[Retracted] Corrosion Inhibition of Tubing Steel during Acidization of Oil and Gas Wells

Table 3

Thermodynamic parameter in absence and in presence of AAL and BAL.

Inhibitor	Δ𝐻^∗ (kJ/mol)	𝐸𝑎 (kJ/mol)	Δ𝐺ads (kJ/mol)	Δ𝑆^∗ (J/mol)
Blank	—	38.4	—	—
AAL	−62.1	57.6	−32.2	−32.5
BAL	−69.4	68.7	−36.7	−22.5