11111 Corrosivity Studies of Well Completion Fluids Comprising ZnCl2/CaCl2 on N-80 Steel

Monday, March 14, 2011: 10:55 AM
Room 352 B (George R. Brown Convention Center)
Alireza Aghasadeghi*
Lloyd's Register EMEA

The pitting corrosion behavior of mixed zinc chloride and calcium chloride well completion fluids used in the high-pressure oil and gas industry were studied. These brines are associated with the problem of pitting type corrosion of tubular goods. The presence of high concentrations of chloride ions leads to severe pitting corrosion but low rates of general corrosion. 

 The corrosion behavior of API 5CT grade N80 in these solutions was investigated by means of weight loss coupons, DC polarization and AC-Impedance (EIS) electrochemical techniques.

 This study identified calcium chloride and zinc chloride mixture solutions with acceptable corrosivity that also satisfies the primary requirements for balancing well pressure and avoiding crystallization. 

 A tri-phase diagram based on ZnCl2, CaCl2 and water at 21 oC was developed to determine the correct fluid density with different concentrations of each component.  In addition, pH-related diagrams were developed based on different compositions of each component and their mixtures with different fluid densities. The corrosivity of fluid compositions with different density ranges from 1.20 kg/m3 (10 ppg[1]) to 1.80 kg/m3 (15 ppg) at different temperatures of 25, 60, 90 and120 oC, were investigated.

Surface observations and analysis were conducted by means of a Scanning Electron Microscope (SEM) to determine the pitting morphology on API N-80 steel surfaces.


[1] Pound Per Gallon