Xuan Linh Nguyen

Mr. Xuan Linh Nguyen


Research Focus & Metrics

Academic Career Length

9Years (2018-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 October 2021 in International Journal of Heat and Mass Transfer
Verified
Journal Article
Closed access
HVHoang Nghia Vu
Hoang Nghia Vu
XNXuan Linh Nguyen
Xuan Linh Nguyen
JHJaeyoung Han
Jaeyoung Han
SYSangseok Yu
Sangseok Yu

1 February 2018 in Diabetes Technology & Therapeutics
Verified
Journal Article
Open access
RCRudolf Chlup
Rudolf Chlup
SRSarah Runzis
Sarah Runzis
JCJavier Castaneda
Javier Castaneda
SLScott W. Lee
Scott W. Lee
XNXuan Linh Nguyen
Xuan Linh Nguyen
OCOhad Cohen
Ohad Cohen
Background: This prospective single-center study recruited insulin-resistant continuous subcutaneous insulin infusion (CSII) therapy-naive patients with type 2 diabetes (T2D) using insulin analog-based multiple daily injections (MDI) therapy and metformin. Methods: A total of 23 individuals with T2D (70% male), aged a mean ± standard deviation 57.2 ± 8.03 years, with body mass index of 36.2 ± 7.02 kg/m2, diabetes duration of 13.3 ± 4.64 years, and HbA1c of 10.0% ± 1.05% were randomly assigned to a CSII arm or an MDI continuation arm to explore glucose control, weight loss, total daily insulin dose (TDD), and insulin resistance. Insulin dosing was optimized over a 2-month run-in period. Results: At 6 months, patients assigned to the CSII arm achieved a significant mean HbA1c reduction of −0.9% (95% confidence interval [CI] = −1.6, −0.1), while reducing their TDD by −29.8 ± 28.41 U/day (33% of baseline [92.1 ± 20.35 U/day]) and achieving body mass (BM) reduction of −0.8 ± 5.61 kg (0.98% of baseline [104.8 ± 16.15 kg]). MDI patients demonstrated a nonsignificant HbA1c reduction of −0.3% (95% CI = −0.8, 0.1) with a TDD reduction of 5% from baseline (99.0 ± 25.25 U/day to 94.3 ± 21.25 U/day), and a BM reduction of −1.0 ± 2.03 kg (0.99% of baseline [108.9 ± 20.55 kg]). After 6 months, the MDI arm crossed over to CSII therapy. At 12 months, patients continuing CSII demonstrated an additional mean 0.7% HbA1c reduction with 54.6% achieving HbA1c<8%. The final TDD reduction was −9.7 U/day in comparison to baseline; BM increased by 1.1 ± 6.5 kg from baseline. The MDI patients that crossed to CSII showed an HbA1c reduction of −0.5% ± 1.04%, HbA1c response rate of 27.3%, a TDD reduction of −17.4 ± 21.06 U/day, and a BM reduction of −0.3 ± 3.39 kg. Diabetic ketoacidosis or severe hypoglycemia did not occur in either arm. Conclusion: CSII therapy safely and significantly improved metabolic control with less insulin usage, with no sustainable reduction of BM, blood pressure, and lipid profile, in insulin-resistant T2D patients. Treatment adherence and satisfaction in these patients were excellent.

1 November 2021 in Renewable Energy
Verified
Journal Article
Closed access
XNXuan Linh Nguyen
Xuan Linh Nguyen
HVHoang Nghia Vu
Hoang Nghia Vu
SYSangseok Yu
Sangseok Yu

28 April 2022 in International Journal of Hydrogen Energy
Verified
Journal Article
Closed access
XNXuan Linh Nguyen
Xuan Linh Nguyen
HVHoang Nghia Vu
Hoang Nghia Vu
YKYounghyeon Kim
Younghyeon Kim
SYSangseok Yu
Sangseok Yu

14 March 2022 in Energies
Verified
Journal Article
Open access
PDF file
HVHoang Nghia Vu
Hoang Nghia Vu
XNXuan Linh Nguyen
Xuan Linh Nguyen
SYSangseok Yu
Sangseok Yu
Maintaining the performance of a fuel cell stack requires appropriate management of water in the membrane electrode. One solution is to apply an external humidifier to the supply gases. However, the operating conditions change continuously, which significantly affects the humidifier performance and supply gas characteristics. A straightforward humidifier module is needed for integration with the fuel cell system model. In this study, a lumped-mass model was used to simulate a hollow-fiber membrane humidifier and investigate the effects of various input conditions on the humidifier performance. The lumped-mass model can account for heat transfer and vapor transport in the membrane bundle without losing simplicity. The humidifier module was divided into three parts: a heat and mass exchanger in the middle and two manifolds at the ends of the exchanger. These components were modeled separately and linked to each other according to the flow characteristics. Simulations were performed to determine the humidifier response under both steady-state and transient conditions, and water saturation was observed in the outlet manifold that may affect the humidifier performance. The findings on the effects of the operating conditions and humidifier dimensions on the cathode gas can be used to improve humidifier design and control.