Method of adsorbing and method of recovering fluorine-containing compound
a fluorine-containing compound and adsorption method technology, applied in the field of adsorption of c2c6 fluorine-containing compound, can solve the problems of high adsorption of csub> and cost, and achieve the effect of avoiding heat decomposition of fluorine-containing compound
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example 1
[0034]Into 500 cc glass bottle, each of active carbons (0.1 g) was charged and then 300 cc of aqueous solution containing 100 ppm of perfluorohexanoic acid (PFHA), which was adjusted to pH 2, was charged. The bottle was shaken at a temperature of 25° C. for 24 hours by a shaking apparatus, to adsorb perfluorohexanoic acid (PFHA) by the active carbon. Then, the equilibrium amount of adsorption was calculated. The concentrations of perfluorohexanoic acid (PFHA) in the raw water and the treated aqueous solution were compared, and the equilibrium adsorption amount of perfluorohexanoic acid (PFHA) per a unit weight of active carbon was determined. Adsorption rate of perfluorohexanoic acid (PFHA) to each active carbon is shown in Table 1.
[0035]The adsorption rate (%) is given by:
[[(Concentration of PFHA in initial raw water [ppm])−(Concentration of PFHA in treated water after adsorption [ppm])]×(Amount of raw water [g])] / [(Amount of used active carbon [g])×1,000,000]×100[%].
[0036]Accordin...
example 2
[0040]The same operation as in Example 1 was repeated except for using an ion-impregnated active carbon. The PFHA adsorption rates of the active carbons classified based on the impregnated ions are shown in Table 2.
[0041]
TABLE 2Impregnated IonAdsorption Rate [%]MgO I14.7MgO II14.6Amines16.0
example 3
[0042]An active carbon (0.1 g), to which PFHA was adsorbed until reaching the breakthrough point, was charged into an autoclave having an internal volume of 20 cc and backwashed with a steam having a temperature of 150° C. and a pressure of 0.5 MPa to 0.6 MPa for 10 minutes. The concentration of PFHA, which was adsorbed by the uptake tubes (two uptake tubes consisting of one uptake tube receiving 300 cc of water and another uptake tube receiving 300 cc of an aqueous solution of 0.1N sodium hydroxide), was determined. Then, the amount of desorption was calculated by multiplying the concentration of PFHA with the amount of the liquid. PFHA desorption effect by the steam from the active carbon is shown in Table 3.
[0043]
TABLE 3AdsorptionDesorptionTypes of ActiveAmountAmountDesorptionCarbon[g / AC-5 g][g / AC-5 g]Rate [%]Highly Activated1.321.2191.7Carbon 1Highly Activated1.171.1295.7Carbon 2Highly Activated1.030.9794.2Carbon 3Highly Activated0.930.9298.9Carbon 4General Carbon 10.390.3794.9G...
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