Approximately 70% of the energy consumed in the U.S. manufacturing sector is dedicated to process heating (Brueske et al., 2012) contributing to 32% of the emissions from the industrial sector (Cresko et al., 2022). With the increasing availability of renewable electricity, heat pumps present a promising alternative by enabling the work-driven upgrading of low-grade heat, thereby reducing emissions associated with conventional process heating (Thiel & Stark, 2021).
However, sequential optimization of unit operations and heat pump networks can lead to markedly sub-optimal solutions. For instance, optimizing parameters such as conversion rates in reactors, the recovery of components during separation processes, or the pressures of unit operations can be crucial for fostering effective heat pumping, thereby reducing emissions. Most prior formulations neglect variations in stream composition and pressure by altering operating conditions, limiting effective integration of electrified heating technologies (Onishi et al., 2014; Razib et al., 2012).
In our research, we investigate the integration of heat pump technology within multi-component distillation systems. Exergy analysis has been widely used in distillation studies to identify thermodynamically efficient designs that minimize second-law losses (Jiang et al., 2019; Tumbalam Gooty et al., 2023). In this study, we examine the conditions under which exergy optimization leads to designs that achieve minimum energy consumption when operated with a heat pump. A key advantage of the exergy methodology is its ability to identify designs compatible with heat pump integrated systems without the need for explicit network modeling. This approach enables the decomposition of unit operations, such as distillation, from the heat pump network, facilitating more efficient system design.
We further benchmark this approach against a simultaneous optimization model that explicitly includes heat pump network design. Results show that, under certain conditions - such as matched thermal qualities of feed and products - exergy optimization alone can yield designs that minimize heat pump work, enabling efficient electrified process heating.
References:
Brueske, S., Sabouni, R., Zach, C., & Andres, H. (2012). U.S. Manufacturing Energy Use and Greenhouse Gas Emissions Analysis. https://www.energy.gov/eere/amo/articles/us-manufacturing-energy-use-an…
Cresko, J., Thekdi, A., Nimbalkar, S., Thirumaran, K., Hasanbeigi, A., & Chaudhari, S. (2022). Thermal Process Intensification: Transforming the Way Industry Uses Thermal Process Energy.
Jiang, Z., Chen, Z., Huff, J., Shenvi, A. A., Tawarmalani, M., & Agrawal, R. (2019). Global minimization of total exergy loss of multicomponent distillation configurations. AIChE Journal, 65(11). https://doi.org/10.1002/aic.16737
Onishi, V. C., Ravagnani, M. A. S. S., & Caballero, J. A. (2014). Simultaneous synthesis of work exchange networks with heat integration. Chemical Engineering Science, 112, 87–107. https://doi.org/10.1016/J.CES.2014.03.018
Razib, M. S., Hasan, M. M. F., & Karimi, I. A. (2012). Preliminary synthesis of work exchange networks. Computers & Chemical Engineering, 37, 262–277. https://doi.org/10.1016/J.COMPCHEMENG.2011.09.007
Thiel, G. P., & Stark, A. K. (2021). To decarbonize industry, we must decarbonize heat. Joule, 5(3), 531–550. https://doi.org/10.1016/J.JOULE.2020.12.007
Tumbalam Gooty, R., Mathew, T. J., Tawarmalani, M., & Agrawal, R. (2023). An MINLP formulation to identify thermodynamically-efficient distillation configurations. Computers and Chemical Engineering, 178. https://doi.org/10.1016/j.compchemeng.2023.108369