In this study, the removal of nitrate ions from aqueous solutions with liquid membrane technique has been investigated for different organic solvent types in which solubilized tetradecyl trimethyl ammonium bromide (TDTMABr) as carrier. n-butyl alcohol, chloroform, and mixture of chloroform + n-hexane (n-hexane 85% + chloroform 15%) were used as organic solvent. Kinetic parameters (k 1d , k 2m , k 2a , t max , R m max , J m max , J a max ) were calculated from obtained data. time R a values of mixture, butyl alcohol, and chloroform are 0.81, 0.78, and 0.55, respectively. Similarly R d , R m , and t max values of the mixture equal to 0.14, 0.04, and 87.92 min, respectively. This behavior of the system shows the organic solvent type is an effective parameter on separation yield. It can be concluded that the mixture is the most effective organic solvent type among the investigated ones, because liquid membrane systems should be operated within the range of having the R m , R d , and t max values are minimum while R a values are maximum.Keywords Liquid membrane AE Nitrate removal AE Organic solvent typeList of symbols C a nitrate ion concentration in acceptor phase (mol l À1 , M) C carrier carrier concentration (mol l À1 , M) C do nitrate concentration in the donor phase at t = 0 moment (mol l À1 , M) C m nitrate concentration in organic (membrane) phase (mol l À1 , M) D QNO 3 mean diffusion coefficient of the complex in the membrane of thickness l (m 2 s À1 ) J a max maximum value of membrane exit flux (min À1 ) J d max maximum value of membrane entrance flux (min À1 ) k 1 membrane entrance rate constant (min À1 ) k 2 membrane exit rate constant (min À1 ) k 1d membrane entrance or leak to membrane rate constant (min À1 ) k 2a acceptor phase entrance rate constant (min À1 ) k 2m membrane phase exit rate constant (min À1 ) K equilibrium constant (-) R reduced nitrate ion concentration (-) R a reduced nitrate ion concentration in acceptor phase (-) R d reduced nitrate ion concentration in donor phase (-) R m reduced nitrate ion concentration in membrane phase (-) R m max maximum reduced nitrate concentration of membrane phase (-) S d/m interface surface of donor and membrane phases (cm 2 ) S a/m interface surface of acceptor and membrane phases (cm 2 ) t time (min) t inf time corresponding to inflection point of the function (min) t imax time which nitrate concentration reaches maximum (min) l i distance between phases (cm)