Abstract
Cryogenic air separation (CAS) is the leading technology for large scale production of pure N2, O2 and Ar. This process is very electric-energy intensive; thus it is a likely candidate for load balancing of power stations in a smart grid. This type of intermittent operation of CAS, requires a non-linear model based control to achieve optimal techno-economic performance. Accordingly, this work presents a computationally efficient and novel approach for solving a tray-by-tray equilibrium model and its implementation for open-loop optimal-control of a cryogenic distillation column. Here, the optimisation objective is to reduce the cost of compression in a volatile electricity market while meeting the production requirements, i.e. product flow rate and purity. This model is implemented in Matlab and uses the ThermoLib rigorous thermodynamic library. The present work represents a first step towards plant-wide dynamic modelling and smart control of a cryogenic distillation plant.
| Original language | English |
|---|---|
| Title of host publication | Proceedings of the 27th European Symposium on Computer Aided Process Engineering – ESCAPE 27 |
| Volume | 40 |
| Publisher | Elsevier |
| Publication date | 2017 |
| Pages | 1543-1548 |
| DOIs | |
| Publication status | Published - 2017 |
| Event | 27th European Symposium on Computer Aided Process Engineering - Barcelona, Spain Duration: 1 Oct 2017 → 5 Oct 2017 Conference number: 27 https://www.elsevier.com/books/27th-european-symposium-on-computer-aided-process-engineering/espuna/978-0-444-63965-3 |
Conference
| Conference | 27th European Symposium on Computer Aided Process Engineering |
|---|---|
| Number | 27 |
| Country/Territory | Spain |
| City | Barcelona |
| Period | 01/10/2017 → 05/10/2017 |
| Internet address |
| Series | Computer Aided Chemical Engineering |
|---|---|
| Volume | 40 |
| ISSN | 1570-7946 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Cryogenic air separation
- Load balancing
- Distillation column
- Dynamic modeling
- Optimal-control
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