Abstract
In this work, a modular millireactor (MMR) is designed and modeled using the computational fluid dynamics (CFD) tool OpenFOAM. First, the method is validated against a conventional packed bed reactor (PBR) model (1D) with Aspen Plus. Next, the method is applied to study the effects of pressure (2–6 MPa) and temperature (483–533 K) on the performance of the MMR. Conjugate heat transfer (CHT) CFD results for the MMR are compared against a corresponding PBR at isothermal conditions. For the MMR, the methanol yield is shown to vary between 9–23 % within the studied parameter range. Overall, the MMR outperforms the PBR at conditions studied in this work. The maximum difference in methanol yield between MMR and the PBR is noted to be a factor of 1.71 at 533 K and 5 MPa. Such a large discrepancy advocates the usage of 3D CHT/CFD.
| Original language | English |
|---|---|
| Article number | 117765 |
| Journal | Chemical Engineering Science |
| Volume | 258 |
| DOIs | |
| Publication status | Published - 31 Aug 2022 |
| MoE publication type | A1 Journal article-refereed |
Funding
The authors acknowledge the Academy of Finland for the support of this research through Grant Nos. 318024, 332835, 333069, and profiling funding 5 for Energy Storage with Grant No. 326346. Business Finland is acknowledged for the main financial support (grant 8797/31/2019) of the P2XEnable project (p2xenable.fi). The project partners are also thanked for their financial contributions.
Keywords
- Aspen Plus
- CO hydrogenation
- Methanol synthesis
- Modular millireactor
- OpenFOAM