scholarly journals Total Acid Number Reduction of Naphthenic Acid Using Subcritical Methanol and 1-Butyl-3-Methylimidazolium Octylsulfate

2016 ◽  
Vol 148 ◽  
pp. 1074-1080 ◽  
Author(s):  
Faisal Zafar ◽  
Pradip Chandra Mandal ◽  
Ku Zilati bt Ku Shaari ◽  
Muhammad Moniruzzaman
2021 ◽  
Vol 1025 ◽  
pp. 337-342
Author(s):  
Noraini Safar Che Harun ◽  
Norshahidatul Akmar Mohd Shohaimi ◽  
Shaari Daud

The Naphthenic Acid (NA) found in the acidic crude oil is one of the main challenges that can lead to corrosion problem in oil refinery equipment and reduces the quality of the oil. In this study, catalytic neutralization reaction was investigated in order to lowering Total Acid Number (TAN) in crude oil to less than one mg KOH/g utilizing 2-Methylimidazole in Polyethylene Glycol (PEG) with aid of Ca/Al2O3 catalyst. The catalyst were supported on the alumina beads through Incipient Wetness Impregnation (IWI) methods and heated in an oven for 24 hours at 80-90°C then calcined at calcination temperatures of 800, 900 and 1000°C. The result showed that Ca/Al2O3 catalyst successfully reduced to 0.52 mg KOH/g from original TAN value 4.22 mg KOH/g by using a catalyst at calcination temperature 1000°C, 0.39 wt % (7 beads) of catalyst loading and 1000 ppm of 2-Methylimidazole in PEG. It can be concluded that catalytic deacidification method was effective method in reducing NAs from the crude oil and can lowered the TAN value to less than 1 mg KOH/g.


2021 ◽  
Author(s):  
Ahmed Almadhaji ◽  
Mohammed Saeed ◽  
Hitham Ibrahim ◽  
Anas Ahmed ◽  
Ragaei Maher

Abstract One of Sudanese fields has a heavy crude oil which has a high Total Acid Number (TAN) and high viscosity, can cause a lot of problems in production operation, transport, and storage facilities. The effect of ethanol dilution on the rheological properties of crude (especially the kinematic viscosity) was studied and presented. Moreover, the consequence of blending Trona (NaHCO3.Na2CO3) with a specified amount of Ethanol in the crude can reduce (TAN) to acceptable limits for solving corrosion and flowability problems. The approach is based on the experiments and laboratory works on the crude's samples after blending with a certain amount of Trona and Ethanol. It depends on the results of apparatuses, that are used to measure the samples, for instance, Calibrated glass capillary viscometer and ASTM D664 titration volume Total Acid Number tester which are employed to get the values of kinematic viscosity and TAN, respectively. The tests are established with crude have kinematic viscosity (187 cst) at temperature 75°C and TAN almost (8.51). While increasing the dosage of Trona at the ambient temperature (38°C) with the certain mass percentage of Ethanol (5%), TAN is decreased from (8.51 to 4.00 mgKOH/g). Also, the kinematic viscosity is declined from (187 cst to 96.75 cst) after increasing the volume of Ethanol at 75°C. These outcomes indicated that Ethanol could reduce Sudanese heavy crude's viscosity, and the Trona could decrease the TAN. This reduction occurred due to Ethanol dilution. The Ethanol molecules disturb the molecular structure of the crude, which forms polar bond within the hydrocarbon chain that leads to lower the friction between molecules of hydrocarbon in the crude. Also, Trona shrinks TAN because the Hydroxide ions (OH+) that founded in Trona neutralize the Hydrogen ions (H−) in Naphthenic acid in Sudanese heavy crude. This study can be summarized in the ability to solve the difficulty of transporting and processing the heavy crude oil in refineries; maintains the quality of the crude while utilizing it with friendly environmental materials and low cost.


2018 ◽  
Vol 32 (7) ◽  
pp. 7660-7669 ◽  
Author(s):  
René B. Madsen ◽  
Konstantinos Anastasakis ◽  
Patrick Biller ◽  
Marianne Glasius

Fuel ◽  
2021 ◽  
pp. 122522
Author(s):  
Hayane A. Fernandes ◽  
Luana N. Zanelato ◽  
Paulo A.P. Decote ◽  
Hélisson N. Santos ◽  
Caroline M. Senger ◽  
...  

ACS Omega ◽  
2020 ◽  
Vol 5 (32) ◽  
pp. 20311-20320
Author(s):  
Shuoxun Shen ◽  
Zhirong Wang ◽  
Juncheng Jiang ◽  
Xingyan Cao ◽  
Peipei Sun ◽  
...  

2018 ◽  
Vol 51 (3-4) ◽  
pp. 65-72 ◽  
Author(s):  
Artur Wolak

This article describes the processes of degradation of five engine oils belonging to the same SAE (Society of Automotive Engineers) viscosity class but launched by different manufacturers. The direction and intensity of changes in the total acid number have been analyzed. As part of the experiment, the changes in engine oils occurring during operation have been examined. The operating conditions throughout the test can be described as “severe,” that is, frequent starting of the engine, short distance driving, and extended engine idling. All engine oils were operated in passenger cars of a uniform fleet of 25 vehicles. The total acid number was determined in accordance with the ASTM D664. The obtained results have led to the development of a statistical model enabling to calculate average predictive values of the total acid number for a given mileage. The results may facilitate decision-making regarding the service life of engine oils.


2015 ◽  
Vol 1107 ◽  
pp. 79-84
Author(s):  
Norshahidatul Akmar Mohd Shohaimi ◽  
Jafariah Jaafar ◽  
Wan Azelee Wan Abu Bakar

Oil is one of the most important energy sources for the world and will likely remain so for many decades, even in the most optimistic projection about the growth of alternative energy sources. Petroleum industry nowadays faced a problem when the naphthenic acid (NA) compound naturally present in the acidic crude oil tends to induce corrosion in oil refining process. Total Acid Number (TAN) represent the amount of naphthenic acid in the oil with the permissible limit of TAN in crude oil is less than 1. Various methods had been used to remove NA in crude oil such as dilution and caustic washing. But all methods have their own weakness. Hence, in order to overcome the acidic crude oil problem, a new catalytic deacidification technique will be introduced in this study. Three types of crude: Petronas Penapisan Melaka Heavy Crude (Crude A) and Light Crude (Crude B) and Korean Crude (Crude C) were studied. Parameters studied were dosing amount of basic chemical used, catalyst calcination temperature, and percentage of the basic chemical in the co-solvent. The basic chemical used in this study was ammonia solution in ethylene glycol (NH3-EG). By using Ca/Al2O3 catalyst with calcination temperature of 10000C, the results showed 66.7% (1000 mg/L of NH3-EG) reduction in TAN for crude A, 53.9% reduction for crude B while for crude C the percentage of TAN reduction was 41% only. Addition of Cu as a dopant in this study had increased the TAN reduction for all three types of crude oil. TAN in crude A (80% of TAN reduction) and crude B (77% of TAN reduction) were successfully reduced to less than 1 with only using 1000 mg/L of NH3-EG with the aids of Cu/Ca (10:90)/Al2O3 catalyst at calcination temperature of 10000C while for crude C the TAN was still higher than 1 but the percentage of TAN reduction increased to 46%.


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