Preferencje help
Widoczny [Schowaj] Abstrakt
Liczba wyników

Znaleziono wyników: 5

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

Wyszukiwano:
w słowach kluczowych:  anaerobic treatment
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
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.
In order to upgrade the quality of anaerobically treated effluent to a level recommended for irrigation, integration of a UASB reactor with UV and AOPs (advanced oxidation processes) (Ozone, H2O2/UV, Fenton, and photo-Fenton) could be a better option for almost complete colour, COD removal, and disinfection of pathogens. High efficiency of the UASB can be maintained by proper process conditions, including temperature, sludge age, pH, hydraulic retention time, and gas-liquid-solid separator (GLSS) design. A fraction of the COD and colour is usually non-biodegradable and renders difficulty for anaerobic digestion. AOPs degrade the organic molecules and converting completely the organic compounds to non-toxic components such as CO2 and/or water. As far as disinfection is concerned, advanced oxidation processes are proved to be extremely effective in killing pathogens (total coliform, fecal coliform, fecal streptococci, salmonella, and E. coli) due to their strong oxidative characters. Although AOPs effectively accomplish pathogen elimination, re-growth of pathogenic microorganisms can take place in the treated effluent. Re-growth potential of pathogens provides helpful information about the quality of the treated water, which is very important in all possible reuse options. The combined application of AOPs with anaerobic treatment minimizes the chances of regrowth due to irreparable damage to nucleic acid. This review paper focuses primarily on the process conditions and treatment efficiency for UASB treatment systems, and to evaluate the advanced oxidation processes (AOPs) as an option for post treatment.
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.