Preferencje help
Widoczny [Schowaj] Abstrakt
Liczba wyników

Znaleziono wyników: 12

Liczba wyników na stronie
Pierwsza strona wyników Pięć stron wyników wstecz Poprzednia strona wyników Strona / 1 Następna strona wyników Pięć stron wyników wprzód Ostatnia strona wyników

Wyniki wyszukiwania

help Sortuj według:

help Ogranicz wyniki do:
Pierwsza strona wyników Pięć stron wyników wstecz Poprzednia strona wyników Strona / 1 Następna strona wyników Pięć stron wyników wprzód Ostatnia strona wyników
The present study looks at the adsorption of polyethylene glycol onto activated carbon with the different molecular weight. The amount of PEG adsorbed on activated carbon depends on temperatures and pH. The adsorption capacities were determined through the adsorption isotherms. The results of the adsorption isotherm and kinetic studies show that the adsorption process can be well described with the Langmuir model. After linearization of the Arrhenius equation the activated energy had been estimated.
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.
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.
The results of experimental and mathematical modelling of simultaneous carbonization, nitrification and denitriiication processes in an industrial wastewater treatment plant are presented. Simplified dynamic mathematical models based on organic and nitrogen substrates, autotrophic and heterotrophic biomass material balances for complete-mixing and tank-in-series hydraulic regimes and Monod-type kinetics were developed. These models were verified by using experimental data obtained in laboratory tank-in-seres equipment with high internal recirculation flow as well as by application of the real Carriousel plant data. The influence of unsteady-state conditions on selected process kinetic parameters was also studied in this work. The process dynamic behaviour in the lab-scale tank-in-series equipment was modelled by step shock loading of the substrate concentration.
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.
A general algorithm of hydraulic protection of groundwater (HPGW) control based on the checking of the maximal closed groundwater contour is proposed. A model describing only flow of groundwater (not spreading of contaminants) is used and therefore short computational time is sufficient to simulate various operational regimes of HPGW. Groundwater flow is described by a twodimensional two-parameters model with 'real time' generation of boundary conditions. Operation of HPGW is determined on the prediction of HPGW behaviour for 2-3 weeks forward. Results obtained using the developed algorithm are illustrated on a real HPGW operating at the 'Žitný Ostrov' in Slovakia. The usage of the proposed algorithm has made it possible to shorten total groundwater pumping to two thirds of the original value.
The process of simultaneous precipitation of phosphorus from synthetic wastewater in aerobic biological systems with Fe(II) and Al(III) salts has been studied. Respirometric measurements have been applied to rvaluate the influence of heavy metals on activated sludge respiration activity. The factors which influence the evaluation of inhibition or stimulation effect of precipitants on biomass have been studied. The stimulation effect of Fe on heterotrophic biomass respiration activity was observed in typical metal concentrations range applied in the chemical process of phosphorous removal. The influence of precipitants on biokinetic parameter values has been investigated. Not only phosphorus elimination and the increase of activated sludge activity, but also the improvement of sludge settlement characteristics and improved efficiency of organic impurities removal resulted from the work.
Activated Sludge Model No. 1 (ASM1) was used in the modeling of an activated sludge system treating effluents from an oil refinery. The measurements of the diurnal variation in wastewater flow and composition at the wastewater treatment plant inlet and outlet were carried out. The calibrated model predicting the influence of changes in the wastewater composition and the operational parameters on the effluent wastewater quality and the related operational costs is available. A calibration technique based on the heuristic method was applied. The model was used to analyze the influence of changes in wastewater flow and composition as well as different aeration systems on the process performance. The results of dynamic simulations indicate that the verified dynamic mathematical model is a useful supporting tool for optimizing operational parameter values and operational costs. The presented results are for illustration purposes only and are not intended as instructions for the operation of a wastewater treatment plant.
Seven small wastewater treatment plants were chosen for evaluation. These WWTPs work on the principle of anaerobic pre-treatment and aerobic post-treatment and were made with the cooperation of Slovak Technical University with ASIO-SK s.r.o. Bytča and ASIO s.r.o. Brno. Wastewater treatment plants are made for 5-600 PE. When operated at suitable conditions, the results match the directive water discharge from small wastewater treatment plants in the Slovak Republic.
An intermittently aerated completely mixing lab-scale bioreactor was applied in the modelling of simultaneous nitrification and denitrification processes carried out in the Carrousel system. Two kinetic models based on the IAWPRC task group kinetic and stoichiometric concept were developed and verified. The model parameters number is reduced and the influence of waste water composition on oxygen transport rate is implicitly incorporated by the evaluation of oxic and anoxic "switching functions" based on oxygen profile data monitored in the bioreactor. The advantages of this approach in comparison to the tank-in-series model are 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%.
Pierwsza strona wyników Pięć stron wyników wstecz Poprzednia strona wyników Strona / 1 Następna strona wyników Pięć stron wyników wprzód Ostatnia strona wyników
JavaScript jest wyłączony w Twojej przeglądarce internetowej. Włącz go, a następnie odśwież stronę, aby móc w pełni z niej korzystać.