Abstract
Poly(oxymethylene) dimethyl ethers (OME) are environmentally benign alternative fuels. This work presents the conceptual design of a novel OME process which employs aqueous solutions of formaldehyde and methanol as feedstock. In this process, OME of the desired chain lengths n = 3-5 and water are separated from the reactive mixture (formaldehyde + water + methanol + methylal + OME). Thermodynamic limits are identified by studying distillation boundaries and chemical equilibria. By that it is shown that OME of chain lengths n = 3-5 can be separated from the reactor outlet by distillation. The separation of water is carried out using either an adsorption or a membrane process. Adsorption isotherms of water on Zeolite 3A are determined experimentally. The OME process is simulated and optimized using a reduced process model accounting for the mass balances and the thermodynamic limits. Favorable operating points of the process are identified using multi-objective optimization.
| Original language | English |
|---|---|
| Pages (from-to) | 11519-11530 |
| Number of pages | 12 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 56 |
| Issue number | 40 |
| DOIs | |
| State | Published - 11 Oct 2017 |
| Externally published | Yes |
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