The study focuses on enhancing hydrogen production rates through passive flow disturbance in methanol steam reformation processes. By analyzing fuel conversion, carbon monoxide concentration, and hydrogen yield in reactor designs with and without flow disturbers, the research aims to optimize industrial hydrogen production. Results show that the implementation of flow disturbers significantly reduces CO levels while increasing hydrogen yield, with reactors achieving up to 9.6 kg/day of hydrogen output. The experiment, conducted over a temperature range, highlights the importance of thermal management and catalysis in efficient hydrogen generation. Past studies on methanol steam reforming underline the benefits of using methanol due to its lower reforming temperature and high hydrogen-to-carbon ratio. The paper also addresses the challenges associated with heat transfer, mass transfer, and chemical kinetics in steam reforming and proposes flow disturbance as a solution to mitigate these limitations. The findings suggest that flow disturbers help spread and mix axial flows, reducing thermal gradients and improving reactor performance. Moreover, the study emphasizes the necessity of minimizing CO generation in hydrogen fuel to enhance catalyst longevity and performance in fuel cell systems. By analyzing the relationship between fuel conversion, CO selectivity, and hydrogen yield, the research offers insights into the potential of flow disturbance for CO reduction in methanol steam reformation. Overall, the study contributes to the advancement of sustainable energy production by focusing on efficient hydrogen generation for industrial applications.