American Petroleum Institute (API) gravity was found according to ASTM D5002 [14], calculated using Equation 1 [16]. This study was conducted in the laboratories of the Petroleum Engineering Department, College of Engineering, Al-Noor University, Nineveh Governorate, Iraq. Figure 2 shows the specific gravity test and the apparatus.

API=141.5/(Sp.gr)-131.5

(1)

 

    Figure2: The Sp.gr test of gasoline, kerosene, gas oil, and lubricating oils

 

1. Results and discussions

3.1Specific gravity of gasoline fuel

        Table 1 presents the results for specific gravity, API gravity, and temperature of gasoline samples, as shown in Figure 3. The results for specific gravity were 0.730 and 0.77

 whereas the API gravity results were 62.33 and 52.27 for gasoline samples 1 and 2, respectively [17]. Compared with the standard tests, Sp.gr ranged from 0.700 to 0.750, while API gravity ranged from 57.2 to 75.6. The results showed that the temperature of the gasoline samples was the lowest compared to kerosene, gas oil, and lubricating oil, reaching 22 °C. These results are attributed to the presence of light volatile aromatic compounds that contribute to the composition of gasoline products [18]. Therefore, these results will strengthen the basic components of the final Table of this research [19]. The gasoline fuel was lightest (lowest boiling point). Contains the shortest hydrocarbon chains (C4 to C12), which are used as car gasoline fuel [20].

 

 

 

 

 

 

 

 

 

Table 1: The results of specific gravity, API gravity, and temperature

Sample name

Sp. gr

API

Temperature °C

Gasoline-1

0.730

62.33

22

Gasoline-2

0.770

52.27

 

 

 

 

 

 

 

 

 

 

 

 

22

                                                                                                         

 

Figure 3: Gasoline fuel sample and samples and the specific gravity test

 

3.2. Specific gravity of kerosene fuel

    Table 2 presents the data on the Sp. gr, API gravity, and temperature for gasoline samples as shown in Figure 4. The range of the specific gravity (Sp. gr.) was 0.765-0.780, and the API was 53.50 and 50.00 for kerosene samples 1 and 2, respectively [21]. Compared to the standard tests, the Sp.gr ranged from 0.750 to 0.800, while the API gravity ranged from 57.2 to 45.4. As a result, the Sp.gr were. The results showed that the kerosene product had an average temperature of 23 °C, compared to gasoline and gasoil. This is due to the mixture used to make kerosene. These findings are due to the existence of light volatile aromatic molecules, which contribute to the composition of gasoline products. Therefore, these data will help reinforce the outcomes that are the basic components of this research's final Table [22]. Intermediate weight, boiling point. Longer chains than gasoline (C10 to C16), which used as fuel for home heating [23].

Table 2: Sp.gr, API, and temperature results of kerosene fuel samples

 

Sample name

Sp. gr

API

Temperature °C

Kerosene-1

0.765

53.50

23

Kerosene-2

0.780

50.00

23

 

 

 

Figure 4: Kerosene fuel sample and specific gravity (Sp.gr) test

3.3. Specific gravity of gasoil fuel

       Table 3 presents the results for specific gravity, API gravity, and temperature of the gasoline samples, as shown in Figure 5. The specific gravity was 0.765 and 0.780, and the API gravity was 53.50 and 50.00 for kerosene samples 1 and 2, respectively. The standard tests for specific gravity range from 0.750 to 0.800, while the API gravity range is from 57.2 to 45.4. The results showed that the temperatures of the gas oil product were reasonable compared to other products, which reached 24 °C [24]. This is attributed to the gas oil, which is a mixture of linear organic hydrocarbon compounds extending up to C30. These results are attributed to the presence of light, volatile aromatic compounds that contributed to the gasoline product's composition. Therefore, these results will help strengthen the results of the Sp.gr test [25]. Heavier than kerosene (higher boiling point) longer hydrocarbon chains (C10 to C28), which are used as a diesel fuel [26].

 

Table 3: The results of the specific gravity (Sp..), API gravity,  and temperature of the gasoil samples of gasoil samples  

 

Sample name

Sp. gr

API

Temperature °C

Gasoil-1

0.810

42.10

24

Gasoil-2

0.820

36.00

24

 

 

 

Figure 5: Gasoil fuel sample and Sp.gr test

3.4. Specific gravity of lubricating oil

     Table 4 presents the specific gravity (Sp. gr.), API gravity, and temperature of the lubricating samples, as shown in Figure 6. The range of Sp. gr. ranged from 0.879 to 0.89, while the API gravity ranged from 35.00 to 25.70 for samples 1 and 2, respectively. For lubricating oil, the standard specific gravity range is 0.850 to 0.900, whereas the API gravity range is 35.00 to 25.700 [27]. The results showed that the lubricating oil products had higher temperatures than other products, reaching 26 °C [28]. These results are attributed to the presence of light volatile aromatic compounds that contribute to the composition of the gasoline product [29]. Therefore, these results will strengthen the basic components of the final Table of this research [30]. Heaviest (highest boiling point/viscosity). Compounds are composed of very long and complex hydrocarbon chains (C22 to C70), which are used as lubricating oil in a car engine [31].

 

Table 4: The specific gravity, temperature, and API gravity results

 

Sample name

Sp. gr

API

Temperature °C

Lubricating-1

0.879

29.50

26

Lubricating-2

0.890

27.50

26

 

 

Figure 6: Lubricating oil sample and specific gravity (Sp.gr) test

 

3.5. Comparative specific gravity

     Table 5 presents data on the ranges of specific gravity (Sp.gr) and API gravity for fuels and oil products (standard tests). As a result, the results for gasoline, kerosene, gas oil, and lubricating oil detailed in Tables 1, 2, 3, and 4, respectively, agreed with the standard results [32]. This finding means the specific gravity (Sp.gr) and API gravity were found to be the same in the range of specific gravity (Sp.gr) and API gravity of fuel and oil samples [33]. The gasoline had the lowest specific gravity (Sp.gr.), ranging from 0.700 to 0.750 (lowest boiling point) [34]. Contains the shortest hydrocarbon chains (C4 to C12), which are used as a car’s gasoline fuel [35]. While kerosene fuel is intermediate in weight, its boiling point and specific gravity range from 0.750 to 0.800, and it has longer chains than gasoline (C10 to C16), which is used as fuel for home heating. Although gasoil fuel was heavier than kerosene (higher boiling point), and has longer hydrocarbon chains (C10 to C28) are used as diesel fuel. Whereas regarding lubricating oil composed of very long and complex hydrocarbon chains (C22 to C70), which is used as lubricating oil in car engine [36].

 

Table 5: The standard tests of specific gravity and API gravity for the petroleum products (gasoline, kerosene, gasoil, and lubricating oil)

 

Sample

Sp.gr

API gravity

min

max

min

max

Gasoline

0.700

0.750

75.6

57.2

Kerosene

0.750

0.800

57.2

45.4

Gasoil

0.800

0.850

45.4

35.0

Lubricating oil

0.850

0.900

35.0

25.7

 


4.Conclusions

This study successfully verified the specifications of petroleum products (gasoline, kerosene, diesel oil, and

lubricating oils). The study showed that the density of gasoline is close to that of heavy naphtha. Therefore, it was necessary to verify the specifications of heavy naphtha to differentiate it from gasoline. The temperatures of (gasoli(gasoline, kerosene, gas oil, and lubricating oils) were 22, 23, 24, and 26 °C respectively. The results showed that the specifications of the petroleum products were rapprochement, but they were distinguished by specific gravity (Sp.gr). Furthermore, this study will provide sufficient information on fuel specifications and facilitate scientific research.

5.Acknowledgment

The authors would like to Oil Products Distribution Company (OPDC). Special thanks to Mr. Nazzal Younus Ramadhan, Head of Salahuldeen Branch (OPDC). They wish to extend a particular expression of Alnoor university, for his helpful support and co-operation during the conduct of this research.

 

 

References

 [1]Khaleel S I,  Ahmad A A, Islam K S, Muneef M M, Ali M S, Ibrahim A M, Omar A H, Mahmod A. A. Discussion of the Parameters Affecting the Boiling Point in the Distillation Test of the Kerosene Product. AUIQ Complement. Biol. Syst. 2026;3(1): 77–83, 2026. DOI: https://doi.org/10.70176/3007-973X.1058

[2]Khalaf  N I, Mohammed Q G, Qays A A, Gasheen I B. Conversion of Algal Biomass via Pyrolysis process into PYRO-CHAR Production at Wastewater Treatment NRC BAIJI.  J Chem. Technol. Metall. 2026; 61(2):249–57.DOI:10.59957/jctm.v61.i2.2026.6

[3]Ahmed A,   Mohamed A A,  Awad E M, Abdullah I I. The effect of physical properties of lost petroleum quantities in vertical tanks at (NRC) Baiji,” Energy Explor. Exploit., p. 01445987231220961, 2023. DOI:10.1177/01445987231220961

[4]Abdulqader M A, “Pre-calculated API Gravity Tables as an Alternative to the Standard Equation,” Al-Noor J Oil Gas Stud. 2026; 2(1):1–5..

[5]Humadi J I, Aabid A A, Mohammed A E, Ahmed G S and Abdulqader MA. New Design of Eco-Friendly Catalytic Electro-Photo Desulfurization process for Real Diesel Fuel.  Chem Eng Res Des. 2024;206 (4):DOI:10.1016/j.cherd.2024.05.001

[6]Jassam G,  Abdulqader MA and  Habeeb O. Additives of Base and Acid to Oxidative Desulphurization Process of Al-Sumoud Refinery at NRC Baiji,” Al-Noor J. Oil Gas Stud. 2026; 2(1,):7–12.

[7]Gubari M Q,  Radha M A,  Ahmed ZMA,  Abdulqader M A and Habeeb O A. “Energy Exploration and Recovery via Microwave Processing of Waste Spent Tea into Micro-Fuel Production. Int J Heat Technol.2025;43(2): 671-678.DOI:

https://doi.org/10.18280/ijht.430227

[8]Abdulqader M A. Awad E M,Sfoog S, Hamid M S Al-Jubouri. Total Remediation of NRC Oily Sludge Using Hydrothermal Carbonization for Hydro char Production,” in 2023 International Conference on Engineering, Science and Advanced Technology (ICESAT), IEEE, 2023, pp:230–235.

[9]Hameed A I, Abdulqader M A,  Habeeb O A, and  Saber S E. A Comparative Study of Specifications Products among Different Refineries at North Refineries Company NRC Baiji. J Pet Min.2026;2(1):54-62.

[10]Gubari  M Q,  Galawesh N T, Bayan H. Al-Jaleel, Aya A S, Ozdan A G,| Gasheen I B, Mahmod A. A. Comparative Performance of NF90 and NF270 Nanofiltration Membranes in Direct Dye Removal from Aqueous Solutions. Int  J  Heat Technol.  2025;43(4): 1449-1460.DOI:10.18280/ijht.430422

[11]Abbas M H,  Mhaimed M A,  Abdulqader M A,  Habeeb O A.The Impact of Different SMAW Electrodes on Trainee Skills Using Virtual Welding Machines at Baiji Oil Training Institute. J Pet Res Stud.2025;15(2):96–105.DOI: https://doi. org/ 10. 52716/jprs.v15i2.956

[12]Saleh A M, Mahmod A. Abdulqader, Hadi H M, Jafar K, Omar K Aty, Khalil FY,Azil B bin Alias, Omar A H, Ibrahim A M. Waste-to-Energy Innovations and Advances in Hydrothermal Carbonization, Microwave, and Pyrolysis Processes: A Review,” AUIQ Complement. Biol  Syst. 2026;3(1): 84–99, 2026.DOI: https://doi.org /10. 70176/3007-973X.1059

[13]Humadi J I,  Mohammed A E,  Khamees L A,  Jafar S A and  Abdulqader M A. Oil upgrading via desulfurization process using a new composite nano-alkaline-iron oxide over titanium oxide catalysts,” Energy Environ. 2025; p. 0958305X251344235 .doi.org/10.1177/0958305X2513442

[14]Lord D L,  Hogge J W and  Allen R G. Fuels Characterization for National Research Council Canada 2-m Pool Fire Test Series,” Sandia National Lab.(SNL-NM), Albuquerque, NM (United States), 2021.

[15]Fidyayuningrum H,  Fatoni R and  Harismah K. Characteristics of Cetane index of traditional diesel oil in Wonocolo district, Bojonegoro. AIP Conference Proceedings, AIP Publishing, 2020.

[16]Silva  A P, Juliana O B, Renato S, Leonardo R, William S F, Hiram M, Jeffrey L andVíktor O. Naphtha characterization (PIONA, density, distillation curve and sulfur content): An origin comparison. Energies. 2023;16(8):3568.  https:// doi. org/ 10.3390/en16083568

[17]Abdulqader M A. Thermochemical Conversion of Oily Sludge, Composition, Hazards, and Treatment Strategies: An Overview. AUIQ Complement Biol Syst.2025;2(2):10–36.DOI:10.70176/3007-973X1031

[18]Humadi J. Conversion of Spent Tea Waste for Solid Carbon Fuel via Hydrothermal Carbonization Process. J  Chem Pet Eng. 2025.

[19]Abdellatief  T M M,  Tamer M M,  Ahmad Mustafa. A unifying methodology for gasoline-grade biofuel from several renewable and sustainable gasoline additives,” Process Saf Environ Prot. 2024; 190:1386–1402.DOI:10.1016/j.psep.2024.07.112

[20]Fabbri  F, Ilaria V, Silvia D, Luca N, Valeria M R, Lisa M , Georg M G, Martina L,  Alessandro P. Mycobacterium smegmatis acyltransferase catalyzes the synthesis of esters and polyesters. RSC Sustain. 2024;2(5):1372–1377, 20. https://doi.org/ 10. 1039/ d4su00038b

[21]Hameed E A, Salih R A, Saleh A M, Issa H M and Abdulqader M A.The Effect of Chemical Coagulant Dosages on the Removal of Turbidity from Wastewater. AUIQ Complement Biol Syst. 2024;1(1):6.DOI:10.70176/3007-973X.1006

[22]Abdulkhader S I and  Barzanjy M J. Upgrading the environmental properties of Kirkuk kerosene using glacial acetic acid,” 3c Empres. Investig. y Pensam. crítico,2023;12(1):382–390.https://doi.org/10. 17993 /3cemp. 2023.120151.382-390

[23]Wanget H, Xiaokang Z, Xiuwei L, Li C.Effects of comb-like poly-α-olefins on the cold flow properties of diesel fuel. Fuel. 2024;356:129562. DOI:10.1016/ j.fuel.2023.129562

[24]Abdulqader M A.Water finding paste and phase finding paste of gasoline fuel: performance comparative study. Al-Noor J. Oil Gas Stud. 2026; 2(1):13–16. 

[25]Abdqadir M A. Evaluation of the Impact of Density on Selected Quality Control Tests of Petroleum Products at North Refineries Company (NRC), Baiji: oil and gas,  J Pet Min. 2026;2(2).

[26]Parsa M and Nazeri S. Enhanced biodegradation of n-alkanes in crude oil by immobilized Methylorubrum populi: Enzymatic roles of Alkane monooxygenase, Cytochrome p450, and Lipase. Biochem Eng J. 2025; 226:109977. DOI:10.1016/j. bej.2025.109977

[27]Abdulqader M A,  Salih H Y, Habeeb O A,  Saber S E M and  Jasem A A. Clean char solid carbon fuel production via microwave processes of oily sludge produced at North Refineries Company Baiji,” in AIP Conference Proceedings, AIP Publishing, 2023.

[28]Alias A B, Ali S, Thaer S, Obed M. Enhancing Flue Gas Cleaning with Modified Activated Carbon Surfaces: A Review Paper. 2025.19(2):66 DOI:10.15866 /ireme.v19i2.24987.

[29]Hamed H, Mohammed A,  Habeeb O,  Ali O,  Aljaf O and  Abdulqader M. Biodiesel Production From Waste Cooking Oil using Homogeneous Catalyst. Egypt J Chem.2021;0(0):0–0. doi: 10.21608 /ejchem. 2021.62395.3339.

 

 

 

 

 

التمييز بين الكثافة النوعية للمنتجات النفطية (الكازولين، والكيروسين، وزيت الغاز، وزيوت التزييت)

 

إبراهيم عبد حسن 1، محمود عبدالكريم عبد القادر 1،2 *، طه حسين السالم 2، رواندوز عبدالرزاق  كوران 2

شركة توزيع المنتجات النفطية، الهيئة الغربية، فرع صلاح الدين، تكريت، العراق، 2 قسم هندسة النفط، كلية الهندسة، جامعة النور، الموصل، العراق

 

الخلاصة

تعتبر الكثافة والوزن النوعي ودرجة معهد البترول الامريكي للمنتجات النفطية هي فحص تعريفي لتعبر عن هوية المنتوج وتحديد الفحوصات المختبرية اللاحقة.

يهدف هذا البحث إلى تحديد الفرق بين الكثافة النوعية وكثافة معهد البترول الأمريكي للمنتجات النفطية التي هي للبنزين والكيروسين وزيت الغاز وزيوت التشحيم،

وبيان الاختلاف بينهما من حيث الكثافة. علاوة على ذلك فقد تناول هذا البحث أربعة منتجات نفطية مختلفة التي هي (الكازولين، والكيروسين، وزيت الغاز، وزيوت

التشحيم) تم جلبها من مختبرات شركة توزيع المنتجات النفطية الهيئة الغربية فرع صلاح الدين. وأظهرت نتائج الفحوصات المختبرية تقاربًا في الكثافة النوعية لتلك

المنتجات. وبالتالي فقد تراوحت الكثافة النوعية للكازولين بين 0.700 و0.750، وللكيروسين بين 0.750 و0.800، ولزيت الغاز بين 0.800 و0.850، أما زيوت

التزييت فتراوحت بين 0.850 و0.900. ختاما فان هذا العمل سوف يُسهم  في سهولة الوصول الى الكثافة من قبل العاملين في قطاع النفط والطلاب المتخصصين في

هذا المجال وبذلك سوف يسهم في تجنب الأخطاء في العمل من خلال تمييز المنتجات النفطية في الكثافة.

 

 

 [1]Khaleel S I,  Ahmad A A, Islam K S, Muneef M M, Ali M S, Ibrahim A M, Omar A H, Mahmod A. A. Discussion of the Parameters Affecting the Boiling Point in the Distillation Test of the Kerosene Product. AUIQ Complement. Biol. Syst. 2026;3(1): 77–83, 2026. DOI: https://doi.org/10.70176/3007-973X.1058
[2]Khalaf  N I, Mohammed Q G, Qays A A, Gasheen I B. Conversion of Algal Biomass via Pyrolysis process into PYRO-CHAR Production at Wastewater Treatment NRC BAIJI.  J Chem. Technol. Metall. 2026; 61(2):249–57.DOI:10.59957/jctm.v61.i2.2026.6
[3]Ahmed A,   Mohamed A A,  Awad E M, Abdullah I I. The effect of physical properties of lost petroleum quantities in vertical tanks at (NRC) Baiji,” Energy Explor. Exploit., p. 01445987231220961, 2023. DOI:10.1177/01445987231220961
[4]Abdulqader M A, “Pre-calculated API Gravity Tables as an Alternative to the Standard Equation,” Al-Noor J Oil Gas Stud. 2026; 2(1):1–5..
[5]Humadi J I, Aabid A A, Mohammed A E, Ahmed G S and Abdulqader MA. New Design of Eco-Friendly Catalytic Electro-Photo Desulfurization process for Real Diesel Fuel.  Chem Eng Res Des. 2024;206 (4):DOI:10.1016/j.cherd.2024.05.001
[6]Jassam G,  Abdulqader MA and  Habeeb O. Additives of Base and Acid to Oxidative Desulphurization Process of Al-Sumoud Refinery at NRC Baiji,” Al-Noor J. Oil Gas Stud. 2026; 2(1,):7–12.
[7]Gubari M Q,  Radha M A,  Ahmed ZMA,  Abdulqader M A and Habeeb O A. “Energy Exploration and Recovery via Microwave Processing of Waste Spent Tea into Micro-Fuel Production. Int J Heat Technol.2025;43(2): 671-678.DOI:
https://doi.org/10.18280/ijht.430227
[8]Abdulqader M A. Awad E M,Sfoog S, Hamid M S Al-Jubouri. Total Remediation of NRC Oily Sludge Using Hydrothermal Carbonization for Hydro char Production,” in 2023 International Conference on Engineering, Science and Advanced Technology (ICESAT), IEEE, 2023, pp:230–235.
[9]Hameed A I, Abdulqader M A,  Habeeb O A, and  Saber S E. A Comparative Study of Specifications Products among Different Refineries at North Refineries Company NRC Baiji. J Pet Min.2026;2(1):54-62.
[10]Gubari  M Q,  Galawesh N T, Bayan H. Al-Jaleel, Aya A S, Ozdan A G,| Gasheen I B, Mahmod A. A. Comparative Performance of NF90 and NF270 Nanofiltration Membranes in Direct Dye Removal from Aqueous Solutions. Int  J  Heat Technol.  2025;43(4): 1449-1460.DOI:10.18280/ijht.430422
[11]Abbas M H,  Mhaimed M A,  Abdulqader M A,  Habeeb O A.The Impact of Different SMAW Electrodes on Trainee Skills Using Virtual Welding Machines at Baiji Oil Training Institute. J Pet Res Stud.2025;15(2):96–105.DOI: https://doi. org/ 10. 52716/jprs.v15i2.956
[12]Saleh A M, Mahmod A. Abdulqader, Hadi H M, Jafar K, Omar K Aty, Khalil FY,Azil B bin Alias, Omar A H, Ibrahim A M. Waste-to-Energy Innovations and Advances in Hydrothermal Carbonization, Microwave, and Pyrolysis Processes: A Review,” AUIQ Complement. Biol  Syst. 2026;3(1): 84–99, 2026.DOI: https://doi.org /10. 70176/3007-973X.1059
[13]Humadi J I,  Mohammed A E,  Khamees L A,  Jafar S A and  Abdulqader M A. Oil upgrading via desulfurization process using a new composite nano-alkaline-iron oxide over titanium oxide catalysts,” Energy Environ. 2025; p. 0958305X251344235 .doi.org/10.1177/0958305X2513442
[14]Lord D L,  Hogge J W and  Allen R G. Fuels Characterization for National Research Council Canada 2-m Pool Fire Test Series,” Sandia National Lab.(SNL-NM), Albuquerque, NM (United States), 2021.
[15]Fidyayuningrum H,  Fatoni R and  Harismah K. Characteristics of Cetane index of traditional diesel oil in Wonocolo district, Bojonegoro. AIP Conference Proceedings, AIP Publishing, 2020.
[16]Silva  A P, Juliana O B, Renato S, Leonardo R, William S F, Hiram M, Jeffrey L andVíktor O. Naphtha characterization (PIONA, density, distillation curve and sulfur content): An origin comparison. Energies. 2023;16(8):3568.  https:// doi. org/ 10.3390/en16083568
[17]Abdulqader M A. Thermochemical Conversion of Oily Sludge, Composition, Hazards, and Treatment Strategies: An Overview. AUIQ Complement Biol Syst.2025;2(2):10–36.DOI:10.70176/3007-973X1031
[18]Humadi J. Conversion of Spent Tea Waste for Solid Carbon Fuel via Hydrothermal Carbonization Process. J  Chem Pet Eng. 2025.
[19]Abdellatief  T M M,  Tamer M M,  Ahmad Mustafa. A unifying methodology for gasoline-grade biofuel from several renewable and sustainable gasoline additives,” Process Saf Environ Prot. 2024; 190:1386–1402.DOI:10.1016/j.psep.2024.07.112
[20]Fabbri  F, Ilaria V, Silvia D, Luca N, Valeria M R, Lisa M , Georg M G, Martina L,  Alessandro P. Mycobacterium smegmatis acyltransferase catalyzes the synthesis of esters and polyesters. RSC Sustain. 2024;2(5):1372–1377, 20. https://doi.org/ 10. 1039/ d4su00038b
[21]Hameed E A, Salih R A, Saleh A M, Issa H M and Abdulqader M A.The Effect of Chemical Coagulant Dosages on the Removal of Turbidity from Wastewater. AUIQ Complement Biol Syst. 2024;1(1):6.DOI:10.70176/3007-973X.1006
[22]Abdulkhader S I and  Barzanjy M J. Upgrading the environmental properties of Kirkuk kerosene using glacial acetic acid,” 3c Empres. Investig. y Pensam. crítico,2023;12(1):382–390.https://doi.org/10. 17993 /3cemp. 2023.120151.382-390
[23]Wanget H, Xiaokang Z, Xiuwei L, Li C.Effects of comb-like poly-α-olefins on the cold flow properties of diesel fuel. Fuel. 2024;356:129562. DOI:10.1016/ j.fuel.2023.129562
[24]Abdulqader M A.Water finding paste and phase finding paste of gasoline fuel: performance comparative study. Al-Noor J. Oil Gas Stud. 2026; 2(1):13–16. 
[25]Abdqadir M A. Evaluation of the Impact of Density on Selected Quality Control Tests of Petroleum Products at North Refineries Company (NRC), Baiji: oil and gas,  J Pet Min. 2026;2(2).
[26]Parsa M and Nazeri S. Enhanced biodegradation of n-alkanes in crude oil by immobilized Methylorubrum populi: Enzymatic roles of Alkane monooxygenase, Cytochrome p450, and Lipase. Biochem Eng J. 2025; 226:109977. DOI:10.1016/j. bej.2025.109977
[27]Abdulqader M A,  Salih H Y, Habeeb O A,  Saber S E M and  Jasem A A. Clean char solid carbon fuel production via microwave processes of oily sludge produced at North Refineries Company Baiji,” in AIP Conference Proceedings, AIP Publishing, 2023.
[28]Alias A B, Ali S, Thaer S, Obed M. Enhancing Flue Gas Cleaning with Modified Activated Carbon Surfaces: A Review Paper. 2025.19(2):66 DOI:10.15866 /ireme.v19i2.24987.
[29]Hamed H, Mohammed A,  Habeeb O,  Ali O,  Aljaf O and  Abdulqader M. Biodiesel Production From Waste Cooking Oil using Homogeneous Catalyst. Egypt J Chem.2021;0(0):0–0. doi: 10.21608 /ejchem. 2021.62395.3339.
 
 
 
 
Volume 2, Issue 2
Summer 2026
Pages 73-78

  • Receive Date 25 November 2025
  • Revise Date 19 July 2026
  • Accept Date 02 August 2026
  • Publish Date 01 September 2026