Autor: Kwarciak-Kozłowska, A. - Katalog OPAC zbiorów

Skocz do pozycji: 1.

Tytuł:: Sposoby eliminacji odorów w procesie kompostowania
Methods for Elimination of Odor in the Composting Process
Autorzy:: Gałwa-Widera, M.
Kwarciak-Kozłowska, A.
Powiązania:: https://bibliotekanauki.pl/articles/1818081.pdf
Data publikacji:: 2016
Wydawca:: Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:: kompostowanie
odory
biofiltracja
mikroorganizmy
composting
odors
biofiltration
microorganisms
Opis:: Composting is a process that allows the elimination of pathogenic microorganisms, and includes biological sludge stabilization in aerated heaps or in sealed chambers with the addition of supplementary substances. An organic substance that is converted into compost is a good product for soil improvement and land reclamation. Compost is a good organic fertilizer used as manure in rural agglomerations. Organic matter included in the compost affecst the properties of the soil, improves the relationship between water and air, as well as soil rich in nutrients. Compost has the additional properties for improving the structure of light and heavy soils. The temperature of the resulting compost pile can reach up to 70°C. Hight temperature affects the removal of pathogenic microorganisms. In wastewater treatment plants, where the processing of sludge includes dewatering process and fermentation composting can be used as the final sludge processing operation, which is a valuable material intended to be used in nature (assuming that it meets the requirement pertaiting to heavy metal content). Treatment processes significantly influences the type of emitted odorant. During the anareobic process different and more intense odors are produced than under aerobic conditions. Odors are often emitted furing the biological treatment processes. They may be released during storage and transportation of raw materials, during the compost and- in each phase of the composting process.
Źródło:: Rocznik Ochrona Środowiska; 2016, Tom 18, cz. 2; 850-860
1506-218X
Pojawia się w:: Rocznik Ochrona Środowiska
Dostawca treści:: Biblioteka Nauki

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Tytuł:: The Application of Integrated System in Dairy Wastewater Treatment
Zastosowanie zintegrowanego system w oczyszczaniu ścieków mleczarskich
Autorzy:: Kwarciak-Kozłowska, A.
Gałwa-Widera, M.
Bień, J.
Powiązania:: https://bibliotekanauki.pl/articles/1813672.pdf
Data publikacji:: 2018
Wydawca:: Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:: dairy wastewater
photocatalysis
TiO2
ZnO
advanced oxidation process
ultrafiltration
ścieki mleczarskie
fotokataliza
zaawansowane metody utleniania
ultrafiltracja
Opis:: The study presented the results of the examinations obtained during treatment of dairy wastewater in a membrane photoreactor where photocatalysis was sequentially combined with low-pressure membrane process. The aim of the study was to determine the effectiveness of degradation of the contaminants contained in such wastewater during photocatalysis and in the arrangement that combined photocatalysis with ultrafiltration. Several experiments were performed in order to determine the most beneficial conditions of the photocatalysis process, e.g. the dose of the photocatalysts used (TiO2 and ZnO), duration of the process and pH of wastewater subjected to oxidation. The dose of titanium dioxide was changed from 1 to 40 g/dm3, whereas the content of zinc oxide ranged from 1 to 6 g/dm3. The results obtained in the study showed that the extension of the irradiation time to over 30 minutes (TiO2) and over 45 minutes (ZnO) during photocatalysis does not lead to increased removal of contaminants from the dairy wastewater. It was also demonstrated that the increase in the doses of both photocatalysts does not lead to the increase in the efficiency of their treatment. In the case of treatment of dairy wastwater with TiO2, the photocatalysis occurred most effectively for its dose of 10 g/dm3. Removal rates for COD, TOC and total nitrogen were 58% (1670 mg/dm3), 62% (450 mg/dm3) and 56% (128 mg/dm3), respectively. Replacing titanium dioxide with zinc oxide (ZnO – 2 g/dm3) in the photocatalysis process allowed for obtaining higher degrees of removal of contaminants determined as COD, TOC and total nitrogen to the level of 77.8% (870 mg/dm3), 62% (445 mg/dm3) and 52% (139 mg/dm3), respectively. Since both photocatalysts were supplied to the photoreactor in the form of a suspension, the membrane in the next reactor represented an efficient barrier for their particles. It was observed that higher volumetric stream of the permeate was obtained during the process of low-pressure membrane filtration of sewage initially treated in the process of photocatalysis with titanium dioxide (4.6·10-5 m3/m2·s – TiO2 and 4.1·10-5m3/m2·s – ZnO). It was found that the ultrafiltration process in the case of the feed material with TiO2 led to the reduction in COD, TOC and total nitrogen by 78% (370 mg/dm3), 72% (126 mg/dm3) and 40% (80 mg/dm3). Slightly better quality of permeate was obtained when the feed material contained ZnO powder. Degree of retention of the contaminants COD, TOC and total nitrogen were 68% (280 mg/dm3), 66% (143 mg/dm3) and 42% (76 mg/dm3), respectively.
W pracy zaprezentowano wyniki badań jakie otrzymano podczas oczyszczania ścieków mleczarskich w fotoreaktorze membranowy w którym sekwencyjnie skojarzono procesy fotokatalizę z niskociśnieniowym procesem membranowymi. Celem badań było określenie skuteczności degradacji zanieczyszczeń znajdujących się w tego rodzaju wodach odpadowych w samodzielnie prowadzonym procesie fotokatalizy jak również w układzie kojarzącym go z procesem ultrafiltracji. Przeprowadzono szereg eksperymentów w celu ustalenia najkorzystniejszych warunków prowadzenia procesu fotokatalizy tj. dawka zastosowanych fotokatalizatorów (TiO2 i ZnO), czas prowadzenia procesu oraz wartość pH ścieków poddawanych utlenianiu. Dawkę ditlenku tytanu zmieniano w zakresie od 1 do 40 g/dm3 a tlenku cynku od 1 do 6 g/dm3. Na podstawie uzyskanych wyników badań stwierdzono, że wydłużanie czasu naświetlania powyżej 30 minut (TiO2) oraz powyżej 45 min (ZnO) w procesie fotokatalizy nie wpływa na zwiększanie usunięcia zanieczyszczeń z oczyszczanych ścieków mleczarskich. Wykazano również, że zwiększanie stosowanych dawek obu fotokatalizatorów nie skutkuje wzrostu efektywności ich oczyszczania. W przypadku oczyszczania ścieków mleczarskich z TiO2 proces fotokatalizy przebiegał najkorzystniej jego dawce wynoszącej 10 g/dm3. Stopień usunięcia ChZT, OWO i azotu ogólnego wynosił odpowiednio 58% (1670 mg/dm3), 62% (450 mg/dm3) i 56% (128 mg/dm3). Zastąpienie ditlenku tytanu tlenkiem cynku (ZnO – 2g/dm3) w procesie fotokatalizy pozwoliło na uzyskanie wyższych stopni usunięcia zanieczyszczeń oznaczanych jako ChZT, OWO i azotu ogólnego odpowiednio do poziomu 77.8% (870 mg/dm3), 62% (445 mg/dm3) i 52% (139 mg/dm3). Z uwagi na fakt, że oba dawkowano do fotoreaktora w formie zawiesiny to znajdująca się w kolejnym reaktorze membrana była skuteczną barierę dla ich cząstek. Zaobserwowano, że wyższy objętościowy strumień permeatu uzyskano w trakcie prowadzenia procesu niskociśnieniowej filtracji membranowej ścieków wstępnie podczyszczonych w procesie fotokatalizy z ditlenkiem tytanu (4,6·10-5 m3/m2·s – TiO2 i 4,1·10-5 m3/m2·s – ZnO). Stwierdzono że wykorzystany proces ultrafiltracji w przypadku nadawy z TiO2 przyczynił się do obniżenia wartości wskaźników ChZT, OWO i azotu ogólnego odpowiednio o 78% (370 mg/dm3), 72 % (126 mg/dm3) i 40% (80 mg/dm3). Nieznacznie lepszej jakości permeat otrzymano, gdy nadawa zawierała proszek ZnO. Stopień retencji zanieczyszczeń ChZT, OWO i azotu ogólnego wynosił odpowiednio 68% (280 mg/dm3), 66 % (143 mg/dm3) i 42% (76 mg/dm3).
Źródło:: Rocznik Ochrona Środowiska; 2018, Tom 20, cz. 1; 602-615
1506-218X
Pojawia się w:: Rocznik Ochrona Środowiska
Dostawca treści:: Biblioteka Nauki

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Tytuł:: Reduction of Odour Nuisance of Industrial Plants – Biofiltering in Composting Plants
Autorzy:: Gałwa-Widera, M.
Kwarciak-Kozłowska, A.
Bień, J.
Powiązania:: https://bibliotekanauki.pl/articles/125363.pdf
Data publikacji:: 2018
Wydawca:: Polskie Towarzystwo Inżynierii Ekologicznej
Tematy:: biomass
composting
industry
sewage sludge
odour
Opis:: Composting produces several hundred different substances. Among them, active fragrance compounds constitute a considerable number. Composting technology and the method of conducting the process are important elements. Due to the different ways of conducting the composting process, there are also areas of odour emissions as well as the volume of emissions. Depending on whether the process is conducted statically or dynamically, in a natural or artificial way and also in an open (e.g. field prism) or closed system (reactors, containers, encapsulated plots), the amount of odourant emitted will be uneven. One of the methods is the use of biofiltration. The biological filter for air purification is designed to remove volatile air pollutants leaving various installations. By using a suitable filter bed, total organic and inorganic carbon, sulfur and nitrogen compounds such as ammonia and hydrogen sulfide can be reduced. They are part of the odours that emerge, for example, from a composting plant. The use of biofilter eliminates polluting emissions, which in practice means reducing the negative impact on the environment and neutralizing odours. The article presents the results of biogas analysis generated in the composting process and ecological methods of removing odorants in the biofiltration process. Two types of filling were used to fill the biofilter. Both are fully biodegradable. It has been shown that these fillings have a high impact on the development of biofilm, and thus on the reduction of pollution.
Źródło:: Journal of Ecological Engineering; 2018, 19, 5; 135-143
2299-8993
Pojawia się w:: Journal of Ecological Engineering
Dostawca treści:: Biblioteka Nauki

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Skocz do pozycji: 4.

Tytuł:: Wykorzystanie procesu ozonowania w oczyszczaniu ścieków koksowniczych
The Use of Ozonation Process in Coke Wastewater Treatment
Autorzy:: Kwarciak-Kozłowska, A.
Krzywicka, A.
Gałwa-Widera, M.
Powiązania:: https://bibliotekanauki.pl/articles/1818115.pdf
Data publikacji:: 2016
Wydawca:: Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:: ścieki koksownicze
ozonowanie
zaawansowane metody utleniania
coke wastewater
ozonation
advanced oxidation process
Opis:: The paper presents presents the possibility of using the ozonation process in coke wastewater treatment. The wastewater produced during processing of coke was initially pre-treated mechanically in order to remove solid impurities, oils and tar substances. The raw wastewater was characterized by the phenolic odor, brown color and alkaline pH (pH 9.2). The COD value of raw wastewater was 8100 mg/dm3 and the value of BOD was very low (180 mg/dm3). A high concentration of total nitrogen (2420 mg/dm3) and TOC (2240 mg/dm3) was also noted. The study was conducted in three stages. In the first stage, coking wastewater was treated only by ozone, the dose of which varied from 10 mg/dm3 to 40 mg/dm3. The effect of pH during ozonation process was determined on TOC removal efficiency. For all of the pH values (pH = 3.5, pH = 7, pH = 8.5 and pH = 11.5) the TOC removal rate constant was determined. In the second stage, the rate OH radicals generation was accelerated by the addition of hydrogen peroxide to the reactor. The ratio by weight of COD: H2O2 was 1:2.5, 1:5, 1:10 and 1:20. In the last stage of the study, we attempted to assist the ozonation process with ultrasonic field. The sonication time was 8 minutes and the amplitude was 61.5 μm. It was found that the ozonation process is the most effective at alkaline pH (8.5). The TOC removal efficiency was 34% (1470 mg/dm3) after 60 minutes of ozonation. The best results of oxidation of pollutants measured as COD and TOC removal were observed when the dose of ozone was 30 mg/dm3.The combination of sonication and ozonation has resulted in a reduction of COD and TOC values by 1000 mg/dm3 and 300 mg/dm3, respectively, in comparison to ozonation process alone. It was found that the most effective process in coke wastewater treatment is the combination of ozonation with hydrogen peroxide addition (COD:H2O2=1:10). The COD, TOC and BOD value were 54%, 35% and 20% lower, respectively, in comparison to ozonation process conducted alone.
Źródło:: Rocznik Ochrona Środowiska; 2016, Tom 18, cz. 2; 61-73
1506-218X
Pojawia się w:: Rocznik Ochrona Środowiska
Dostawca treści:: Biblioteka Nauki

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