Please use this identifier to cite or link to this item:
http://hdl.handle.net/10603/479793
Title: | Optimal Column Sequencing for Multicomponent Mixture |
Researcher: | Giri Prashant Ashokgir |
Guide(s): | Prof. Y. S. Mahajan |
Keywords: | Engineering and Technology Engineering Engineering Chemical |
University: | Dr. Babasaheb Ambedkar Technological University |
Completed Date: | 2022 |
Abstract: | The most of the distillation processes used in the chemicals, biotechnological, as well as petroleum refineries are very energy consuming and responsible for 40 to 60 percentage of the total energy requirement of the unit. In 2020, it was anticipated that distillation will use around 6 percentage of the total energy supply of the plant, handling the utilities of such operations is crucial. Distillation is the operation that is employed more often throughout the newlineindustrial applications, which is a process of separating distinct hydrocarbons based on the variations in their relative volatilities or boiling points. Distillation is accountable for about 90 95 percentage among all separation methods and uses approximately 40 60 percentage of the energy in the chemical and refining industries. newlineThe scientific literature on distillation as a method for separating a feed mixture into its newlinecomponents stretches back at least many centuries. However, despite the large amount of research on this subject, there are still a great number of outstanding pending issues. Since it is more energy consuming operation, which is one of the factors that may have prompted the majority of past study. Heat integration between columns or between the column and other newlineelements of the plant has been the standard strategy for boosting plant efficiency. However, due to the inspection of Indian company policies and the limitations imposed by environmental legislation, most recent research focuses on designs that provide operational (energy) and capital cost savings. newlineThis work proposes three different methods (parametric method, rigorous method and newlineevolutionary-algorithmic approach) for the selection of distillation column sequences. The salient feature of these methods is the application of quantified criterion that determines the optimal sequence for a range of separation problems. newline |
Pagination: | |
URI: | http://hdl.handle.net/10603/479793 |
Appears in Departments: | Department of Chemical Engineering |
Files in This Item:
File | Description | Size | Format | |
---|---|---|---|---|
0.01 cover page.pdf | Attached File | 109.28 kB | Adobe PDF | View/Open |
0.06 contents.pdf | 208.13 kB | Adobe PDF | View/Open | |
0.0 front pages.pdf | 1.15 MB | Adobe PDF | View/Open | |
0.1 abstract.pdf | 280.3 kB | Adobe PDF | View/Open | |
0.2 chapter01_introduction.pdf | 625.05 kB | Adobe PDF | View/Open | |
0.3 chapter02_literature review.pdf | 637.76 kB | Adobe PDF | View/Open | |
0.4 chapter03_development of proposed methods.pdf | 656.13 kB | Adobe PDF | View/Open | |
0.5 chapter04_application examples.pdf | 1.79 MB | Adobe PDF | View/Open | |
0.6 chapter05_conclusions.pdf | 185.38 kB | Adobe PDF | View/Open | |
0.8 references.pdf | 470.63 kB | Adobe PDF | View/Open | |
80_recommendation.pdf | 178.5 kB | Adobe PDF | View/Open |
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