Compressed air enters tangentially near one end of a plain cylindrical tube through a nozzle, spinning up into a fast helical vortex with no moving parts. The outer layer of the vortex spirals down the tube toward an adjustable conical valve at the far ("hot") end. Turbulent shear inside the vortex transfers rotational kinetic energy from the inner layers outward to the outer layers, so the inner core loses energy, cools, reverses axial direction, and flows back up the tube's center to exit through a small orifice at the near ("cold") end, coaxial with the inlet.
The valve position sets the cold mass fraction μ = ṁcold/ṁin. Closing it forces more flow out the cold orifice (μ↑); opening it sends more out the hot end (μ↓).
Ideal isentropic expansion drop:
ΔT_s = T_in · [1 − (P_in/P_atm)^(−(γ−1)/γ)], γ = 1.4 (air)
Cold-side temperature drop (empirical vortex-tube
efficiency correlation, peaks near μ ≈ 0.3):
η_c(μ) = η_max·(μ/μ_p)·exp(1 − μ/μ_p)
T_cold = T_in − η_c(μ)·ΔT_s
Hot-side temperature (first-law energy balance,
adiabatic, no external work — exact, not empirical):
μ·T_cold + (1−μ)·T_hot = T_in
T_hot = (T_in − μ·T_cold) / (1 − μ)
- Inlet pressure — sets the isentropic drop ΔT_s available to work with; higher pressure ratio means a bigger possible split.
- Cold fraction μ (valve) — the single strongest lever: the cold stream cools most around μ≈0.3, while the hot stream keeps heating further as μ→0 because less mass carries the same rejected energy.
- Inlet temperature — both outlet temperatures shift with it, since the separation is a fraction of the inlet's absolute temperature.
- Real devices reach 40–60 °C splits from compressed shop air and are used for spot-cooling machining tools, cabinet cooling and gas sampling where a compact, moving-part-free cooler is worth the poor thermodynamic efficiency (~10–15% of a Carnot device).