Sibel Uludag-Demirer

Recovery of acids from anaerobic acidification broth by liquid-liquid extraction.

In this study, anaerobic acidification of sugar beet processing wastes and subsequent liquid-liquid extraction of produced fermentation metabolites were investigated. The aim of extraction experiments was to asses the influence of pH and extractant (trioctylphosphine oxide (TOPO) in kerosene) concentrations on the recovery of volatile fatty acids (VFAs) from fermentation broth. The effect of TOPO in kerosene concentration was as crucial as the effect of pH on the recovery of VFAs via extraction. Consequently, pH 2.5 was determined as optimum. At this pH, percent recoveries of VFAs were changed from 43% to 98%, depending on the type of the acid extracted (acetic, butyric, propionic and valeric acids) and the concentration of TOPO in kerosene (5-20%). As the concentration of TOPO in kerosene was increased, efficiency of extraction was increased. As a result, highest VFA recoveries (61-98%) were observed at 20% TOPO in kerosene with distribution ratio values ranging between 1.54 and 40.79. At pH 2.5, the increase in TOPO concentration directly increased the chemical oxygen demand (COD) removal efficiencies, as it does for total VFA recovery. Up to 72% COD removals were achieved, at 20% TOPO in kerosene at pH 2.5, while the removal efficiencies remained between 19% and 22% at pH 5.5.

Effects of surface oxidation and oxygen on the removal of trichloroethylene from the gas phase using elemental iron

The reduction of trichloroethylene (TCE) in the gas phase byFe° was examined under water vapor saturatedconditions (relative humidity (RH) = 100%). The reactionconformed to first-order rate kinetics under anaerobic(N2 atmosphere) conditions and acid-washedFe°exhibited a faster TCE removal rate than unamended (partially oxidized) Fe°, i.e., kobs = 0.015 h-1 versus0.012 h-1. Analysis of the two types of Fe° showedthat 40.3% of the unamended Fe° surface was nonreactive. Experiments with iron oxides, which form commonly on the surface of Fe° exposed to humid air (magnetiteand maghemite), showed that these solids were nonreactive with TCE under anaerobic conditions. Under aerobic conditions (air),TCE reduction occurred in two distinct phases. There was a fastinitial rate followed by a slower later rate of reduction when the oxide layer was formed. Further experiments showed that theFe° surface was saturated with TCE at higher concentrations (K1/2 = 5,397.4 ± 345.4 ppmv) and thatoxygen acted as an irreversible inhibitor of TCE reduction(maximum rate of reaction decreased when oxygen was present).

Modification of a conventional anaerobic digester for improving the effluent and sludge characteristics.

The aim of this study was to enrich the composition of anaerobic digester sludge in terms of nitrogen and phosphorus by struvite (MgNH4PO4) formation. Waste activated sludge was anaerobically digested in batch reactors under the conditions that the minimum stoichiometric requirement for struvite formation was satisfied in all reactors. For this purpose, different amounts of magnesium (Mg2+) and phosphate (PO4(3-)) ions were added initially to the batch reactors. The results showed the effects of adding Mg2+ and PO4(3-) ions on the performance of anaerobic digestion and on the amounts of ammonium (NH4+) and PO4(3-) ions released during digestion. The results indicated that the performance of the anaerobic digestion in chemical oxygen demand removal changed between -4.0% and 15.4% for a Mg2+ concentration range of 277.2 to 529.3 mg/L and a PO4(3-) concentration range of 377.4 to 2372.4 mg/L. There was an increase in the concentration of NH4+ in all reactors during digestion, but the extent of concentration increase could be controlled by increasing the initial concentrations of Mg2+ and PO4(3-). The maximum removal of NH4+ ions (33.7%) was observed in the reactor dosed initially by Mg2+ and PO4(3-) concentrations of 467.2 and 2123.3 mg/L, respectively. The concentration of PO4(3-) ion was lower than its initial concentration in all reactors, indicating considerable fixation of PO4(3-) as it was released, by struvite and other solid species formation. The decrease in the concentration of Mg2+ ions similar to PO4(3-) was accepted as evidence for the formation of solid species composed of Mg2+ and PO4(3), in addition to struvite. Water

Estimating the turnover number in enzyme kinetic reactions using transient and stationary state data

Substrate and product concentration data obtained by simulating enzyme-substrate reaction rate equations were used to test two proposed kinetic rate constant estimation techniques in this study. In the first technique, the turnover number, k3, was calculated using early transient time domain data, which are difficult to obtain experimentally. The technique used an iterative approach to calculate k3 with a pair of data and the value of k3 could be retrieved with 35% error. The second technique calculated k3 using stationary domain data and the value of k3 could be retrieved with less than 5% error. This second technique also offered internal consistency in the calculation of k3 by calculating k3 both from the intercept and the slope of the linear plot derived in this study. A series of sensitivity analyses was conducted to understand the robustness of the second technique in estimating k3 from simulated data to the changes in the reaction rate constants (k1, k2, and k3) and the initial concentration of enzyme used for simulation. It was found that the second technique generally worked well in the estimation of k3 except for the simulated data for fast substrate conversions such as in the large k3 and [E]0 cases . This latter method, thus, shows promise for the use of late time experimental substrate/product concentration data to obtain k3. Exclusively using late time data avoids the need for difficult and expensive rapid early time measurement techniques for estimating k3. Once a reasonable estimate for k3 is obtained, the initial enzyme value can easily be determined from the maximum velocity constant established from fitting the Michaelis-Menten or Briggs-Haldane equations to substrate and product stationary state domain (late time) data. While the first technique can estimate k3 with only one point in the transient domain, it is suggested that the second method generally be favored since it only requires late-time stationary domain data and appears to be more accurate.

Control of Trichloroethylene Emissions from Sparging Systems by Horizontal Bio- and Chemo- Barriers

The scope of this study was to develop a continuous system to clean-up a trichloroethylene (TCE) contaminated gas stream, where biotic and abiotic removal mechanisms are undertaken sequentially simulating the horizontal bio- and chemo-barriers proposed for the in-situ remediation of the contaminated sites. The bio- and chemo-barriers were simulated by using glass columns packed with granular anaerobic mixed culture and Fe(0) filings, respectively. The effect of gas residence time, which is adjusted by the gas flowrate, on the TCE removal efficiency of the reactor system was investigated. TCE removal efficiency of over 90% was achieved at gas residence times above 1hr. Furthermore, the effluent of reactor system contained only ethane and ethylene, which are non-toxic by-products of TCE reduction reactions, along with trace amounts of TCE.