Abstract
Replacing fossil technologies with renewable carbon-based technologies is of vital importance for the development of sustainable chemical processes in the future. However, impacts beyond climate change should be carefully evaluated to ensure that this transition to defossilized chemicals is truly sustainable. Here, we develop a framework for sustainable process design that explicitly accounts for the performance attained in the Sustainable Development Goals (SDGs), which is computed using standard life cycle assessment (LCA) metrics alongside the planetary boundaries (PBs) concept. We apply this approach to design a CO 2 hydrogenation to methanol process, where economic and SDGs-based performance are the objectives optimized. We show that the environmentally optimal design reduces the impact on SDG 13 (climate action) substantially relative to the business-as-usual (BAU) fossil counterpart, yet this is done at the expense of worsening other categories. A prospective LCA reveals that such collateral damage will be drastically reduced in the future due to improvements in a range of economic sectors. Overall, this work highlights the need to embrace impacts beyond climate change in process design and the advantages of using hybrid surrogates to expedite the computation of Pareto designs.
| Original language | English |
|---|---|
| Pages (from-to) | 2816–2830 |
| Number of pages | 15 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 64 |
| Issue number | 5 |
| DOIs | |
| Publication status | Published - 5 Feb 2025 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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SDG 12 Responsible Consumption and Production
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SDG 13 Climate Action
Keywords
- Production plant
- Simulation
- Supply chains
- Multiobjective optimization
- Co2
- Tools
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