Conceptual Design of a Novel Process for the Production of OME Fuels

Poly(oxymethylene) dimethyl ethers (OME) are oxygenates of the general structure H3C-O-(CH2O)n-CH3 with n = 2. OME are synthetic diesel fuels, which strongly reduce the soot formation and indirectly also the NOx formation in diesel engines. This work presents the conceptual design of a novel OME pro...

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Main Authors: Niklas Schmitz, Christian Breitkreuz, Eckhard Strofer, Jakob Burger, Hans Hasse
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2018-10-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/9159
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spelling doaj-15c6cb4035354ae0b78f906ba3a8f34e2021-02-16T21:19:11ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162018-10-016910.3303/CET1869036Conceptual Design of a Novel Process for the Production of OME FuelsNiklas SchmitzChristian BreitkreuzEckhard StroferJakob BurgerHans HassePoly(oxymethylene) dimethyl ethers (OME) are oxygenates of the general structure H3C-O-(CH2O)n-CH3 with n = 2. OME are synthetic diesel fuels, which strongly reduce the soot formation and indirectly also the NOx formation in diesel engines. This work presents the conceptual design of a novel OME process, which employs aqueous solutions of formaldehyde and methanol as feedstock. Process-relevant data on physico-chemical properties are determined experimentally and models for their description are developed. This includes describing the chemical equilibrium and the vapor-liquid-liquid equilibrium in the system (formaldehyde + water + methanol + methylal + OME). The models are used for determining thermodynamic limits of the process like chemical equilibria and distillation boundaries. Based on that knowledge the novel OME process is designed. It consists of a reactor, two distillation columns, and a pervaporation unit. The first column is a reactive distillation in which OME with n = 3 are separated from a complex reactive multicomponent mixture with more than 30 components. All critical units, including the reactive distillation and the pervaporation are tested in lab-scale experiments. The column profiles of the distillation experiments are well described by simulations using the equilibrium-stage model.https://www.cetjournal.it/index.php/cet/article/view/9159
collection DOAJ
language English
format Article
sources DOAJ
author Niklas Schmitz
Christian Breitkreuz
Eckhard Strofer
Jakob Burger
Hans Hasse
spellingShingle Niklas Schmitz
Christian Breitkreuz
Eckhard Strofer
Jakob Burger
Hans Hasse
Conceptual Design of a Novel Process for the Production of OME Fuels
Chemical Engineering Transactions
author_facet Niklas Schmitz
Christian Breitkreuz
Eckhard Strofer
Jakob Burger
Hans Hasse
author_sort Niklas Schmitz
title Conceptual Design of a Novel Process for the Production of OME Fuels
title_short Conceptual Design of a Novel Process for the Production of OME Fuels
title_full Conceptual Design of a Novel Process for the Production of OME Fuels
title_fullStr Conceptual Design of a Novel Process for the Production of OME Fuels
title_full_unstemmed Conceptual Design of a Novel Process for the Production of OME Fuels
title_sort conceptual design of a novel process for the production of ome fuels
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2018-10-01
description Poly(oxymethylene) dimethyl ethers (OME) are oxygenates of the general structure H3C-O-(CH2O)n-CH3 with n = 2. OME are synthetic diesel fuels, which strongly reduce the soot formation and indirectly also the NOx formation in diesel engines. This work presents the conceptual design of a novel OME process, which employs aqueous solutions of formaldehyde and methanol as feedstock. Process-relevant data on physico-chemical properties are determined experimentally and models for their description are developed. This includes describing the chemical equilibrium and the vapor-liquid-liquid equilibrium in the system (formaldehyde + water + methanol + methylal + OME). The models are used for determining thermodynamic limits of the process like chemical equilibria and distillation boundaries. Based on that knowledge the novel OME process is designed. It consists of a reactor, two distillation columns, and a pervaporation unit. The first column is a reactive distillation in which OME with n = 3 are separated from a complex reactive multicomponent mixture with more than 30 components. All critical units, including the reactive distillation and the pervaporation are tested in lab-scale experiments. The column profiles of the distillation experiments are well described by simulations using the equilibrium-stage model.
url https://www.cetjournal.it/index.php/cet/article/view/9159
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AT eckhardstrofer conceptualdesignofanovelprocessfortheproductionofomefuels
AT jakobburger conceptualdesignofanovelprocessfortheproductionofomefuels
AT hanshasse conceptualdesignofanovelprocessfortheproductionofomefuels
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