Analysis of the feasibility of using Invar process pipes in multichannel cryogenic helium transfer lines based on the second law of thermodynamics

Authors

  • Paweł Duda Wroclaw University of Science and Technology, Wybrzeże Stanisława Wyspiańskiego 27, 50-370 Wrocław, Poland
  • Maciej Chorowski Wroclaw University of Science and Technology, Wybrzeże Stanisława Wyspiańskiego 27, 50-370 Wrocław, Poland
  • Ziemowit Malecha Wroclaw University of Science and Technology, Wybrzeże Stanisława Wyspiańskiego 27, 50-370 Wrocław, Poland
  • Jarosław Poliński Wroclaw University of Science and Technology, Wybrzeże Stanisława Wyspiańskiego 27, 50-370 Wrocław, Poland

DOI:

https://doi.org/10.24425/ather.2025.154196

Abstract

This work describes examples of the use of cryogenic lines and their designs, referring in detail to typical structural nodes found in cryogenic transfer lines. As a special case, multichannel cryogenic transfer lines are described, in which the process pipes are made of Invar. This has a significant impact on the number of internal supports and the method of thermal shrinkage compensation, which directly impact into reduced heat input during the transfer of cryogenic media. The second law of thermodynamics and the Gouy-Stodola theorem are discussed from the perspective of their application in optimizing and evaluating heat and mass transfer devices. The next part of the work presents the internal structure of the selected 250 m multichannel cryogenic transfer line. Several variants of the method of supporting process pipes have been presented and compared with the solution using Invar. For each solution, an entropy analysis was carried out in order to select the best design in terms of the entropy generated in the process pipes. From the examples presented, it is proven that entropy minimization method can be used for complex optimization of entire cryogenic distribution systems, as well as their individual components.

References

[1] Deng, B.C., Yang, S.Q., Xie, X.J., Wang, Y.L., Pan, W., Li, Q., & Gong, L.H. (2019). Thermal performance assessment of cryogenic transfer line with support and multilayer insulation for cryogenic fluid. Applied Energy, 250, 895−903. https://doi.org/10.1016/j.apenergy.2019.05.025

[2] Rohan, D., Ghosh, P., & Chowdhury, K. (2011). Application of parallel heat exchangers in helium refrigerators for mitigating effects of pulsed load from fusion devices. Fusion Engineering and Design, 86(4-5), 296−306. https://doi.org/10.1016/j.fusengdes.2011.01.133

[3] Iwamoto, A., Nobutoki, M., Kumaki, T., Higaki, H., Hamaguchi, S., Takahata, K., Imagawa, S., Mito, T., Takada, S., & Nadehara, K. (2017). In-situ calibration method of orifice flow meter equipped in 600 W helium refrigerator/liquefier with variable temperature supplies. Fusion Engineering and Design, 123, 107−110. https://doi.org/10.1016/j.fusengdes.2017.05.045

[4] Benedikt, M., & Zimmermann, F. (2016). Status of the Future Circular Collider Study. 25th Russian Particle Accelerator Conference, TUYMH01. https://doi.org/10.18429/JACoW-RuPAC2016-TUYMH01

[5] Collier, P. (2015). The technical challenges of the Large Hadron Collider. Philosophical Transactions A, 373, 20140044. https://doi.org/10.1098/rsta.2014.0044

[6] Gistau-Baguer, G. (2020). Cryogenic Helium Refrigeration for Middle and Large Powers. Springer. https://doi.org/10.1007/978-3-030-51677-2

[7] Quack, H.H. (1994). Maximum efficiency of helium refrigeration cycles using non-ideal components. Advances in Cryogenic Engineering, 39. https://doi.org/10.1007/978-1-4615-2522-6_148

[8] Van Sciver, S.W. (2012). Helium Cryogenics (1st ed.). Springer. https://doi.org/10.1007/978-1-4419-9979-5

[9] Chorowski, M., Choudhury, A., Datta, T.S., & Polinski, J. (2008). Synthesis of multilayer cryogenic insulation modeling and measurements. AIP Conference Proceedings, 985(1), 1367–1374. https://doi.org/10.1063/1.2908496

[10] Khan, M.N., Ahmad, S., Wang, Z., Hussien, M., Alhuthali, A.M.S., & Ghazwani, H.A. (2024). Flow and heat transfer insights into a chemically reactive micropolar Williamson ternary hybrid nanofluid with cross-diffusion theory. Nanotechnology Reviews, 13(1), 20240081. https://doi.org/10.1515/ntrev-2024-0081

[11] Khan, M.N., Ahmad, S., Wang, Z., Ahammad, N.A., & Elkotb, M.A. (2023). Bioconvective surface-catalyzed Casson hybrid nanofluid flow analysis. Tribology International, 188, 108859. https://doi.org/10.1016/j.triboint.2023.108859

[12] Mohanty, B., Mohanty, S., Mishra, S.R., & Pattnaik, P.K. (2021). Analysis of entropy on peristaltic transport of micropolar nanofluid. European Physical Journal Plus, 136, 1139. https://doi.org/10.1140/epjp/s13360-021-02150-z

[13] Nadeem, S., Ishtiaq, B., Akkurt, N., & Ghazwani, H.A. (2023). Entropy optimized flow of hybrid nanofluid with partial slip boundary effects. International Journal of Modern Physics B, 37(29), 2350252. https://doi.org/10.1142/s0217979223502521

[14] Bejan, A. (1980). Second law analysis in heat transfer. Energy, 5(8-9), 712−732. https://doi.org/10.1016/0360-5442(80)90091-2

[15] Mahmud, S., & Fraser, R.A. (2002). Second law analysis of heat transfer in cylindrical annular space. Exergy, 2(4), 322−329. https://doi.org/10.1016/S1164-0235(02)00078-X

[16] Bejan, A. (1995). Entropy Generation Minimization. CRC Press. https://doi.org/10.1201/9781482239171

[17] Pietsch, M., Rummel, T., Nagel, M., Bosch, H.S.F., & Carovani, F. (2023). Development and installation of multichannel transfer lines at W7-X. Fusion Engineering and Design, 188, 113429. https://doi.org/10.1016/j.fusengdes.2023.113429

[18] Duda, P., Chorowski, M., & Polinski, J. (2017). Impact of parameters on heat leaks in cryogenic lines. Physical Review Accelerators and Beams, 20, 033202. https://doi.org/10.1103/PhysRevAccelBeams.20.033202

[19] Duda, P., Chorowski, M., & Polinski, J. (2020). Entropy analysis of support systems in cryogenic lines. IOP Conf. Series: Materials Science and Engineering, 755, 012065. https://doi.org/10.1088/1757-899X/755/1/012065

[20] Rusiński, E., Chorowski, M., Iluk, A., Fydrych, J., & Malcher, K. (2014). Design of a cryogenic transfer line. Archives of Civil and Mechanical Engineering, 14(2), 231−241. https://doi.org/10.1016/j.acme.2013.11.003

[21] Chuang, P.-S., Chang, S.-H., Chiou, W.-S., Hsiao, F.-Z., Li, H.-C., Liao, W., Lin, T.-F., & Tsai, H. (2016). Development of multi-channel line for NSRRC system. IPAC2016. https://doi.org/10.18429/JACoW-IPAC2016-TUPMB050

[22] Thakkar, A., & Vyas, M.I. (2011). Design & analysis of bellows free cryogenic transfer line. NUiCONE-2011.

[23] Cadwallader, L.C. (2010). Vacuum bellows and cryogenic failure rate estimates. Idaho National Laboratory. https://doi.org/10.2172/983360

[24] Cadwallader, L.C. (1992). Cryogenic system operating review for fusion application. Idaho National Engineering Laboratory. https://doi.org/10.2172/5550141

[25] Kirkconnell, C.S., & Curran, D.G.T. (2002). Thermodynamic optimization of multi-stage cryogenic systems. AIP Conf. Proc., 613(1), 1123−1132. https://doi.org/10.1063/1.1472137

[26] Hånde, R., & Wilhelmsen, Ø. (2019). Minimum entropy generation in cryogenic heat exchanger. International Journal of Hydrogen Energy, 44(29), 15045−15055. https://doi.org/10.1016/j.ijhydene.2019.03.229

Downloads

Published

2025-06-30

How to Cite

Duda, Paweł, et al. “Analysis of the Feasibility of Using Invar Process Pipes in Multichannel Cryogenic Helium Transfer Lines Based on the Second Law of Thermodynamics”. Archives of Thermodynamics, vol. 46, no. 2, June 2025, pp. 5-13, doi:10.24425/ather.2025.154196.

Issue

Section

Articles

Similar Articles

1 2 > >> 

You may also start an advanced similarity search for this article.