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Anaerobic digestion and methane generation potential of rose residue in batch reactors

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dc.creator GÖNÜLLÜ, MUSTAFA TALHA
dc.creator GÜNAY, Ahmet
dc.creator Tosun, I
dc.date 2003-12-31T22:00:00Z
dc.date.accessioned 2020-10-06T09:18:38Z
dc.date.available 2020-10-06T09:18:38Z
dc.identifier 08a8bbc4-e817-4896-89eb-1e02a3ea4e6f
dc.identifier 10.1081/ese-120028402
dc.identifier https://avesis.sdu.edu.tr/publication/details/08a8bbc4-e817-4896-89eb-1e02a3ea4e6f/oai
dc.identifier.uri http://acikerisim.sdu.edu.tr/xmlui/handle/123456789/52661
dc.description In the study, anaerobic digestion of residues from rose oil industry was investigated by using a laboratory scale completely mixed batch reactor in volume of 10 L and 4 small reactors in volume of 400 mL. Ten liters reactor isolated with a water jacket and 0.4 L reactors settled into a water bath were operated at 35 +/- 1degreesC. The study supplies biochemical methane potential of hydrolyzed and original residues. Experimental results showed that hydrolyzed rose residue produced a bit more methane than original residue. Methane production results were analyzed with first-order and Chen&Hashimoto's models, and Chen&-Hashimoto's model was found to be more suitable than first-order kinetic model.
dc.language eng
dc.rights info:eu-repo/semantics/closedAccess
dc.title Anaerobic digestion and methane generation potential of rose residue in batch reactors
dc.type info:eu-repo/semantics/article


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