Bench-scale anaerobic bioconversion of newsprint and office paper.

Anaerobic bioconversion of newsprint and waste office paper was performed in bench-scale reactors with three inocula sources: landfill, rumen, and anaerobic digester. Office paper bioconversion was nearly complete within 20 days but continued for about 165 days with methane yield efficiencies ranging from 71-85% of potential chemical oxygen demand (COD) conversion. Average newsprint methane conversion efficiencies ranged from 32-41% of total COD under strictly anaerobic conditions for 300 days. Mass balance calculations revealed that more than 80% of newsprint cellulose was biodegraded. The apparent limiting factor for anaerobic bioconversion of newsprint was the physical association between lignin and cellulose. After proper acclimation, the three inocula tested equally well for methane production under strictly anaerobic conditions. Testing of ground, shredded strips, and whole paper pieces showed no effects of feedstock size on bioconversion rate or extent. Alkali pretreatment with NaOH concentration up to 10% significantly improved newsprint biodegradability. Treatment for longer duration or at elevated temperatures increased the solubilization of lignin, but did not improve bioconversion of newsprint to methane. Neutralizing treated samples with carbon dioxide gave higher methane yields compared to sulfuric or hydrochloric acids, suggesting that digester neutralization could be combined with biogas scrubbing.

Transformations of TNT and related aminotoluenes in groundwater aquifer slurries under different electron-accepting conditions.

The transport and fate of pollutants is often governed by both their tendency to sorb as well as their susceptibility to biodegradation. We have evaluated these parameters for 2,4,6-trinitrotoluene (TNT) and several biodegradation products. Slurries of aquifer sediment and groundwater depleted TNT at rates of 27, 7.7 and 5.9 microM day-1 under methanogenic, sulfate-reducing and nitrate-reducing conditions, respectively. Abiotic losses of TNT were determined in autoclaved controls. Abiotic TNT loss and subsequent transformation of the products was also observed. These transformations were especially important during the first step in the reduction of TNT. Subsequent abiotic reactions could account for all of the transformations observed in bottles which were initially nitrate-reducing. Other controls removed TNT reduction products at much slower rates than slurries containing live organisms. 2-Amino-4,6-dinitrotoluene was produced in all slurries but disappeared in methanogenic and in sulfate-reducing slurries within several weeks. This compound was converted to 2,4-diamino-6-nitrotoluene in all slurries with subsequent removal of the latter from methanogenic and sulfate-reducing slurries, while it persisted in autoclaved controls and in the nitrate-reducing slurries. Aquifer slurries incubated with either 2,4- or 2,6-diaminotoluene showed losses of these compounds relative to autoclaved controls under nitrate-reducing conditions but not under sulfate-reducing or methanogenic conditions. These latter compounds are important as reduced intermediates in the biodegradation of dinitrotoluenes and as industrial chemicals. In experiments to examine sorption, exposure to landfill sediment resulted in losses of approximately 15% of diaminotoluene isomers and 25% of aminodinitrotoluene isomers from initial solution concentrations within 24 h. Isotherms confirmed that the diaminotoluenes were least strongly sorbed and the amino-dinitrotoluenes most strongly sorbed to this sediment, while TNT sorption capacity was intermediate. In our studies, 2,4,6-triaminotoluene sorption capacity was indeterminate due to its chemical instability. Coupled with biodegradation information, isotherms help describe the likelihood of contaminant removal, persistence, and movement at impacted sites.

Effect of fluoride on nitrification of a concentrated industrial waste.

The potential for biological nitrification of an industrial waste containing 4,000 mg of ammonia N (NH(4)-N) and 10,000 mg of fluoride per liter was investigated. Ammonium sulfate and sodium fluoride were tested in various combinations of 100 to 2,000 mg of NH(4)-N per liter and 0 to 5,000 mg of F per liter in suspended-growth stirred-tank reactors containing enriched cultures of nitrifying bacteria from a municipal sewage treatment plant. The stirred-tank reactors were fed once per day at a constant hydraulic retention period and cell retention time of 10 days. Temperature was 23 degrees C, and pH was 7.0 to 7.5. Clarified secondary effluent was used to make up feeds and to provide minor nutrients. Steady-state data, confirmed by mass balances, were obtained after five to six retention periods. In the absence of fluoride, nitrification efficiency was near 100% for up to 500 mg of NH(4)-N per liter. The influence of fluoride was studied at a low ammonia concentration (100 mg/liter) and exerted no significant effect on nitrification at concentrations of up to 200 mg/liter. Maximum effect of fluoride was reached at 800 mg of F per liter, and no greater inhibition was observed for up to 5,000 mg of F per liter. At the highest concentrations studied, ion pairing of ammonium and fluoride may exert a significant effect on kinetic coefficients. Kinetic analyses showed maximum specific substrate removal rates (q(max)) of NH(4)-N to be about 2.3 mg of N per mg of volatile suspended solids per day in the absence of fluoride and 0.85 mg of N per mg of volatile suspended solids per day in the presence of fluoride. The form of inhibition due to the presence of fluoride was shown to be not competitive, conforming to a mixed inhibition model.