hydronic loop design
Hydronic loop design for AI data centers
Secondary loop architecture for 100 kW+ racks: pipe sizing, ΔT/ΔP budgets, expansion volume, air separation and commissioning gates.
A hydronic loop for a 100 kW+ rack is a mechanical system where every joint, elbow and valve is a candidate for a leak that kills a million dollars of GPU time. This is the blueprint we use.
Design principles that survive contact with reality
- Constant ΔT beats constant flow. Design pumps to modulate, not to run flat out.
- Every rack drop must be isolatable without taking the row down.
- No mixed metals without dielectric unions. Full stop.
- Air is the enemy. Design in air separators and vent points at every high spot.
- Expansion tanks sized for full ΔT swing plus 10% for coolant makeup.
Pipe and pump sizing
Target velocity 1.5–2.5 m/s in steel risers, under 1.5 m/s in copper drops. Pipe friction losses under 250 Pa/m keep the pump curve honest. Undersized risers are the number-one root cause of ΔP alarms we're called to.
Expansion, makeup and air management
- Bladder-type expansion tank sized for the full 10–40 °C swing.
- Automatic makeup with dedicated de-ionised water skid, isolated by check valve.
- Coalescing air separator at the highest point of the loop.
- Manual vent points at every riser cap.
Controls and setpoints
A modern CDU PLC controls: secondary supply temp (setpoint 35 °C ±0.5), pump VFDs to hold ΔP, flow limits per rack, leak-rope zones, and CDU-to-CDU failover logic. Publish everything to BMS via BACnet/IP or Modbus TCP.
Commissioning gates
- Hydrostatic pressure test at 1.5× MAWP for 4 h.
- Chemical clean and passivation.
- Fill with de-aerated fluid, run air separator 24 h.
- Balance flow to every rack drop within ±5%.
- Load bank test to 110% design load.
- Sign-off leak-detection matrix with facility ops.
Need immediate hydronic support?
Critical leak response, pump diagnostics, and pressure stabilization. Engineers en route in under 4 hours.