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Proizvodnja bioetanola kao alternativnog goriva iz ostataka krompira

dc.contributor.authorSehsah, El-Sayed
dc.contributor.authorBelal, El-Sayed
dc.contributor.authorSheisha, Refai Abu
dc.contributor.authorEllawaty, Ahamed
dc.date.accessioned2015-09-11T16:56:48Z
dc.date.available2015-09-11T16:56:48Z
dc.identifier.urihttp://arhiva.nara.ac.rs/handle/123456789/629
dc.description.abstractProduction of ethanol from biomass is one way to reduce both the consumption of crude oil and environmental pollution. The current research focused to produce the bioethanol from crop wastes. The study carried out in Agricultural Engineering Department and Agric. Botany Department at faculty of Agriculture, Kafrelsheikh University. The main objective in this part of the current study is producing the bioethanol from potato wastes to applicable in the engine of the farm machine. The experiment was carried out in aerobic batch digester and bioreactor after potato tubers wastes pretreatment with Bacillus subtilis (E34) as amylolytic bacteria for 7 days. The bioreactor system consists of three main units. The first unit was ethanol reactor which represents the main unit of the fermentation process and the second is the agitating unit required to enhance the fermentation process and to increase the efficiency of ethanol production for all treatments. Third unit is the collector tank; it is consisted of the 8 liters capacity tank with input and output valves. The output valve used to measure the pH values for different ethanol production. The 10 liters of water that was feeding in solution of potatoes wastes was heated to 30°C. Bioethanol fermentation was conducted in reactor. The yeast Saccharomyces cerevisae was used for fermentation process in dried form. The inoculum was used at 50 g from dried Saccharomyces cerevisae were used to inoculate 3 l from the pretreated potato wastes. The pH of the medium was adjusted to 4.5. All experiments were incubated at 30°C under different stirring speeds (30, 120 and 200 min-1) in the reactor for 7 days. The values of the percentage of bioethanol production increased and reached to the maximum values after 18 hour of elapsed time for 30 min-1, 120 min-1 and 200 min-1 agitation rotational speeds. The maximum values of bioethanol production percentage were 37.8%, 44.45% and 68.68% after 18 hour elapsed time for 30, 120, 200 min-1 respectively. On the other hand, the increase of agitation speed from 30 to 200 min-1 tends to increase the percentage of bioethanol production. The energy requirement of volume bioethanol production increased due to increase of the agitation speed from 30 min-1 to 200 min-1. The highest value of energy requirement was 5.9 Wh at 200 min-1 after 24 hours for bioethanol production. The lowest energy requirement for agitation was 8.7 Wh at 30 min-1 after 2 hours. Bioethanol production increased and reached to 70.9% at 18 hour of duration time for bioreactor compared to 65% bioethanol percent after 18 days for batch reactor.en
dc.description.abstractProizvodnja etanola iz biomase je jedan od načina za smanjenje potrošnje sirove nafte i zagađenja okoline. Skorija istražuvanja se odnose na proizvodnju bioetanola iz biljnih ostataka. Ova studija je izvedena na Institutima za poljoprivrednu tehniku i poljoprivrednu botaniku Poljoprivrednog fakulteta Univerziteta Kafrelsheikh. Osnovni cilj ovog dela istraživanja je proizvodnja bioetanola iz ostataka krompira, koji će moći da se koristi u motorima poljoprivrednih mašina. Ogled je izveden u aerobnom digestoru i bioreaktoru posle prethodnog tretmana ostataka krompira amilolitičkom bakterijom Bacillus subtilis (E34) u trajanju od 7 dana. Sistem bioreaktora sastoji se od tri glavne jedinice. Prva je etanolski reaktor, u kome se odvija glavni deo procesa fermentacije. Drugi je aktivaciona jedinica koja pojačava fermentaciju i povećava efikasnost produkcije etanola u svim tretmanima. Treća jedinica je kolektorski rezervoar; on se sastoji od tanka kapaciteta 8 litara sa ulaznim i izlaznim ventilima. Izlazni ventil ujedno i meri pH vrednosti proizcedenog etanola. 10 litara vode, koja se dodaje u rastvor ostataka krompira, je zagrevano na 30°C. Fermentacija bioetanola je izvođena u reaktoru. Za fermentaciju je korišćen suvi kvasac, glivica soja Saccharomyces cerevisae. 50 g suvog Saccharomyces cerevisae je upotrebljeno za inokulaciju 3 litra prethodno tretiranog otpada krompira. pH vrednost je bila podešena na 4.5. U svim ogledima, inkubacija je na 30°C, pod različitim brzinama podsticanja (30, 120 i 200 min-1) u reaktoru trajala 7 dana. Procentualne vrednosti produkcije bioetanola rasle su dostigle maksimume posle 18 časova pri aktivacionim brzinama rotacije od 30 min-1, 120 min-1 i 200 min-1. Maksimalne procentualne vrednosti produkcije bioetanola iznosile su 37.8%, 44.45% i 68.68% posle 18 časova, pri aktivacionim brzinama rotacije od 30, 120, 200 min-1, redom. Sa druge strane, povećanje aktivacione brzine sa 30 na 200 min-1 ima tendenciju povećanja procenta produkcije bioetanola. Zahtevi za energijom pri proizvodnji veće zapremine bioetanola su se povećali zbog povećanja aktivacione brzine sa 30 min-1 na 200 min-1. Najveća potrošnja energije bila je 5.9 Wh pri 200 min-1 posle 24 časa proizvodnje etanola. Najmanja potrošnja energije za aktivaciju bila je 8.7 Wh pri 30 min-1 posle 2 časa. Produkcija bioetanola porasla je i dostigla 70.9% posle 18 časova u bioreaktoru, u poređenju sa 65% bioetanola posle 18 dana u digestoru.sr
dc.subjectbioethanolsr
dc.subjectproductionen
dc.subjectwastesen
dc.subjectenergyen
dc.subjectbioetanolsr
dc.subjectproizvodnjasr
dc.subjectotpadsr
dc.subjectenergijasr
dc.titleProduction of Bioethanol from Potatoes Wastes as an Alternative Fuelen
dc.title.alternativeProizvodnja bioetanola kao alternativnog goriva iz ostataka krompirasr


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  • Issue 2015-3.
    www.jageng.agrif.bg.ac.rs/files/casopis/PT_03-2015.pdf

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