Direct solventless supercritical fluid extraction of chlorbiphenyls from aqueous solutions at 0.1 × 10 -12 g/g level and whole extract analysis by GC/ECD

Glazkov, I. N.; Revelsky, I. A.; Efimov, I.P.; Zolotov, Yu. A.

doi:10.1007/s002160051498

Cited by 9 publications

(1 citation statement)

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“…The dechlorination reactor consists of a column of a zero-valent bimetallic mixture of palladium and iron (Pd 0 /Fe 0 ) that is heated to 450 uC. The extraction efficiency from either the contaminated soil or the resulting aqueous surfactant suspension is influenced by the solubility of PCBs in scCO 2 , 3 the concentration of PCBs in the aqueous phase, 4,5 the operating pressure and temperature 6,7 and the solvent modifier added to the scCO 2 . [8][9][10] For optimized reaction conditions, the dechlorination is very efficient; however, the time required for efficient scrubbing is anticipated to depend on the loading of PCBs within the soil/aqueous surfactant emulsion.…”

Section: Introductionmentioning

confidence: 99%

Extractions of polychlorinated biphenyl (PCB) compounds from surfactant suspension/soil extracts with dechlorination on-line

Marshall

2001

J. Environ. Monitor.

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Polychlorinated biphenyl (PCB) formulation (Aroclor 1242 or 1248)-surfactant (Brij 97 or Triton CF54) emulsions (0.1-1.0%, v/v) were extracted with supercritical carbon dioxide (scCO2). The declinations curve that resulted for each loading of PCB substrate was accurately modelled as a single-exponential decay, and the half-life [t1/2, 10.76 min +/- 2% (Brij 97) or 10.0 min +/- 14% (Triton CF54)] was independent of the level of loading. When the extraction was combined with on-line dechlorination, t1/2 was increased to 17.62 min +/- 6% or 16.46 min +/- 5%, respectively The dechlorination reactor contributed appreciably to the back-pressure of the system so that, under identical scCO2 head pressures, the flow rate at the exit of the system was reduced from 1500 mL min-1 (as decompressed gas) to 900 mL min-1. When corrected for the difference in flow rates, the declination curves in the absence and presence of the reactor became virtually identical. For a surfactant suspension from a soil that was field-burdened with only 6 ppm PCBs, extended operation (extraction-dechlorination) for 15 h, during which the substrate suspension was replaced every 30 min, caused no loss of the dechlorination efficiency; however, for 1% (v/v) Aroclor 1242 or 1248 in surfactant suspension, the reactor gradually lost reactivity over 5 h of continued operation. However, the reactivity could be restored virtually completely by purging the reactor column with scCO2 for 3 h or washing the column at ambient temperature with 30 mL of methanol-water (7 + 3, v/v). Mass spectrometry of the reaction products indicated that the principal products included biphenyl and toluene, but methylated benzenes and phenols were also present.

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