Heat transfer coefficients of additively manufactured tubes with internal pin fins for supercritical carbon dioxide cycle recuperators. (25th November 2020)

• Record Type: Journal Article
• Authors: Searle, Matthew; Black, Jim; Straub, Doug; Robey, Ed; Yip, Joe; Ramesh, Sridharan; Roy, Arnab; Sabau, Adrian S.; Mollot, Darren
• Is Part Of: Applied thermal engineering. Volume 181(2020)
• Publication Date: 2020-11-25
• Subjects: Supercritical carbon dioxide -- Recuperator -- Enhanced heat transfer -- Additive manufacturing -- Helical pin fins; Heat engineering -- Periodicals; Heating -- Equipment and supplies -- Periodicals; Periodicals; 621.40205
• DOI: 10.1016/j.applthermaleng.2020.116030
• Languages: English
• ISSNs: 1359-4311

Abstract

Highlights: HTC for supercritical CO2 flowing in tubes with internal pin fins were measured. The tube-side conductance increased by 277% relative to the smooth tube. The friction factor increased significantly. A pin fin heat exchanger will require 10% less material than a smooth tube heat exchanger. Both heat exchangers have the same pressure drop and friction factor. Abstract: This paper describes the measurement of convective heat transfer coefficients and friction factors for sCO2 flowing in additively manufactured tubes with internal pin fins at the US DOE's National Energy Technology Laboratory in Morgantown, WV. The measurement procedures were validated by conducting benchmark tests with smooth stainless-steel tube and comparing the results with published correlations for Nusselt number ( Nu ) and friction factor. Over Reynolds numbers ( ReD ) ranging from 5 × 10 4 to 2.5 × 10 5, measured Nu was within 5% of the Dittus-Boelter correlation and measured friction factors were within 5% of the McAdams correlation for smooth tube flow. The candidate pin fin patterned pipes were additively manufactured (AM) at the Oak Ridge National Laboratory. The pins were circular or elliptical in cross-section and were printed at a 30° angle relative to the inner wall (to meet AM constraints). The pin arrangement was helical to promote enhanced heat transfer due to swirl flow. Pin length to diameter aspect ratio was 1.33, 2, and 8, while the pin diameter to tube diameter ratio was 0.188, 0.125, and 0.063. Tests were performed for ReD varying from 6.9 × 10 4 to 2.2 × 10 5 and at conditions equivalent to the low pressure (LP) outlet (8.69 MPa, 361 K) and the high pressure (HP) inlet (20.7 MPa, 350 K) of the low temperature recuperator (LTR) in an indirect sCO2 cycle. The Wilson plot technique was utilized to measure the bulk heat transfer coefficients. For the best performing design (tube A, pin length to tube diameter ratio: 1.33, pin diameter to tube diameter ratio: 0.19), the local heat transfer coefficient increased by 136% relative to the Dittus-Boelter correlation at the LTR low pressure outlet and 194% at the LTR high pressure inlet. These correspond to a 282% and a 271% increase in the product of the heat transfer coefficient and surface area (adjusted for fin efficiency) product, respectively. Large pressure drops across the test articles were observed. For Tube Design A, the average friction factor, across the range of ReD considered, was significantly larger than the McAdams correlation at both the LTR LP outlet and the LTR HP inlet. A thermal performance factor was utilized to express the ratio of material required to build a finned heat exchanger relative to a finless heat exchanger with the same heat duty and pumping power. Tube Design A was estimated to decrease the required heat exchanger material by 13%.