1950
DOI: 10.1021/ie50492a036
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Solvents for Extracting Nicotine from Aqueous Solutions

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Cited by 10 publications
(5 citation statements)
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“…In the first step of extraction, toluene showed a 90% extraction efficiency of Nic, in agreement with literature reports. 35,50 Using the Hendersen-Haaselbach equation, the calculated dissociation factor of NicH + in the remaining solutions of 10% Nic and total NicH + was found to be <0.1%. Considering the initial conditions of nicotine in the sample set, re-equilibration between Nic and NicH + in the sample extract introduces negligible measurement error.…”
Section: Nicotine Quantification and Partitioning In E-liquidmentioning
confidence: 99%
“…In the first step of extraction, toluene showed a 90% extraction efficiency of Nic, in agreement with literature reports. 35,50 Using the Hendersen-Haaselbach equation, the calculated dissociation factor of NicH + in the remaining solutions of 10% Nic and total NicH + was found to be <0.1%. Considering the initial conditions of nicotine in the sample set, re-equilibration between Nic and NicH + in the sample extract introduces negligible measurement error.…”
Section: Nicotine Quantification and Partitioning In E-liquidmentioning
confidence: 99%
“…The solvent system, pH and temperature and time is a critical points in extraction efficiency of nicotine, chloroform -aqueous system have a good extraction ratio because the highest distribution coefficient between the two solvents, nicotine trend to dissolved in aqueous solvent whenever pH 3 or less and temp 25 or less than, vice versa nicotine dissolved in organic solvent at pH above 9 or higher and temp above 25 o C. The purity of nicotine rose from 16.43% to 99% after converting crude nicotine to its esters (nicotine bitartarate) 16 .…”
Section: Resultsmentioning
confidence: 99%
“…Those systems for which substantially complete ternary equilibria were obtained are listed in Table I. Additional distribution coefficients for various solute-solvent systems were determined as follows: acetic acid between water and ethyl acetate, butyl acetate, ethyl propionate, and ethyl butyrate (243); acetic and butyric acids between water and isophorone or o-cresol (224); penicillin between water and butyl acetate, ethyl acetate, and trichloroethylene as a function of pH (257); acetylacetone between benzene and water (210); acetic, citric, tartaric, and glycolic acids between water and tributyl phosphate as a function of temperature (188); a number of methyl-substituted pyridine» and quinolines between cyclohexane or chloroform and water or citrate-phosphate buffer (90); uranyl nitrate between water and ethyl, butyl, amyl, and isopropyl acetates, methyl ethyl and1 methyl isobutyl ketones, and n-butyl, isobutyl, and isoamyl alcohols and isobutyl methyl carbinol (129); iodine between carbon tetrachloride and aqueous potassium iodide (136); some 150 organic compounds of various types between water and isobutyli alcohol (46); and nicotine between water and a variety of solvents as a function of temperature (9). Equilibrium distribution measurements served as a means of studying other phenomena: the exchange of CN between Ni(CN)4…”
Section: Diffusion and Equilibriamentioning
confidence: 99%