Honors Theses

Date of Award

Spring 5-7-2026

Document Type

Undergraduate Thesis

Department

Chemical Engineering

First Advisor

Brenda Prager

Second Advisor

Songtao Xie

Relational Format

Dissertation/Thesis

Abstract

This paper investigates the optimization and dynamic control of acetone production via catalytic dehydrogenation of isopropyl alcohol. Optimization was conducted using steady-state Aspen Plus modeling with product specifications of 30,000 metric tons per year of 99.9% pure acetone by weight. Dynamic modeling of the feed preparation and reaction portions of the process was conducted in Aspen Plus Dynamic. Through optimization efforts the primary economic factor, net present value (NPV), was increased from $(126.6) million to $(83.2) million, representing a $43.4 million increase. This was primarily accomplished through a switch to low temperature catalyst, optimization of reactor dimensions, pressurization of key separation processes, and purification of the hydrogen by-product. Despite the increase in NPV, it was determined that the project would not be successful unless the market price trends of acetone and isopropyl alcohol alter. By the addition of key controllers, the dynamic system was able to appropriately respond to a variety of alterations in process flowrates. However, the process would benefit from more aggressive manual tuning of process feed control, the addition of feedforward control to temperature control cascades, and pump controls.

Creative Commons License

Creative Commons Attribution 4.0 International License
This work is licensed under a Creative Commons Attribution 4.0 International License.

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