Iron nitrilotriacetic acid ([Fe(II)NTA]−) solution is able to absorb NO from flue gases. In this study, the kinetics of the gas–liquid reaction between NO and [Fe(II)NTA]− has been determined using a double stirred cell. The study indicates that the reaction between NO and [Fe(II)NTA]− is turned into gas film controlling as the [Fe(II)NTA]− concentration is over 0.03 mol L−1. The reaction rate between NO and [Fe(II)NTA]− is in proportion to the inlet nitric oxide concentration. 50°C is considered to be the best temperature for [Fe(II)NTA]− solution absorbing nitric oxide. The reaction rate between NO and [Fe(II)NTA]− decreases as pH drops below 5.5. The negative effect of pH may be reduced as the [Fe(II)NTA]− concentration increases. The reaction rate between NO and [Fe(II)NTA]− varies little in the pH range from 5.5 to 8.0. The kinetic equation for the gas–liquid reaction between NO and [Fe(II)NTA]− under the controlling of both liquid film and gas film has been obtained as follows:
The activation energy Ea for the gas–liquid reaction between NO and [Fe(II)NTA]− is 13.06 KJ/mol. stands for the rate of chemisorptions, mol/(m2 · s); for the NO concentration in the interface, mol L−1; and for [Fe(II)NTA]− concentration in the liquid, mol L−1.