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Tool 9: Hydronics & Central Chiller Plant

Chilled Water Pipe Sizing & Hazen-Williams Engine

Sizes Schedule 40 carbon steel / GI chilled water supply and return headers using the Hazen-Williams formulation ($C=120$). Enforces ASHRAE 90.1 dual screening criteria for maximum velocity ($\le 8.5\text{ FPS}$) and head loss rate ($\le 4.0\text{ ft / 100 ft}$).

✔ 1. Formula Verified → ⚡ 2. Engineering Screening → 📐 3. Standards Referenced (ASHRAE 90.1 / Hazen-Williams) → ⚖ 4. Engineer Review Required
💧 Chilled Water System Parameters
TR (Tons of Refrig.)
Design cooling capacity in Tons of Refrigeration (1 TR = 12,000 BTU/hr = 3.516 kW).
°F
Supply vs Return water temperature difference (Default: 10°F e.g. 44°F supply / 54°F return, 5.56°C).
📊 Sizing Calculation Sheet
ASHRAE 90.1 OPTIMAL
Recommended Schedule 40 Commercial Pipe Size
150mm (6") Schedule 40
Internal Diameter: 6.065 in (154.1 mm) | Carbon Steel / Heavy GI
Design Flow Rate (Q)
360.0 GPM
22.71 L/s (81.76 m³/h)
Actual Fluid Velocity
4.00 FPS
1.22 m/s • Limit ≤ 8.5 FPS
Frictional Head Loss (hf)
1.09 ft / 100 ft
0.107 bar / 100m • Limit ≤ 4.0
Dual Pass Verification
Pass Both Checks
Velocity & Head Loss OK
💬 Consult Chilled Water Engineer on WhatsApp

Governing Engineering Standards & Calculation Model (Hazen-Williams & ASHRAE 90.1)

1. Thermodynamic Water Flow Rate Equation

Based on the specific heat of chilled water ($1.0 \text{ BTU/lb}\cdot^\circ\text{F}$) and standard density ($8.33 \text{ lb/gal}$):

Q (GPM) = [ Capacity (TR) × 12,000 BTU/hr ] / [ 500 × ΔT (°F) ]
Q (GPM) = (Capacity × 24.0) / ΔT
Flow (L/s) = Q × 0.06309
Flow (m³/h) = Q × 0.2271

2. Hazen-Williams US Customary Frictional Head Loss

The head loss per 100 feet of pipe is determined using the Hazen-Williams empirical equation with roughness coefficient C = 120 (standard commercial schedule 40 mild steel and galvanized pipe in closed hydronic loops):

h_f = 0.2083 × (100 / C)^1.852 × [ Q^1.852 / d_i^4.8655 ] (ft head loss per 100 ft)
Velocity V = (0.408 × Q) / (d_i)² (FPS)

Where Q is fluid flow in US Gallons per Minute (GPM) and d_i is actual inside diameter in inches.

⚖ Statutory Notice & Engineering Disclaimer (Tier D Integration)

This calculation provides preliminary engineering screening and pipe diameter selection for initial spatial layout, shaft clearance, and pumping preliminary estimates. Detailed hydraulic distribution networks require dynamic balancing valve calculations, 3D piping thermal expansion loop analysis per ASME B31.9, chiller evaporator minimum flow rate validation, and hydraulic network simulation verified by a licensed mechanical engineer.