Informacja

Drogi użytkowniku, aplikacja do prawidłowego działania wymaga obsługi JavaScript. Proszę włącz obsługę JavaScript w Twojej przeglądarce.

Wyszukujesz frazę "Wiśniewski, D." wg kryterium: Autor


Wyświetlanie 1-3 z 3
Tytuł:
Wpływ obciążenia hydraulicznego Okresowego Bioreaktora Beztlenowego odciekami na warunki termiczne fermentacji oraz skład wytwarzanego biogazu
Influence of Hydraulic Loading Rate of Sequence-Anaerobic-Bioreactor on Fermentation Conditions and Generation of Biogas
Autorzy:
Białowiec, A.
Wiśniewski, D.
Pulka, J.
Wiśniewski, A.
Powiązania:
https://bibliotekanauki.pl/articles/1818579.pdf
Data publikacji:
2015
Wydawca:
Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:
biogaz
odcieki
recyrkulacja
bioreaktor
odpady komunalne
temperatura
biogas
leachate
recirculation
bioreactor
municipal solid waste
temperature
Opis:
The technology of municipal solid waste biological treatment in Sequence-Anaerobic-Bioreactors consists an enhanced, and controlled fermentation occurring in waste heap having status of bioreactor. Comparing to traditional landfills, where also as an effect of biological processes biogas is generated, the organic waste stabilization is accomplished after 5 years. According to construction, and operation regime, the reactor is a sequence bioreactor having self-heating character. Waste, substrate, are delivered into bioreactor once time, bioreactor is closed, gas extraction and leachate recirculation system, and monitoring devices are installed. Finally mineral sealing is placed. From that moment optimization of conditions of fermentation process by gathering, treatment, and recirculation of leachate starts. Sequence-Anaerobic-Bioreactor has been implemented by USKOM Ltd. Enterprise in location of Kosiny Bartosowe near Mlawa. Bioreacto has total capacity of municipal solid waste 200000 Mg. The research on the influence of recirculation of leachate on Sequence-Anaerobic-Bioreactor, with hydraulic loading rate ranging from 0 to 4 mm/d, on fermentation conditions and biogas composition were done. The measurements of temperature inside the bioreactor, and gas composition in gas wells were executed. The implementation of leachate recirculation with hydraulic loading rate from 1 to 4 mm/d improved the fermentation conditions and quality of generated biogas. The hydraulic loading rate of leachate 1 mm/d has been proposed for application.
Źródło:
Rocznik Ochrona Środowiska; 2015, Tom 17, cz. 2; 1259-1273
1506-218X
Pojawia się w:
Rocznik Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Biosuszenie pofermentu z biogazowni rolniczych
Biodrying of the Digestate from Agricultural Biogas Plants
Autorzy:
Białowiec, A.
Wiśniewski, D.
Pulka, J.
Siudak, M.
Jakubowski, B.
Myślak, B.
Powiązania:
https://bibliotekanauki.pl/articles/1818636.pdf
Data publikacji:
2015
Wydawca:
Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:
poferment
biosuszenie
utrata masy
temperatura
digestate
biodrying
mass loss
temperature
Opis:
Anaerobic digestion residue represents a nutrient rich resource which, if applied back on land, can reduce the use of mineral fertilizers and improve soil fertility. However, dewatering of digestate may be recommended in certain situation. Limited applicability of digestate as fertilizer may appear, especially in winter, during the vegetation period or in areas where advanced eutrophication of arable land and water bodies is developing. The use of digestate may be also governed by different laws depending on whether it is treated as fertilizer, sewage sludge or waste. The solution for thus problem may by application of biodrying process. The aim of this paper is to present the possibilities of digestate from agricultural biogas plant drying in biodrying process, and analysis of its kinetic and efficiency. Dewatered digestate from agricultural biogas plant, with initial moisture of 78%, was mixed with wood chips in proportion 45:55, respectively. The mixture was placed in container reactor, and aerated during 4 weeks. During the experiment the temperature in the reactor, weight of the digestate, and energy demand was measured. Due to biodrying process, with mean air flow rate 0.025 m3/kg.h, 502 kg mass loss was achieved, what consists 76% of the initial weight of the digestate. Mean temperature in the bioreactor during first 10 days, fluctuated between 55 to 60°C. After that, gradual decrease of the temperature to 40°C in the end of 3rd week was observed. During last week the intense cooling of the bioreactor to final temperature below 20°C was observed. It was determined, that digestate mass loss had I-order reaction character. The k constant rate value was estimated, which was on the level of 0.00068 [1/h]. Total energy demand was 14.792 kWh, what relates to 0.0295 kWh of used energy per kg of mass removed.
Źródło:
Rocznik Ochrona Środowiska; 2015, Tom 17, cz. 2; 1554-1568
1506-218X
Pojawia się w:
Rocznik Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Badania ruchowe prototypowego reaktora zgazowania biomasy
Operational Studies of Prototype Biomass Gasification Reactor
Autorzy:
Wiśniewski, D.
Piechocki, J.
Białowiec, A.
Pulka, J.
Siudak, M.
Jakubowski, B.
Myślak, B.
Powiązania:
https://bibliotekanauki.pl/articles/1818633.pdf
Data publikacji:
2015
Wydawca:
Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:
zgazowanie termiczne
syngaz
biomasa
charakterystyka pracy
dolnociągowy reaktor
thermal gasification
syngas
biomass
operation characteristics
downward reactor
Opis:
Gasification reactors are devices for thermochemical biomass treatment. In such reactors, complex of mass, and heat exchange, interphase, and chemical processes occur. Designing a mathematical models of processes occurring in such devices requires expensive research, and leads not always to satisfying results. Moreover, some authors executed complex computational simulations of gasifying process aiming to approximate calculation of: composition of generated syngas, temperatures level in the reactor, and even simulations of two-phase flow of gas enriched in pollutants. In given article the initial research of prototype downward gasification reactor feed by model feedstock – wood pellets, has been presented. The construction of the reactor has been described. Particular parts of the reactor has been shown, and the concept of reactor controlling has been given. The gasification reactor tightness has been examined by testing the generated pressure in gasification chamber. Executed research aimed on testing the correctness of particular elements of the reactor work, and determination of motion characteristic for wide range of technological parameters. Static characteristics of bed temperature in the oxidation zone, and the converted biomass stream in function of gasifying agent have been determined. Additionally, the characteristics of removed carbonizate stream in function of grate rotation rate has been determined. In the further experiments the dynamic characteristics of gasification process in the prototype reactor will be tested. The composition of syngas generated from hardly treatable waste materials will be measured. Determined characteristics will be used for further experiments on designing of process control algorithms.
Źródło:
Rocznik Ochrona Środowiska; 2015, Tom 17, cz. 2; 1094-1112
1506-218X
Pojawia się w:
Rocznik Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
    Wyświetlanie 1-3 z 3

    Ta witryna wykorzystuje pliki cookies do przechowywania informacji na Twoim komputerze. Pliki cookies stosujemy w celu świadczenia usług na najwyższym poziomie, w tym w sposób dostosowany do indywidualnych potrzeb. Korzystanie z witryny bez zmiany ustawień dotyczących cookies oznacza, że będą one zamieszczane w Twoim komputerze. W każdym momencie możesz dokonać zmiany ustawień dotyczących cookies