Ladtboy Tube -

| Parameter | Range | Increment | |-----------|-------|-----------| | Helical amplitude α | 0.05 – 0.15 | 0.025 | | Number of turns N | 2 – 8 | 2 | | Outer sheath thickness t_o | 0.5 mm – 2 mm | 0.5 mm | | Porosity gradient (φ_out – φ_in) | 0.10 – 0.25 | 0.05 |

Correspondence: [your.email@university.edu] A new tubular geometry, termed the Ladtboy Tube (LBT) , is presented for applications requiring sustained laminar flow at elevated Reynolds numbers while minimizing pressure drop and wall shear stress. The LBT combines a helical corrugated inner wall with a graded‑porosity outer sheath, enabling passive suppression of secondary vortices and enhanced momentum diffusion. Computational Fluid Dynamics (CFD) simulations (Re = 10⁴–10⁶) reveal up to a 45 % reduction in friction factor relative to conventional smooth circular pipes of equal hydraulic diameter, and a 30 % increase in volumetric throughput for a fixed pressure budget. Experimental validation in a 3‑m‑long prototype demonstrates repeatable performance across a range of Newtonian and non‑Newtonian fluids. Potential applications include high‑speed chemical reactors, biomedical micro‑circulatory devices, and aerospace fuel delivery systems. ladtboy tube

¹Department of Mechanical Engineering, University of X ²Institute for Microfluidic Technologies, Y Research Center ³Department of Applied Physics, Z University \endaligned ] The Ladtboy Tube: A Novel Low‑Loss,

[ \beginaligned \nabla \cdot \mathbfu &= 0,\ \rho \left( \frac\partial \mathbfu\partial t + \mathbfu\cdot\nabla\mathbfu \right) &= -\nabla p + \mu \nabla^2\mathbfu. \endaligned ] [Co‑author Name]³ Ladtboy Tube

The Ladtboy Tube: A Novel Low‑Loss, High‑Throughput Tubular Architecture for Laminar‑Dominated Fluid Transport Authors: [Your Name]¹, [Co‑author Name]², [Co‑author Name]³

Ladtboy Tube, laminar flow enhancement, low‑loss transport, helical corrugation, graded porosity, CFD, experimental validation 1. Introduction Efficient fluid transport is a cornerstone of numerous engineering systems, from petrochemical pipelines to micro‑fluidic biomedical platforms. Classical pipe designs, while mature, encounter a fundamental trade‑off: increasing flow rate typically incurs higher pressure losses, especially when operating near the laminar–turbulent transition (Re ≈ 2 000 for smooth circular pipes). Recent research has pursued passive flow‑control strategies —such as surface riblets, helical inserts, and porous liners—to delay transition and reduce drag without active actuation (see Table 1).