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New approach to the design and optimization of energy efficient chemical processes
by Amale, Amit, Ph.D., University of Rhode Island, 2008, 278 pages; AAT 3314439

Abstract (Summary)

Energy use in many process industries is dominated by separation processes. With increase in energy costs better methodologies for the synthesis, design and/or retrofitting of separation processes are needed. In this thesis, a novel method for determining energy efficient process designs based on finding the separation with the shortest stripping line distance is proposed. A problem formulation based on mixed integer nonlinear programming (MINLP) is given and a global optimization algorithm is presented for determining energy efficient process designs. A variety of examples of separations are used to demonstrate the versatility and advantages of the shortest stripping line distance approach over available methods in literature. One of the major advantages of the proposed methodology is that it can be used to identify minimum energy requirement for multi-unit processes such as hybrid separations involving extraction followed by distillation.

The proposed shortest stripping line distance method is extended and a two-level distillation design procedure is developed for finding portfolios of minimum energy designs when specifications are given in terms of key component recoveries. The two-level design procedure is flexible and can find minimum energy designs for both zeotropic and azeotropic distillations. The two-level design method encompasses Underwood's solution, when it exists, and can find minimum energy designs when Underwood's method is not applicable.

Non-pinched, minimum energy distillation designs are an important and often overlooked class of distillation designs that provided added economic advantages in practice. All current methods for designing distillation columns available in literature are based on the concept of pinch points and are incapable of finding non-pinched, minimum energy solutions. In contrast, it is demonstrated that shortest stripping line distance approach is capable of systematically and reliably finding non-pinched, minimum energy distillation designs as well as providing insights into the reasons for the existence of non-pinched, minimum energy design.

Studied examples clearly show that the shortest stripping line distance methodology is indeed a powerful and versatile tool for designing energy efficient processes and can be considered as a next generation method for conceptual design of energy efficient chemical processes.

Indexing (document details)

Advisor:Lucia, Angelo
School:University of Rhode Island
School Location:United States -- Rhode Island
Keyword(s):Energy efficiency, Two-level design method, Distillation design, Nonpinched solution, Shortest stripping line, Hybrid separations, Extraction-distillation
Source:DAI-B 69/05, Nov 2008
Source type:Dissertation
Subjects:Chemical engineering
Publication Number: AAT 3314439
ISBN:9780549633723
Document URL:http://proquest.umi.com/pqdlink?did=1543908481&Fmt=7&clientI d=79356&RQT=309&VName=PQD
ProQuest document ID:1543908481


 

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