Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration

Several activity tests on a zeolite-based catalyst for the ethanol to ethylene dehydration reaction are used to outline the stoichiometry of 4 reactions describing the observed outcome. The heat and mass balances of a reactor were calculated. The thermal input was mainly sustained with a standard pr...

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Main Authors: I. Rossetti, A. Tripodi, E. Bahadori, G. Ramis
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2018-06-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/2921
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spelling doaj-69c3e0eef8a447c78c7f2bf9ca7149d22021-02-17T21:07:14ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162018-06-016510.3303/CET1865013Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat IntegrationI. RossettiA. TripodiE. BahadoriG. RamisSeveral activity tests on a zeolite-based catalyst for the ethanol to ethylene dehydration reaction are used to outline the stoichiometry of 4 reactions describing the observed outcome. The heat and mass balances of a reactor were calculated. The thermal input was mainly sustained with a standard product-to-feed heat exchange. Upstream, two possible strategies of ethanol-water beer concentration were compared, namely a single stage flash and a small column, yielding respectively a 3:1 water:ethanol mixture and a slightly diluted azeotrope. The external heat input needed for the separation unit, the feed heating up to the reaction temperature and the reaction upkeep are compared. A flow diagram for the hot utility is then designed, converting part of the water of the beer into superheated steam that gives also electric power. The conceptual design of an ethanol to ethylene plant is therefore available to exploit bioethanol solution with different water/ethanol ratios, with different ethanol purification routes with variable heat input and energy recovery.https://www.cetjournal.it/index.php/cet/article/view/2921
collection DOAJ
language English
format Article
sources DOAJ
author I. Rossetti
A. Tripodi
E. Bahadori
G. Ramis
spellingShingle I. Rossetti
A. Tripodi
E. Bahadori
G. Ramis
Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration
Chemical Engineering Transactions
author_facet I. Rossetti
A. Tripodi
E. Bahadori
G. Ramis
author_sort I. Rossetti
title Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration
title_short Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration
title_full Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration
title_fullStr Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration
title_full_unstemmed Exploiting Diluted Bioethanol Solutions for the Production of Ethylene: Preliminary Process Design and Heat Integration
title_sort exploiting diluted bioethanol solutions for the production of ethylene: preliminary process design and heat integration
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2018-06-01
description Several activity tests on a zeolite-based catalyst for the ethanol to ethylene dehydration reaction are used to outline the stoichiometry of 4 reactions describing the observed outcome. The heat and mass balances of a reactor were calculated. The thermal input was mainly sustained with a standard product-to-feed heat exchange. Upstream, two possible strategies of ethanol-water beer concentration were compared, namely a single stage flash and a small column, yielding respectively a 3:1 water:ethanol mixture and a slightly diluted azeotrope. The external heat input needed for the separation unit, the feed heating up to the reaction temperature and the reaction upkeep are compared. A flow diagram for the hot utility is then designed, converting part of the water of the beer into superheated steam that gives also electric power. The conceptual design of an ethanol to ethylene plant is therefore available to exploit bioethanol solution with different water/ethanol ratios, with different ethanol purification routes with variable heat input and energy recovery.
url https://www.cetjournal.it/index.php/cet/article/view/2921
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