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WE ,• s' <br /> argaratus at selrxted temperatures,the Henrv's Law Constants an,! direct t'asmeanecessary <br /> o! Hor%ii 6 law <br /> - 5olu6jlili�s constant•�s necessary for iticse sub- <br /> ovetall mass Iransler coefGcrents were stances because they may b:miscible <br /> ea.lculaled and the results interpreted Henry's law constants were measured with water and the conventional de,Gni- <br /> suct:essfully using the two•resistante ,Or a number of compounds,partin.larly tion of H as the ratio of vapor pressure to <br /> theory.The effects of solute molecular hydrocarbons and halogenated hyt.'ro- aqueous setubility is not applicable.A <br /> size and temperature wire adequately carbons in distilled water and in the simple test of the volatilization potential <br /> described and correlated using the presence of humic acid•fulvic acid and of a solute in water is 10 prepare a <br /> bentonite. A gas stripping Systerr. solution of the solute in water of <br /> solu'te's 5thmidt number, which con- method was used.and analysis was by concentration at about 10 mg/L distill <br /> ` tains information about the diffusivity. <br /> fluorescence or gas chromatography, half the water oft, and measure the <br /> The experimental system may be A number of solubility measurements <br /> concentration in the residue and in the <br /> suitable for screening new solutes !or were also made in the presence of co- distillate. if the concentration in the <br /> their volatilizaticn characteristics as a solutes such as lulvie acid using a distillate ii much higher than that of the <br /> functilin of concentration.temperature, genEV"or column system, and a cot- residue.than volatilization is likely to be <br /> i and presence of other compound: or relation was devatoped to calculate the an important environmental p.ahway, <br /> phases in the water that may influence effect of the-salubilization'•induced by <br /> r.: volatilization behavior. the dissolved organic matter.From the Valatiliratiort CaleuhlionS <br /> experiments conducted,it was concluded <br /> Wind Wave Tank Studies that at normal environmental concen- The repun concludes with a disc rssion <br /> stations of orginic matter there is <br /> A 6-m-long by 60-cm-deep wind unlikely to be sicnificant effect on solute of procedures for calculating environ- <br /> t wave lank wassonstructedandoperated <br /> solubility. and. therefore, on Henrys mental volatilization rates.including:he <br /> w r particularly at high wind speeds, to law constant. The e(Ject of the organic acquisition of physical and chemic.•1 <br /> determine the dependence of gas and material may bs 10 increase or decrease data.envitonmantal concentrations ono` <br /> liquid mass transfer coefficients an solubility, the estimation of mass transfer coeffi- + <br /> wind speed. Measurements of wind Anovel-relative votatitity"apparatus ciente as a function of environmental <br /> velocity profiles were also made to was developed that can be used to conditions and solute properties. acid <br /> measure Henry's law constants for the roles ofsedimentation and sorption- <br /> obtain friction velocities and surface <br /> substances shat have low Henry's law The carculation of concentration profiler. <br /> - roughnesses. The transfer rates of 1 i constants, i.e.,values close to that of _ of volatilizing solutes from rivers and <br /> organic solutes were measured at water. The system was tested with a lakes is discussed,including the use of <br /> various wind speeds. series of alcohols and ketunes.and the oxygen transfer data, (reaerA,-::-con- <br /> a tt was again found that the two- agreement with literature data was scants)for rivers as a means of <br /> resistance model adequately described satisfactory. It should be noted '.at • volatilization rates for othf:r Solute.. <br /> the mass transfer rates of the substances <br /> as inrluenced Sy Henry's law constant. <br /> The Schmidt number raised to an D.hlackar.W.Y.Shiu,A.Bobra,J.Billington E.Chau,A. Yeurr,C.Ng,and F. <br /> appropriate power was also found to Srato are with the University of Toronto, Toronto, Canada MSS fA4, <br /> be an appropriate determinant of <br /> S. W.lfarickhoffis the EPA Project Officer fseebelowl- <br /> ;'^ solute molecular size and temperature. The complete report.entitled••VulatilirationOforganic Pcllwantsfrom Warer,•' <br /> A number of correlaiions were developed 10rderNo.P882.23093°:Cost;518.00,subject to chan;_I will be available <br /> in which the mass transfer coefficients only from: <br /> were expressed as a function of friction National Technicallnformation Service <br /> " velocity (which can be related to the 52d5 Port Royal Road <br /> actual wind velocity) or to roughness- Springfield VA 22161 <br /> Reynold's Number (a dimensionless Telephone:703-487-4650 <br /> parameter indicative of the :urbulen, )he EPA Project Officer can be conracred at: <br /> ` conditions as the air-water :nterface). Envirortinentaf Research Laboratory <br /> Given the quality of existing zxperimen- U.S.j nvjranmental Protection Agency <br /> W data, the friction velociry alone may Athens,GA 30613 <br /> be an adequate descriptor of masa <br /> transfer coelficienL corrected by Schmidt <br /> Number for solute size,diffusivity and <br /> temperature.Anoutcome of this analysis us cvv:;.r.•cn7snW:.rc orr'c�tree_1SfafSr77w <br /> is the suggestion that mass transfer <br /> coefficients measured in the laboratory <br /> may be higher than those applying in <br /> the environment,because laboratory <br /> conditions tend to result in higher <br /> friction velocities at the sante wind <br /> velocity.This may help to explain some <br /> reported inconsistencies between vola- <br /> .• tilita•Raratescalvrlatedintheenviron- <br /> 6" mens and measured is the laboratory. <br /> 3 <br /> ra. <br />