Abstract
The purpose of this study was the coupling simulation of the vacuum block of the ethanolamine mixture separation unit to determine the optimal layout of the vacuum creation system. For this, a computational model of the vacuum unit, which was identified by comparing the computational data with the data of an industrial study of vacuum rectification columns, was synthesized in the Unisim Design R461 software package. To determine the required load on the vacuum system, a numerical experiment was carried out, during which it was discovered that the load on the system would be 9600 m3/h. It was proposed to replace individual column vacuum pumps with a single vacuum-generating system (VGS) based on a liquid ring vacuum pump (LRVP). When defining the layout, two possible schemes were considered, the models of which were created in Unisim Design R461. The system layout was determined by matching the characteristics of the system elements with the characteristics of the vacuum columns. A technical and economic comparison of the proposed solutions was carried out and the payback period for capital costs was calculated, which for Scheme 1 was 4.14 years, and for Scheme 2–3.59 years.
Subject
Process Chemistry and Technology,Chemical Engineering (miscellaneous),Bioengineering
Reference34 articles.
1. Kirk-Other. Encyclopedia of Chemical Technology;Edens,1991
2. Analysis and modeling of adiabatic reactor for monoethanolamine selective production
3. Ethanolamines and propanolamines;Frauenkron,2008
4. A new approach to an established product: Cost-efficient production of ethanolamines;Fassler;Sulzer Tech. Rev.,2008
5. Organoboron Ionic Liquids as Extractants for Distillation Process of Binary Ethanol + Water Mixtures
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