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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AIDIC Servizi S.r.l.
2018-10-01
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Series: | Chemical Engineering Transactions |
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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 |
work_keys_str_mv |
AT niklasschmitz conceptualdesignofanovelprocessfortheproductionofomefuels AT christianbreitkreuz conceptualdesignofanovelprocessfortheproductionofomefuels AT eckhardstrofer conceptualdesignofanovelprocessfortheproductionofomefuels AT jakobburger conceptualdesignofanovelprocessfortheproductionofomefuels AT hanshasse conceptualdesignofanovelprocessfortheproductionofomefuels |
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