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The results of anaerobic treatment of molasses processing wastewater in labscale AHR are presented. The performance of the model has shown that wastewater from molasses processing in BIOPO Leopoldov is suitable for anaerobic treatment. In the reactor, anaerobic granulated biomass was cultivated. As follows from granulation process observation, intensive wash-out of the suspended biomass started at Bv= 10-12 kg/m3d. This loading is significantly higher compared to the wash-out from UASB reactors with similar dimensions and technological parameters, as separation in the AHR filter layer is more effective than the separation in UASB gasliquid-solid separators. At Bv = 13 kg/m3d the operation of AHR was completed under the following parameters: hydraulic retention time =0.34 d, sludge concentration =26,4 g/1, COD removal =89%, effluent suspended solids < 100mg/l, and effluent COD about 500 mg/1.
The influence of solid retention time on cadmium uptake by activated sludge at different concentrations of the metal was studied. Activated sludge was cultivated in a lab-scale bioreactor with plug-flow pattern. Respirometric measurements were applied to evaluate the inhibitive effects of cadmium on activated sludge. The obtained values of the conditional adsorption constant indicate a similar affnity of cadmium to activated sludges cultivated in both plug-flow and complete-mixing reactors. The decrease of the metal affinity to activated sludge cultivated in a semicontinuous system with an increasing solid retention time was observed. High value of the mass ratio of cadmium in the activated sludge to metal in the surrounding liquid phase at equilibrium conditions made possible subsequent cadmium recovery. Maximum inhibition of cadmium to non-acclimated activated sludge was observed after 6 to 10 hours of exposure. The highest toxicity of this metal was observed between 2 and 5 hours after cadmium dosing of the acclimated sludge. A beneficial influence of solid retention time on the toxicity of the metal with regard to non-acclimated activated sludge resulted from this work.
This paper reviews the present status of sewage, wasterwater treatment and water quality management in Slovakia. The impact of discharged wastewater on the quality of receiving waters is presented. Legislation in Slovakia is compared with European legislation concerning water quality effluent standards. Typical treatment methods used are described and the problems of wastewater monitoring discussed. The serious problems with sludge treatment and disposal are analyzed. Possible perspectives with the relation of size of wastewater treatment plants and the requirements of approved effluent standards are indicated. The suggested steps for improving the present situation in this field are presented.
Half a year experience in sludge dosing from a water treatment plant to the municipal wastewater treatment plant in Holič is presented. Sludge from the water treatment plant containing a high percentage of iron (15 t%) in different forms was used as a coagulant. The dosing of water treatment sludge at the WWTP strengthened the water treatment effect on insoluble substances, phosphorus removal, and caused a remarkable improvement of the sedimentation properties of the wastewater treatment sludge.
Due to its structure, hexamethylenetetramine (HMT) is a slowly biodegradable substance, hydrolysing in acid environment to ammonium and formaldehyde. Formaldehyde is toxic under normal conditions for biological treatment processes. Following an adaptation, a formaldehyde concentration of 1000 mg·l⁻¹ may become biodegradable both in aerobic and anaerobic conditions. Acidic conditions for hydrolysis may be created chemically or by using natural biological treatment processes. The process of nitrification may be used in aerobic treatment, when H⁺ ions are created and pH drops below 5. For anaerobic treatment, the process of acidification may be used, when volatile fatty acids are formed and pH of the environment is decreasing. This work examines HMT degradation in an anaerobic baffled reactor (ABR). Spatial segregation of individual anaerobic degradation phases was used in the ABR, when hydrolysis and acidification in the first reactor compartments are accompanied by low pH values in these compartments. ABR performance was compared with UASB (upflow anaerobic sludge bed) reactor performance working under the same conditions. The removal efficiency of 95.8% HMT in ABR reactor and of 85.4% in UASB reactor, respectively, was measured at the organic loading 4 kg·m⁻³·d⁻¹ and retention time 84 hours. 98% overall COD (chemical oxygen demand) removal was measured in ABR reactor and 95.6% in UASB reactor. The ABR proved to be the appropriate reactor for HMT removal. Better results of HMT removal in the ABR reactor in comparison with the UASB reactor were proved.
Denitriiication using real wastewaters from chemical production was studied in lab-scale reactors. The wastewater streams contained as main compounds vinyl acetate, acetaldehyde and methanol. The highest denitrification rates were estimated in the wastewater with vinyl acetate. The effect of the tested substrates on endogenous metabolism and nitrification inhibition is discussed.
Sugar beet pulp is a very suitable material for anaerobic biodegradation. This work investigates anaerobic treatment of sugar beet pulp in a pilot plant. The pilot plant consisted of an acidogenic reactor (volume 5.3 m(3)) and an methanogenic reactor (volume 3.5 m(3)). It was found that designed technology was convenient for both, high degradation of beet pulp dry matter and sufficient specific biogas production. Recommended organic loading rate for the acidogenic reactor was 20 kg, COD m(-3) d(-1), hydraulic retention time 4 days, and maximum content of acidified pulp (dry matter) in this reactor - 6-7%. During the operation period, the organic loading of the methanogenic reactor achieved was 21 kg COD m(-3) d(-1). Hydraulic retention time in this reactor varied from 27 days (at the loading 3 kg m(-1) d(-1)) to 3.9 days (at the loading 21 kg m(-1) d(-1)). An average value of specific biogas production was 0.391 m(3) per kg of dried beet pulp added. The average efficiency of dried pulp matter degradation was 91.5%.
Distillery wastewater treatment in a laboratory anaerobic UASB reactor is described. The aim of the modelling was to determine optimum reactor organic loading and the design reactor volume. The process was followed at 20°C reactor temperature, because the distillery wastewater was diluted with municipal wastewater to achieve the required nutrient balance (the UASB reactor will be situated at a municipal wastewater treatment plant). In addition, the effect of high suspended solids concentrations in distillery wastewater on UASB treatment efficiency is described. Separation of suspended solids in a pre-equalization tank followed by stabilization of settled solids in a digester of municipal sewage sludge was proposed to eliminate the accumulation of these solids in the UASB sludge bed.
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