The aim of the present work is to monitor dew point corrosion of crude and vacuum distillation column overhead section in a petroleum refinery. The material of construction of overhead line pipe was carbon steel. The state of art of crude unit process was introduced. The corrosion and associated hydrolyzing mechanisms were briefly described. The crude processing in a petroleum refinery was extremely dynamic and thus field monitoring attempts were made, which provides some useful information on structural integrity of column downstream equipments. The demulsifier, neutralizer, and corrosion inhibitor were mixed in crude unit at specific locations for corrosion prevention. Field monitoring includes evaluation of pH and chloride content of desalter extracted water and overhead condensed water, Base Sediment & Water (BS&W) and chloride content of as-received & desalted crude, and iron content of overhead condensed water. Furthermore, corrosion coupon was installed in overhead section to obtain the actual corrosion rate. All the field study was conducted for a specified period. The acidity, chloride concentration, and iron loss of condensed water confirmed that acidic corrosion was under control. The corrosion rate of the installed coupons confirmed that corrosion rate was within the specified limit. The results revealed in this paper intended for refinery operators and corrosion engineers involved in understanding of actual process parameters in prevention of overhead acidic corrosion.
K E Y W O R D Sacidic HCl, aqueous corrosion, crude oil refining, naphthenic acid corrosion, refinery overhead corrosion
| INTRODUCTION AND BACKGROUND INFORMATIONCorrosion always occurs in petroleum refining process especially in crude unit which process crude oil that constitutes different boiling point and molecular weight of long chain hydrocarbon. Major impurities in crude oil are chloride salts, sulfur compounds, and carbon-dioxide gases. [1][2][3] The chloride salts could be in form of 75% NaCl, 15% MgCl, and 10% CaCl approximately. Further crude contain various acidic components including organic acids (R[CH 2 ] n COOH, R is cyclopentane or cyclohexane, n > 12) and mineral acids (H 2 S, HCN, & CO 2 ) collectively referred as naphthenic acids, and measured in Total Acidic Number (TAN, mg KOH/g). The main types of corrosion occurs in crude unit of petroleum refinery are naphthenic acid corrosion (NAC), sulfidation, hydrochloric acid (HCl) corrosion, ammonium chloride (NH 4 Cl) corrosion, ammonium bi-sulfide (NH 4 HS) corrosion, polythonic acid stress corrosion cracking (PASCC) and oxidation corrosion (rust formation). 2,[4][5][6] The size and structure of naphthenic acid decides corrosion severity between 180 C and 400 C, which could be operating temperature of heat exchanger, heater tube outlets, transfer lines, distillation column especially at flash zones and reflux lines of crude processing unit. The presence of elemental sulfur, mercaptans (RSH),