Effect of process conditions on the analysis of free and conjugated estrogen hormones by solid-phase extraction-gas chromatography/mass spectrometry (SPE-GC/MS).

Simultaneous analysis of 11 free estrogen hormones and five conjugated estrogens in water and municipal wastewater was studied. The analytical method was developed and tested for different types of solid-phase extraction adsorbents, eluents, sample containers and storage conditions, derivatization, and matrix effects. Varian Bond Elut C-18 solid-phase extraction adsorbent cartridge was selected based on its high recoveries for both free and conjugated estrogens. Sample storage conditions, as well as selection and pretreatment of sample container materials, can affect the trace level analysis of estrogens. Silanization of glassware is observed to provide low relative standard deviation (RSD) in the analysis and less percentage loss due to contacting with sample container materials. Light exposure during the test can significantly impact the results. The derivatized samples stored at -20°C for at least 6 days showed less than 10.5% average RSD in the analysis. The recovery efficiency in clean water varies from 72% to 101% for free estrogens and 78% to 82% for conjugated estrogens. The method detection limits (MDL) for most of the compounds range from 30 to 870 ng/L using a sample volume of 200 mL. With a sample volume of 3 L, the most sensitive compound produces a MDL of 0.03 ng/L. Dilute methanol is used to wash the loaded cartridge as a cleanup step in order to remove interfering species during analysis of wastewater samples. Using the optimized analytical methods, the concentration level of free estrogens in the influent and effluent municipal wastewaters is tested.

Influence of alkalinity and salinity on the sonochemical degradation of estrogen hormones in aqueous solution.

Ultrasound assisted degradation of estrogen hormones was examined in a batch reactor using a 2 kW (20 kHz) sonication unit. The degradation of estrogens follow a pseudo first order rate kinetics, and the order of degradation is 17alpha-dihydroequilin > equilin >17alpha-ethinyl estradiol >17alpha-estradiol >17beta-estradiol > estrone > estriol. Effect of solution alkalinity and salinity on the sonochemical degradation of estrogen hormones is examined. At alkalinity concentration of 10 mM, no adverse effect on the degradation rate constants of estradiols (17alpha-estradiol, 17beta-estradiol, and 17alpha-ethinyl estradiol) was observed, whereas equilin compounds showed a decrease in their degradation rate constants. Significant inhibitory effects were observed for all the compounds at high alkalinity concentration of 120 mM and which could be due to the scavenging of OH(*) radicals in the bulk solution. The presence of salinity (0.17 M) enhanced the estrogen degradation except for the equilin compounds. Simultaneous presence of high alkalinity (120 mM) and salinity (0.17 M) also increased the degradation of estrogen hormones than the case when only alkalinity (120 mM) was present, indicating the diffusion of analytes to the cavity interface where most of the degradation occurs under these conditions. A mechanistic approach was used to model the degradation behavior of estrogen hormones under different solution alkalinity and salinity conditions.

Thermodynamic and breakthrough column studies for the selective sorption of chromium from industrial effluent on activated eucalyptus bark.

Studies were carried out on adsorption of Cr(VI) on an adsorbent made from eucalyptus bark. Results revealed that sorption of chromium on activated eucalyptus bark (AEB) was endothermic in nature. Thermodynamic parameters such as the entropy change, enthalpy change and Gibb's free energy change were found out to be 100.97 J mol(-1)K(-1), 33 kJ mol(-1) and -0.737 kJ mol(-1), respectively. Industrial chrome effluent of different chromium concentration at different pH was used as feedstock for the fixed bed adsorption studies. When effluent was fed to the column at low pH of 2, the breakthrough volume increased significantly compared to effluent at higher pH of 4.85. The surface properties of sorbent were characterized by the Scanning electron microscopy, X-ray diffraction technique and Infrared techniques. It was concluded that AEB sorbent column could be used effectively for removal of chromium from industrial effluents by reducing the pH of chrome effluent to two and at optimal column conditions.

Solidification/stabilization of arsenic containing solid wastes using portland cement, fly ash and polymeric materials.

Stabilization/solidification (S/S) is used as a pre-landfill waste treatment technology that aims to make hazardous industrial wastes safe for disposal. Cement-based solidification/stabilization technology is widely used because it offer assurance of chemical stabilization of many contaminants and produce a stable form of waste. The leaching behavior of arsenic from a solidified/stabilized waste was studied to obtain information about their potential environmental risk. Activated alumina (AA) contaminated with arsenic was used as a waste, which was stabilized/solidified (S/S) using ordinary portland cement (C), fly ash (FA), calcium hydroxide (CH) and various polymeric materials such as polystyrene and polymethyl methacrylate (PMMA). Toxicity characteristics leaching procedure (TCLP) and semi-dynamic leach tests were conducted to evaluate the leaching behavior of arsenic. Formations of calcite along with precipitate formation of calcium arsenite were found to be responsible for low leaching of arsenic from the stabilized/solidified samples. Effective diffusivity of arsenic ion from the matrix and leachablity index was also estimated. Minimum leaching of the contaminant was observed in matrix having AA+C+FA+CH due to the formation of calcite.

Equilibrium and kinetics studies on removal of arsenite by iron oxide coated activated alumina.

Arsenic in drinking water is causing much concern because of its toxicity. It occurs in water naturally as As(III) and As(V). Of these As (III) is more toxic. Adsorption on activated alumina has been one of the most commonly used methods for As (V) removal from drinking water. But it is not very effective for As (III). Activated alumina was modified by coating it with Iron oxide to make it suitable for As (III) adsorption. Iron oxide coated activated alumina was tested for its effectiveness as an adsorbent for As (III). The As (III) adsorption was strongly dependent on pH and a maximum removal of 98% was observed at a pH of 12. The adsorption process followed a first order kinetics. The equilibrium was attained after 8 hours. The kinetic study was carried out with different initial As (III) concentration. It was observed that time taken to attain equilibrium was independent of initial concentration but percentage removal decreased with increasing initial concentration. The adsorption isotherms were fitted well to both Langmuir and Freundlich equation.