Please use this identifier to cite or link to this item: http://hdl.handle.net/10603/434725
Title: Modelling and optimization based Control of dissolved oxygen for Industrial effluents in semibatch Fermenter
Researcher: Sumathi, J
Guide(s): Arulmozhi, M
Keywords: Engineering and Technology
Engineering
Engineering Chemical
dissolved oxygen
Industrial effluents
University: Anna University
Completed Date: 2021
Abstract: Effluents from industries such as textile, distillery, bone wash, paper newlineand paint pose serious environmental hazard and leads to health problems. newlineGovernment and other environmental agencies have coordinated efforts to newlinecombat or neutralize the adverse effect on human beings, animals and plants newlineby proper treatment prior to disposal. The first stage in treatment of such newlineeffluents is aeration. Arbitrary aeration of effluents in many industries has newlinebeen recorded leading to effluents with odour. Dissolved oxygen is an newlineimportant parameter in the aeration process of effluents to be controlled. newlineExperimental setup for batch process was fabricated with a speed adjustable newlineagitator in a semi batch reactor. It consist of lark hygiene fermenter, effluent newlinestorage, rotameter, Dissolved Oxygen probe (DO), stirrer, control valve and newlinepersonal computer. The 1.5 litre semi batch reactor has provisions for newlineadjustment of air flow, temperature and speed of stirrer. Fresh effluent was newlinediluted with water to obtain various concentrations ranging from 10 to 100 newlinepercent in steps of 10 percent. One litre of fresh effluent of known newlineconcentration was charged into the semi batch fermenter from storage tank 1 newlineusing a peristaltic pump. The dissolved oxygen was monitored using an online newlinedissolved oxygen probe interfaced to a PC. At time t = 0, purified air was newlinesuddenly metered through a rotameter at a rate of 1 lpm. newlineThe dissolved oxygen was monitored and recorded for ten newlineconcentrations and three speeds (135, 145, and 155 rpm) with time till newlinesaturation. Based on the data generated different models for the aeration newlineprocess with dissolved oxygen as controlled variable have been studied newline
Pagination: xxxii,207p.
URI: http://hdl.handle.net/10603/434725
Appears in Departments:Faculty of Information and Communication Engineering

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01_title.pdfAttached File181.56 kBAdobe PDFView/Open
02_prelim pages.pdf1.17 MBAdobe PDFView/Open
03_content.pdf228.74 kBAdobe PDFView/Open
04_abstract.pdf220 kBAdobe PDFView/Open
05_chapter 1.pdf459.76 kBAdobe PDFView/Open
06_chapter 2.pdf585.85 kBAdobe PDFView/Open
07_chapter 3.pdf1.54 MBAdobe PDFView/Open
08_chapter 4.pdf8.99 MBAdobe PDFView/Open
09_annexures.pdf3.71 MBAdobe PDFView/Open
80_recommendation.pdf105.68 kBAdobe PDFView/Open
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