Electrical & Logic | Module 105

Low-Temp Chilled Water Freeze-Point Tracking

Field Status: Low-load conditions on chiller plants pose severe operational risk. When a plant operates at minimum capacity, fluid velocity within the evaporator barrel drops significantly, paving the way for rapid localized ice formation and catastrophic shell-and-tube expansion failures.

A closed-loop system must maintain a precision fluid profile to counter sensory drift or flow stagnation. Introducing inhibitors like Ethylene or Propylene glycol lowers the freezing point of the working fluid, creating a mandatory safety buffer beneath your minimum operational temperature targets.

SYS AUDIT: Fluid Freeze Vector
CALCULATED FREEZE POINT:
THERMAL BUFFER:
AUDIT RESULTS:

The Phase Boundary Law

According to the laws of solution thermodynamics, adding a solute lowers the solvent’s chemical potential, directly depressing its freezing point. If the mixture is left too lean, pure water crystals drop out of the solution first at the tube boundaries, raising the local viscosity until flow stalls entirely. This local boundary breakdown causes cascading heat transfer failure and rapid tube stress structural cracking.

Concentration Level Freezing Threshold (°F) Application Profile
0% (Pure Water) 32.0°F High risk. Restricted to standard comfort cooling with strict low-limit safeties.
20% Glycol Mix 14.0°F Standard safety profile for commercial loops prone to moderate ambient load drops.
30% Glycol Mix 5.0°F Heavy industrial process cooling and permanent low-temp loop installations.
40% Glycol Mix -4.0°F Sub-zero storage, heavy industrial processing, and extreme ambient exposure zones.

Diagnostic Gateway Challenge

A process chiller has a leaving water setpoint of 36°F. The field test shows a 15% glycol mixture. Given that a 15% mix provides a 18.5°F freezing point, should you authorize low-load operation?

Request Professional Audit

CONTACT SUPPORT