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HVAC — From the Chiller Plant to the Diffuser

A component-by-component reference for the central chilled-water system of a super-tall tower. We follow the cooling from its source — the chiller plant — through every device, pipe and duct, to the last grille in a hotel room. Each component gives you: what it is, how to design it, a worked numeric example, how to do it in the software, and the governing code.

The system chain — what we are following

A central chilled-water HVAC system is one long energy path. Cooling is made at the chiller, carried by water up the tower, transferred to air at the AHU/FCU, and delivered to the room through a diffuser — while heat is rejected outside through cooling towers (or to a district-cooling plant). This module walks that whole path.

Chillerplant CHWpumps Risers + HX(zoning) AHU /FCU Ducts+ VAV Roomgrille Coolingtowers / DC heat rejected outside Cooling is made → pumped → zoned up the tower → transferred to air → delivered to the room
Figure 1-0 · The HVAC chain we follow in this module. Each box is a section below. (Original schematic.)
How each component section is laid out
Role (what it does) → Design parametersDesign method & formulaWorked numeric exampleIn the software (what to enter for accurate results) → Code reference.
Constants, symbols & conversions used in the worked examples

Every number in the calculations below comes either from the example's "Given" line or from one of these fixed physical constants/conversions:

Symbol / constantValueWhat it is & where it comes from
QThe cooling load (kW) — taken from the cooling-load calc (1.2) or the example's Given.
ṁ (m-dot)Mass flow rate (kg/s) — what we solve for.
cp (water)4.187 kJ/kg·KSpecific heat of water — fixed property; energy to raise 1 kg of water by 1 °C.
cp (air)1.005 kJ/kg·KSpecific heat of air — fixed property.
ρ (water / air)1000 / 1.2 kg/m³Density — fixed property.
g9.81 m/s²Gravity — fixed constant (pump-power formula).
η (eta)0.65–0.80Pump/fan efficiency (decimal) — from the example's Given or manufacturer data.
ΔT(per Given)Temperature difference (°C = K for a difference) — a design choice in the Given.
1 TR= 3.517 kWTon of refrigeration → kW conversion.
1 MW= 1000 kWSo 3.06 MW = 3,060 kW (this is where the "3,060" comes from).
Water flow1 kg/s ≈ 1 L/sBecause water ρ ≈ 1000 kg/m³, so kg/s and L/s are practically equal.

Key formulas: heat carried by water/air Q = ṁ · cp · ΔT · pump power P = ρ · g · Q · H ÷ η · fan power P = Q · Δp ÷ η

1.1 Start with the design criteria (Basis of Design)

Nothing is sized until the criteria are fixed. These are the agreed inputs every later calculation depends on.

CriterionTypical value (hot-climate tall building)Source
Outdoor design (summer)≈ 40–42 °C DB / 28–30 °C WB (0.4% annual)ASHRAE Climatic Design Data / SBC 601
Indoor designHotel room 23 °C / 50% RH; office 24 °C / 50%; lobby 24 °CASHRAE 55, SBC 501
Fresh-air ratePer ASHRAE 62.1 (e.g. hotel room ≈ 2.5 L/s·person + 0.3 L/s·m²)ASHRAE 62.1
CHW temperaturesSupply 6 °C, return 13 °C (ΔT = 7 °C)Design choice (high ΔT for tall buildings)
Diversity factor0.80–0.90 on summed peak loadsASHRAE / engineering judgement
Key takeaway
Garbage in, garbage out: the outdoor/indoor conditions, fresh-air rates and ΔT you fix here propagate through every downstream component. Lock them in the Basis of Design and get client sign-off before sizing.

1.2 Cooling-load calculation — the starting number (Carrier HAP)

Role: the cooling load is the heat (kW / TR) each space, zone and the whole building needs removed at peak. Every chiller, pump, pipe, AHU and duct is sized from it. We compute it space-by-space, then aggregate with diversity.

Design method

Modern practice uses a dynamic method (ASHRAE Radiant Time Series / Heat Balance) rather than hand calculation, because solar and thermal mass shift the peak through the day. The load is the sum of: solar through glazing, conduction through envelope, infiltration, people, lighting, equipment, and the fresh-air (ventilation) load.

Qspace = Qsolar + Qenvelope + Qinfiltration + Qpeople + Qlights + Qequipment

Worked example 1.2 · One hotel guestroom

Given: room 4 m × 7 m = 28 m²; one exterior glazed wall 4 m × 3.2 m = 12.8 m², glass SHGC 0.25, U 1.8 W/m²K; peak solar on west glass ≈ 500 W/m²; 2 occupants; lighting 8 W/m²; equipment 150 W; outdoor 40 °C, room 23 °C; fresh air 2 × 2.5 + 0.3 × 28 = 13.4 L/s.
Solar: 12.8 × 500 × 0.25 = 1,600 W
Glass conduction: 12.8 × 1.8 × (40−23) = 392 W
People: 2 × (75 sens + 55 lat) = 260 W
Lighting: 8 × 28 = 224 W; Equipment = 150 W → 374 W
Fresh-air load (approx, total): ≈ ṁ·Δh. Air ṁ = 13.4 L/s × 1.2 = 16.1 g/s; enthalpy drop ~40 kJ/kg (hot humid → room) → 0.0161 × 40 = 644 W
Room peak ≈ 1,600 + 392 + 260 + 374 + 644 ≈ 3,270 W ≈ 3.3 kW (0.93 TR). Intensity ≈ 117 W/m² — consistent with the 120 W/m² rule used for a quick floor estimate.
In Carrier HAP — to get an accurate load
  1. Weather: select the project's design-city weather file (or enter the 0.4% DB/WB from ASHRAE climatic design data). Set the correct design months — peak for west rooms is afternoon, for east is morning.
  2. Spaces: create one space per room type; enter floor area, wall/glass areas by orientation (critical — HAP applies the right solar profile per façade), U-values and SHGC from the façade spec.
  3. Internals: set people density, activity, lighting W/m² and equipment W/m² with realistic schedules (hotel rooms are not 100% occupied at the building peak).
  4. Ventilation: enter the ASHRAE 62.1 rates; let HAP compute the fresh-air coil load.
  5. Systems & Plant: assign spaces to air systems, then air systems to a plant. Run the "Design" simulation — read the coil load (for AHU/FCU sizing) and the block/plant load with diversity (for chiller sizing). Do not just add space peaks — use HAP's coincident block load.
Accuracy traps: wrong orientation, unrealistic 100% schedules (oversizes plant), and ignoring diversity (oversizes chillers, hurts part-load efficiency).
Code
Method: ASHRAE Handbook—Fundamentals (RTS/HB). Ventilation: ASHRAE 62.1. Envelope limits feeding U/SHGC: SBC 601 / ASHRAE 90.1.
loadCHILLERrejectionpumpsrisersAHUductroom

1.3 Chillers — the source of cooling

Role: a chiller is a refrigeration machine that produces chilled water (≈6 °C) by absorbing heat from the return water and rejecting it to the condenser side. It is the "source" we follow everything back to.

Types & selection

TypeDriveUse
Water-cooled centrifugalElectric, very efficientLarge towers / central plant (most common)
Air-cooled screwElectric, no cooling towerSmaller / where no condenser water
AbsorptionHeat-drivenWhere waste heat / district energy available

Design method — number & size

Total plant capacity = block load ÷ diversity. Split into multiple chillers for part-load efficiency and redundancy (N+1). Each chiller's evaporator flow comes from Q = ṁ·cₚ·ΔT.

Worked example 1.3 · Chiller plant for a zone

Given: summed space peaks for a stack of floors = 14.4 MW; diversity 0.85; CHW ΔT = 7 °C.
Plant load = 14.4 × 0.85 = 12.24 MW = 12,240 ÷ 3.517 = 3,480 TR.
Select 4 working + 1 standby (N+1) → each = 12.24 / 4 = 3.06 MW (≈ 870 TR) chillers, 5 installed.
Evaporator flow per chiller — rearrange Q = ṁ·cp·ΔT to ṁ = Q ÷ (cp × ΔT):
ṁ = 3,060 kW ÷ (4.187 kJ/kg·K × 7 K) = 104 kg/s ≈ 104 L/s
where 3,060 = one chiller's load (3.06 MW × 1,000 = 3,060 kW); 4.187 = specific heat of water; 7 = the chosen ΔT (°C) from the criteria; and for water 1 kg/s ≈ 1 L/s.
5 × ~870 TR water-cooled centrifugal chillers (4 duty + 1 standby), ~104 L/s evaporator flow each. Staging them matches the part-load profile and protects efficiency (see IPLV below).
Water-cooled centrifugal chiller — efficiency vs part load (IPLV)
kW per ton of refrigeration (lower is better) across the load range. Centrifugal chillers are most efficient near part load — which is why several smaller machines are staged. Set the operating load and machine size to read the input power and the efficiency penalty versus the best point.
Fraction of the machine's rated capacity it is running at right now.
Nameplate cooling capacity of one machine (1 TR = 3.517 kW).
Efficiency at load
0.50 kW/TR
Cooling delivered
750 TR
Input power
375 kW
vs best point
IPLV curve with your operating point marked; kW/TR is interpolated between the 25/50/75/100% rating points. Centrifugal chillers bottom out near 50% load.
In the software
Take the block load from HAP as plant capacity. Select actual machines in the manufacturer's selection software (e.g. Carrier ECAT, Trane Select Assist, York) — enter CHW supply/return temps, condenser water temps and fouling to get the certified AHRI 550/590 kW/TR and IPLV. Confirm the part-load (IPLV) meets ASHRAE 90.1 / SBC 601 minimums.
Code
Performance rating: AHRI 550/590. Min efficiency: ASHRAE 90.1 / SBC 601. Refrigerant & machinery room safety: ASHRAE 15 & 34, SBC 501.
loadchillerHEAT REJECTIONpumpsrisersAHUductroom

1.4 Heat rejection — cooling towers (or district cooling)

Role: the heat the chiller absorbs plus the compressor's own work must be dumped outside. Water-cooled plants do this through cooling towers, which reject heat by evaporating a little water. On many Saudi giga-projects the tower instead takes district cooling — then "heat rejection" happens off-site and the building only has an energy-transfer station (plate HX) at the intake.

Design method

Heat rejected ≈ chiller load × (1 + 1/COP). Cooling-tower performance is set by range (condenser water ΔT) and approach (how close the cold water gets to the outdoor wet-bulb).

Worked example 1.4 · Heat rejection & make-up water

Given: chiller evaporator load 3,060 kW, COP = 6.0, condenser ΔT (range) = 5 °C, design wet-bulb 30 °C, approach 4 °C → cold water 34 °C.
Heat rejected = chiller load + the compressor's own work = Q × (1 + 1/COP):
Qcond = 3,060 kW × (1 + 1/6) = 3,570 kW
where 3,060 kW = the chiller's cooling load and 6 = its COP (efficiency); 1/6 adds the compressor heat.
Condenser-water flow: ṁ = 3,570 ÷ (4.187 × 5) = 170 L/s per chiller.
Evaporation make-up ≈ 0.8 × Qcond ÷ 2,400 kJ/kg = 0.8 × 3,570 / 2,400 = 1.19 kg/s ≈ 1.2 L/s (≈ 4.3 m³/h) per chiller, plus drift & blowdown (total make-up ≈ 1.5–2× evaporation).
~3,570 kW rejected, ~170 L/s condenser water, ~1.2 L/s evaporative make-up per chiller. In a district-cooling scheme these towers are off-site; the tower just sizes the intake HX for 12.24 MW.
In the software
Select towers in the manufacturer tool (e.g. Baltimore Aircraft/BAC, Marley) by entering flow, range and design wet-bulb → it returns the cell size/fan power. Water-balance (evaporation, drift, blowdown, cycles of concentration) is a manufacturer/CTI calc. For a district-cooling interface, size the plate HX in the vendor tool (e.g. Alfa Laval) for the building load and approach.
Code
Cooling-tower thermal rating: CTI ATC-105. Legionella control of open condenser water: ASHRAE 188. Make-up water & reuse: NWC / local authority.
chillerrejectionCW PUMPSCHW pumpsrisersroom

1.5 Condenser-water pumps

Role: circulate water between chiller condensers and the cooling towers. Sized on the condenser flow (1.4) and the head around that loop (tower static lift + pipe + condenser + spray nozzles).

Worked example 1.5 · Condenser pump power

Given: flow Q = 170 L/s = 0.170 m³/s; loop head H = 22 m; pump efficiency η = 0.80.
Hydraulic power: P = ρ·g·Q·H ÷ η = 1000 × 9.81 × 0.170 × 22 ÷ 0.80
P = 45,800 W ≈ 45.8 kW shaft → motor next size up (≈ 55 kW)
~46 kW per condenser pump; select a 55 kW motor. Use one pump per chiller (headered) for redundancy.
In the software
Compute the loop head in AFT Fathom (or a spreadsheet) from pipe lengths, fittings, condenser ΔP (from chiller data) and tower nozzle pressure. Take Q + H into Grundfos/Armstrong/Wilo selection software → it gives the exact pump curve, motor kW, NPSH required and efficiency. Verify the duty point sits near best-efficiency point (BEP).
Code
Pump energy limits: ASHRAE 90.1 / SBC 601. NPSH margin per HI (Hydraulic Institute) standards.

1.6 Chilled-water pumps (primary / secondary)

Role: push chilled water from the chillers out to the coils. Modern plants use primary–secondary (constant primary through chillers, variable secondary to the building) or variable-primary flow. Secondary pumps have VFDs and modulate to keep a remote differential-pressure set-point — saving large pumping energy at part load.

Worked example 1.6 · Secondary CHW pump for a zone

Given: zone load 3,060 kW, ΔT 7 °C → Q = 3,060 ÷ (4.187 × 7) = 104 L/s = 0.104 m³/s; design head H = 32 m (coil + control valve + pipe + HX); η = 0.78.
P = 1000 × 9.81 × 0.104 × 32 ÷ 0.78 = 41,800 W ≈ 41.8 kW
With a VFD, at 80% flow the affinity laws give power ≈ 0.8³ = 0.51 → ~21 kW. Huge part-load saving.
~42 kW duty; specify VFD + remote DP control. Stage multiple pumps (N+1). Affinity-law savings are the main reason variable secondary flow is mandatory on tall buildings.
In the software
Get system head from AFT Fathom (it builds the system curve); pick the pump in the manufacturer selector; model VFD part-load with the affinity laws. In HAP, set the plant pumping type (primary-secondary / variable-primary) so energy results are realistic.
Code
Variable-flow & pump power: ASHRAE 90.1 / SBC 601. Affinity laws: pump theory (ASHRAE Fundamentals).
pumpsRISERS + ZONINGpipe sizingAHUroom

1.7 Vertical distribution & zoning (heat-exchanger floors)

Role: carry chilled water up ~1 km without the static pressure crushing the equipment. As in Module 0, the riser is broken into stacked low-pressure loops by plate heat exchangers on plant floors — cooling passes up, pressure resets.

ParameterGuide
Zone height~15–25 floors so static pressure stays within pipe/valve PN rating
HX approach~1 °C (a tight approach needs more plate area — a cost trade-off)
Pressure ratingLow zones may need PN16/PN25; deepest risers sometimes PN40 fittings
Each HX step costs ~1 °C
Every heat-exchanger break warms the water slightly, so the chillers must make water a touch colder for the top zones. Account for the cumulative approach when setting the chiller leaving-water temperature.
In the software
Model the whole vertical network in AFT Fathom — it shows the static + dynamic pressure at every node so you can confirm each zone stays within its PN rating and place HX floors correctly. For surge on tall CHW risers (pump trip), check transients in Bentley HAMMER / AFT Impulse.
Code
Pressure ratings: pipe/fitting PN class (ISO/EN/ASME B31.9 building services piping). Insulation: ASHRAE 90.1 / SBC 601.

1.8 Pipe sizing & material

Role: deliver the flow at acceptable velocity and friction. Pipes are sized by velocity limits (noise, erosion) and friction-rate limits (pump energy).

A = Q ÷ v   →   d = √(4A ÷ π)

ServiceVelocityFriction rate
CHW mains2.0–3.0 m/s~100–250 Pa/m
CHW branches1.0–2.0 m/s

Worked example 1.8 · Size the zone CHW main

Given: Q = 104 L/s = 0.104 m³/s; target velocity v = 2.5 m/s.
A = 0.104 ÷ 2.5 = 0.0416 m²; d = √(4×0.0416 ÷ π) = 0.230 m.
Select DN250 (next standard size up); check actual velocity = 0.104 ÷ (π/4 × 0.25²) = 2.12 m/s and friction ≈ 150 Pa/m. Material: black steel (ASTM A53) to ASME B31.9, insulated with vapour barrier.
In the software
In Revit MEP, set the pipe system's sizing method to "velocity + friction" with these limits and use Size Pipe; Revit picks sizes from the loaded pipe schedule. Validate the full network ΔP and pump head in AFT Fathom (Revit sizes, AFT proves the hydraulics & pump duty).
Code
Building-services piping: ASME B31.9. Velocity/friction guidance: ASHRAE Fundamentals, CIBSE Guide C. Insulation: SBC 601 / ASHRAE 90.1.

1.9 Valves, balancing & accessories

Between pump and coil sit the devices that control and protect the loop. Size each — never just "match the pipe."

  • 2-way control valves (modulate flow to coils) — sized by Kv/Cv, not pipe size, for good authority.
  • Balancing valves / PICVs (pressure-independent control valves) — set each terminal's design flow.
  • Isolation valves, check valves, strainers, automatic air vents.
  • Expansion tank — absorbs water's thermal expansion; sized on system volume and temperature swing.

Worked example 1.9 · Control-valve sizing (Kv)

Given: AHU coil flow Q = 6 m³/h; desired valve pressure drop Δp = 0.3 bar (for good authority ≥ coil ΔP).
Kv = Q ÷ √Δp = 6 ÷ √0.3 = 6 ÷ 0.548 = 10.96 m³/h/bar^½
Select the valve with Kv ≥ 11 (next standard, e.g. Kv 12). Confirm valve authority β = Δpvalve/Δpbranch ≥ 0.3 so control is stable.
In the software
Use the valve manufacturer's sizing tool (Belimo, Danfoss) — enter flow and design ΔP, it returns Kv, authority and the actuator. PICVs are auto-selected by design flow. Schedule them in Revit.
Code
Valve sizing & authority: CIBSE / BSRIA commissioning guides. Materials: project spec / SBC 501.
risersAHUductVAVroom

1.10 Air-handling units — where water becomes cold air

Role: the AHU mixes return + fresh air, cools/dehumidifies it across the CHW coil, filters it, and a fan delivers it to the ducts. Sized on airflow (from the sensible load) and the coil load (total).

SectionDesign parameter
Cooling coilFace velocity ≤ ~2.5 m/s (avoid moisture carry-over); 4–8 rows
Supply fanAirflow + total static pressure (duct + coil + filter + terminals)
FiltersISO 16890 ePM grade; clean+dirty ΔP in fan static
Mixing boxFresh/return ratio per ASHRAE 62.1

Worked example 1.10 · AHU for a floor

Given: floor sensible load 84 kW; supply air 14 °C, room 24 °C (ΔT 10 °C); air ρ 1.2, cₚ 1.005.
Airflow: ṁ = 84 ÷ (1.005 × 10) = 8.36 kg/s → 6.97 m³/s ≈ 7.0 m³/s (25,200 m³/h).
Coil face area at 2.5 m/s: A = 7.0 ÷ 2.5 = 2.8 m².
Fan power at total static 1,000 Pa, η 0.65: P = Q·Δp ÷ η = 7.0 × 1000 ÷ 0.65 = 10.8 kW.
~7 m³/s AHU, ~2.8 m² coil face, ~11 kW fan. Coil CHW flow: 84 ÷ (4.187 × 7) = 2.87 L/s.
In the software
Take coil load + airflow from HAP. Select the AHU in the manufacturer tool (Daikin, Trane, AHRI-certified) — enter airflow, entering/leaving air conditions, CHW temps; it sizes coil rows, face area, fan and gives the certified ΔP and sound power. Verify fan power vs ASHRAE 90.1 fan-power limits. Place the AHU + connect in Revit.
Code
AHU rating: AHRI 430 / EN 1886 & 13053. Ventilation: ASHRAE 62.1. Fan power: ASHRAE 90.1 / SBC 601. Filters: ISO 16890.

1.11 Ductwork — sizing & distribution

Role: carry conditioned air from AHU to the terminals at low noise and low fan energy. Sized by the equal-friction or static-regain method.

DuctVelocityFriction
Main / riser6–8 m/s~0.8–1.0 Pa/m
Branch3–5 m/s(equal-friction)
Final run-out2–3 m/s(low noise)

Worked example 1.11 · Main supply duct

Given: Q = 7.0 m³/s; main velocity v = 7 m/s.
A = 7.0 ÷ 7 = 1.0 m² → rectangular ≈ 1,250 × 800 mm (or Ø1,130 mm round).
1.0 m² main; reduce size down the run to hold equal friction. Construction & gauges per SMACNA; leakage class per DW/144 / SMACNA.
In the software
In Revit MEP, set the duct system sizing to Equal Friction (e.g. 1 Pa/m) with velocity caps, then Size Duct. Use the ASHRAE Duct Fitting Database for fitting loss coefficients to compute the index-run static pressure that feeds the AHU fan selection. Cross-check noise (NC) at terminals.
Code
Construction/leakage: SMACNA HVAC Duct Construction Standards. Fire/smoke dampers: NFPA 90A, SBC 801. Sizing: ASHRAE Fundamentals.

1.12 VAV boxes & dampers

Role: a Variable-Air-Volume box throttles airflow to each zone to match its changing load, while the AHU fan rides a VFD. Dampers (volume, fire, smoke) control and protect airflow paths.

Worked example 1.12 · VAV box turndown

Given: zone max airflow 0.6 m³/s at peak; ASHRAE 62.1 minimum ventilation needs 0.18 m³/s.
Turndown = 0.18 ÷ 0.6 = 30% → select a box whose minimum setpoint can hold 30% accurately (size the box so 0.6 m³/s is mid-range, not its max).
Pick the VAV size where design flow sits comfortably in range and the 30% minimum is controllable; specify the controller + reheat if needed.
In the software
Select VAV boxes in the manufacturer tool (Titus, Trox) by max/min airflow and inlet size, reading the radiated/discharge NC. Schedule and tag in Revit; map setpoints into the BMS points list.
Code
Minimum ventilation at min flow: ASHRAE 62.1. Fire/smoke dampers: NFPA 90A / SBC 801.

1.13 Fan-coil units (guestrooms & apartments)

Role: a small local unit (CHW coil + fan) that conditions one room. Hotels and apartments use FCUs for individual control, with a separate fresh-air supply (often pre-treated by a dedicated outdoor-air AHU).

Worked example 1.13 · FCU selection

Given: guestroom total load 3.3 kW (from 1.2), of which sensible ≈ 2.6 kW; CHW 6/13 °C.
Select an FCU whose total capacity ≥ 3.3 kW and sensible ≥ 2.6 kW at the design entering-air and CHW conditions — pick the speed tap that meets it at acceptable NC (≤ NC 30 for a bedroom).
FCU CHW flow: 3.3 ÷ (4.187 × 7) = 0.11 L/s; fit a PICV set to that flow.
Choose the FCU size meeting both total & sensible at design conditions and noise limit; fresh air delivered separately to meet ASHRAE 62.1.
In the software
Use the FCU manufacturer selector (Daikin, Zehnder) — enter room entering-air temp/RH, CHW temps and required total+sensible; it returns the model, speed, water flow, ΔP and sound. Don't select on total capacity alone — the sensible capacity at your entering conditions is what controls the room.
Code
FCU rating: AHRI 440 / EN 1397. Ventilation: ASHRAE 62.1. Sound: NC limits (ASHRAE Applications).
AHUductVAV/FCUROOM DIFFUSER

1.14 The last piece — room diffusers & grilles

Role: the air terminal that delivers conditioned air into the occupied space with the right throw (how far the jet reaches), good mixing, and low noise (NC). This is the very end of the chain the occupant actually feels.

ParameterGuide
Neck velocity2–4 m/s (noise & throw)
ThrowReach to ~75% of the way to the next diffuser / wall for good mixing
NC≤ 30 bedroom, ≤ 35 office, ≤ 40 lobby

Worked example 1.14 · Diffuser selection

Given: room supply airflow 0.10 m³/s (100 L/s); ceiling height 2.7 m; want 4-way throw, NC ≤ 30.
At neck velocity 3 m/s, neck area = 0.10 ÷ 3 = 0.033 m² → ~Ø205 mm neck or a 300×300 face diffuser.
From the catalogue at 100 L/s, that diffuser gives throw ≈ 2.0–2.5 m and NC ≈ 25 .
Select 300×300 (Ø200 neck) 4-way ceiling diffuser at 100 L/s: throw ~2.3 m, NC 25 — comfortable, draught-free, quiet.
In the software
Use the diffuser manufacturer selector (Titus, Trox, Krueger) — enter airflow, mounting height and room size; it returns throw, pressure drop and NC for each model. Lay them out in Revit on a ceiling grid; check throws overlap for even coverage.
Code
Terminal performance: ASHRAE 70 (testing) & ISO 5219. Comfort/draught: ASHRAE 55. Sound: NC criteria (ASHRAE Applications).

1.15 Controls & BMS — making it all behave

Role: sensors, controllers and control valves/dampers run the system to setpoint and report to the Building Management System. The chain ends not at the diffuser but at the room thermostat that tells the FCU/VAV and ultimately the chiller plant how hard to work.

  • Field sensors: room temp/RH, duct temp, CHW supply/return temp & flow, differential pressure, CO₂ (demand-controlled ventilation).
  • Control loops (PID): room thermostat → modulates FCU valve / VAV damper; AHU supply-air-temp loop → modulates coil valve; secondary pump → holds remote DP.
  • Plant optimisation: chiller staging, CHW reset, condenser-water reset, optimum start/stop.
  • Protocol: BACnet (ISO 16484-5) over IP, integrated to the head-end and to fire (for smoke control).
In the software
Document the points list and control sequences (often in a controls package / BMS configuration tool from Siemens, Honeywell, JCI). Demand-controlled ventilation uses CO₂ to trim fresh air (ASHRAE 62.1 allows it). Energy impact of resets is best proven in the HAP energy model.
Code
BMS/interoperability: ISO 16484 (BACnet). Economiser/DCV/resets: ASHRAE 90.1 & 62.1 / SBC 601. Fire interface: NFPA 72 cause & effect.

1.16 Smoke control & stair pressurisation

Role: in a fire, keep escape routes and firefighting lifts smoke-free using fans and pressurisation — the HVAC engineer's life-safety duty. Stair/lobby pressurisation also counters the stack effect.

Worked example 1.16 · Stair pressurisation airflow (concept)

Given: pressurised stair, target +50 Pa vs floor; leakage area of closed doors/cracks per floor ≈ 0.02 m²; flow through a leak ṁ ∝ A·√(2ΔP/ρ).
Leak velocity at 50 Pa: v = √(2×50/1.2) = 9.1 m/s; flow per leak = 0.02 × 9.1 = 0.18 m³/s; with several doors open during escape, total can reach several m³/s — sized by the NFPA 92 design fire scenario, not a single number.
Pressurisation fan sized to hold +50 Pa with a defined number of doors open and to limit door-opening force — confirmed by modelling, not a hand calc.
In the software
Model stair/lobby pressurisation and smoke movement in CONTAM (NIST) — it includes the stack effect over the full height and computes the fan airflow to hold the design pressure with doors open. Coordinate the cause-and-effect with the fire-alarm matrix.
Code
Smoke control: NFPA 92. Life safety/egress: NFPA 101. Under SBC 801 & Saudi Civil Defense approval. Alarm interface: NFPA 72.

1.17 Testing, adjusting, balancing & commissioning

Design is only proven when the installed system is balanced (TAB) and commissioned: every terminal set to its design flow, every control sequence verified, and the whole plant integrated and witnessed. On a tower this is staged zone-by-zone as floors are released.

  • TAB: set water flows at PICVs/balancing valves and air flows at terminals to the design schedule.
  • Commissioning: verify sequences (chiller staging, resets, smoke control), alarms, and integrated fire cause-and-effect with Civil Defense witnessing.
Code
Commissioning: ASHRAE Guideline 0 & Standard 202; TAB per AABC/NEBB. Smoke-control acceptance test: NFPA 92.
central system+DECENTRALISED / PACKAGED SYSTEMS

1.18 Packaged, split & VRF systems — when central CHW isn't used

Not every space is on the central chilled-water plant. Standalone areas — retail, podium, back-of-house, security/electrical/IT rooms, tenant fit-outs, areas that must run 24/7 independent of the main plant — use decentralised (direct-expansion, DX) systems. A complete HVAC design specifies these too.

SYSTEM A — PACKAGED / ROOFTOP UNITS (RTU)

Role: a self-contained DX unit (compressor, condenser, evaporator, fan, filters) in one casing — typically on a roof or podium — supplying ducted air to a block of spaces. Common for retail, podium and amenity areas.

Worked example 1.18a · Packaged unit selection

Given: retail block load 30 kW total (8.5 TR); ducted distribution.
Supply airflow ≈ 0.045–0.055 m³/s per kW (sensible-led) → 30 × 0.05 = 1.5 m³/s (5,400 m³/h).
Pick a packaged DX unit ≥ 30 kW total at the design ambient (40–46 °C), giving ≥ 1.5 m³/s at an external static of ~200 Pa for the ductwork.
Select a packaged DX unit rated at the local high ambient (capacity drops as outdoor temp rises — always read capacity at site design ambient, not nominal 35 °C).
SYSTEM B — SPLIT SYSTEMS

Role: an indoor unit + a remote outdoor condensing unit linked by refrigerant pipes. Forms: high-wall, 4-way ceiling cassette, floor-standing, and concealed ducted (mid-static) which hides above a ceiling and feeds short ducts to grilles (good for hotel suites/apartments/small offices). Single-zone, simple, independent.

Limit to checkWhy
Max refrigerant pipe length & height between indoor/outdoorCapacity & oil return; manufacturer limits (e.g. ~30–50 m / 15–30 m lift)
Outdoor-unit location & heat rejectionNeeds clear airflow; clustering on a tall façade is a design problem
Don't cool critical rooms on a single split
Electrical / IT / telecom rooms need redundancy (N+1) and 24/7 duty — use two units on auto-changeover or precision AC, not one comfort split.
SYSTEM C — VRF / VRV (VARIABLE REFRIGERANT FLOW)

Role: one (or more) outdoor unit serves many indoor units on a shared refrigerant circuit, modulating compressor speed; heat-recovery versions move heat from rooms that need cooling to rooms that need heat. Excellent for offices/hotels with diverse, part-load-heavy loads. Branch (BC) controllers distribute refrigerant.

Worked example 1.18c · Refrigerant concentration safety check (the design trap people miss)

Given: a VRF circuit total charge 20 kg of R-410A; the smallest room it serves has volume 30 m³. Refrigerant concentration limit (RCL) for R-410A ≈ 0.44 kg/m³.
If the whole charge leaked into that room: 20 ÷ 30 = 0.67 kg/m³ > 0.44 → exceeds the safe limit.
Mitigate per ASHRAE 15 / ISO 817 / EN 378: reduce circuit charge, increase room volume, add a leak-detection + mechanical-ventilation interlock, or split the circuit. Always run this check for VRF in small occupied rooms.
In the software
Design VRF in the manufacturer tool (Daikin VRV Xpress, Mitsubishi Diamond System Builder, etc.) — it sizes pipes/branch controllers, applies correction factors for pipe length & height, derates for ambient, and runs the refrigerant-concentration check. Model the system energy in HAP (it has VRF/DX system types).
SYSTEM D — DEDICATED OUTDOOR-AIR SYSTEM (DOAS) & ENERGY RECOVERY

Role: decouples ventilation from cooling — a central unit pre-treats only the fresh outdoor air (cooling + deep dehumidification, often via an energy-recovery wheel/plate that pre-cools incoming air with exhaust), and delivers neutral, dry air to spaces served by FCUs/VRF. In humid climates DOAS is the clean way to handle the big latent load and guarantee ventilation.

Why DOAS matters in humid climates
FCUs and VRF are poor at deep dehumidification. A DOAS dries the fresh air centrally so terminal units only handle sensible room load — better humidity control and comfort.
SYSTEM E — PRECISION / CLOSE-CONTROL AC (CRAC / CRAH)

Role: high-sensible, tight-tolerance cooling for data centres, telecom/IT and major electrical rooms — DX (CRAC) or chilled-water (CRAH). High sensible heat ratio, controlled RH, and N+1 redundancy with 24/7 duty and standby power. Often the most critical HVAC in the building.

Code (decentralised systems)
DX equipment rating: AHRI 210/240 (small), 340/360 (large); refrigerant safety: ASHRAE 15 & 34, ISO 817, EN 378; min efficiency: ASHRAE 90.1 / SBC 601; ventilation still per ASHRAE 62.1. Data-centre cooling guidance: ASHRAE TC 9.9.

1.19 Installation, accessories & field tricks

A correct calculation still fails if the system is badly installed. These are the accessories every design must show and the field practices that make systems quiet, reliable and maintainable — the knowledge that separates a drawing from a working system.

Water-side accessories & detailing

AccessoryPurposeField rule / trick
Pipe hangers & supportsCarry weight, control sagSpacing per pipe size/material (MSS SP-58); support at changes of direction & valves; never hang one pipe off another.
Anchors, guides & expansion loops/bellowsAbsorb thermal movementCHW & hot pipes grow with temperature; place loops/bellows between fixed anchors so risers don't buckle.
Vibration isolators + inertia basesStop equipment vibration entering structureSpring isolators under chillers/pumps/AHUs; size deflection to equipment rpm.
Flexible pipe connectorsIsolate pump/chiller vibration from pipeFit at every rotating-equipment connection.
Strainers (Y / basket)Protect pumps & control valves from debrisAlways upstream of pumps & valves; flush at commissioning (temporary fine mesh, then remove).
Air & dirt separators, auto air ventsRemove entrained air/dirtAir vents at every high point or the system air-locks; separator near the chillers.
Expansion tank / pressurisation unitAbsorb water expansion, hold fill pressureSize on system volume × expansion at max ΔT; set fill pressure so the top of the system stays positive.
Isolation & drain valves, unions/flangesMaintenanceValve + union around every device so it can be removed without draining the riser; drains at every low point.
Gauges, thermometers, test points (P/T plugs)Verify & commissionAt pump suction/discharge, coil in/out, chiller in/out — you can't balance what you can't read.
Insulation + vapour barrierStop heat gain & condensationCHW must be fully vapour-sealed or it drips into ceilings; protect riser insulation mechanically.
Pipe sleeves + fire-stoppingPenetrations through rated walls/slabsUse a tested/UL-listed firestop system at every fire-rated penetration; escutcheons at finished surfaces.

Air-side accessories & detailing

AccessoryPurposeField rule / trick
Volume / balancing dampersSet branch airflowPlace with straight duct upstream for stable, readable flow; not right at a diffuser neck.
Turning vanes in elbowsCut pressure loss & noiseSquare elbows need vanes; or use radiused bends.
Fire & smoke dampersMaintain fire/smoke compartmentationAt every rated-barrier crossing; provide an access door at each (NFPA 90A / SBC 801).
Access doors/panelsClean & service dampers/coilsCoordinate with ceiling access tiles — a damper you can't reach is useless.
Flexible duct connectors at fans/AHUIsolate vibration & noiseShort canvas connector at AHU discharge/return.
Flexible duct (final run-outs)Connect diffusersKeep ≤ ~1.5 m, pulled taut, no kinks — sloppy flex destroys airflow & adds noise.
Acoustic lining / silencers (attenuators)Meet NC limitsAdd attenuators near AHU & cross-talk silencers between rooms sharing a duct.
Duct sealing (leakage class)Stop wasted air/energySeal to SMACNA leakage class; leaky ducts blow the fan power budget.

Worked example 1.19 · Condensate drain trap depth (a classic field failure)

Given: a draw-through AHU/FCU; negative static at the drain pan = 250 Pa. Condensate must drain out against that suction or the pan overflows.
250 Pa ≈ 250 ÷ 9.81 = 25.5 mm water gauge.
Rule: trap seal (water leg) ≥ the negative static, plus margin → ≈ 1.5× → trap seal ≈ 40 mm, total trap height ≈ 75–100 mm; slope the drain line ≥ 1%.
Build a deep-enough P-trap (and prime it at commissioning). Too-shallow traps get sucked dry, the pan overflows, and you get a ceiling leak blamed on the pipework. Add a secondary drain pan under ceiling-void FCUs.

Equipment, clearances & restraint

  • Maintenance clearances: leave chiller tube-pull length, AHU access-section space, and pump/coil removal room — show them on the drawings, not just the kit.
  • Housekeeping pads & drip trays under all plant; bunds where needed.
  • Seismic / wind restraint of equipment, pipes and ducts at height (SBC 301; SMACNA seismic & MSS guidance) — critical in tall buildings.
  • Refrigerant pipework (splits/VRF): braze under flowing nitrogen, fit oil traps on long suction risers, pressure-test & vacuum-dehydrate, and charge per actual pipe length.
In the software
Most accessories are shown on Revit details & schedules and on coordinated sections (clash-checked in Navisworks). Hanger spacing & seismic bracing follow MSS SP-58 / SMACNA tables. Commissioning & balancing procedures follow BSRIA / CIBSE Commissioning Codes and AABC/NEBB.
Code
Pipe supports: MSS SP-58. Duct construction & seismic: SMACNA. Fire-stopping penetrations: UL-listed firestop systems / NFPA 101 & SBC 801. Vibration & acoustics: ASHRAE Applications. Commissioning: ASHRAE Guideline 0; BSRIA/CIBSE.

Terms & abbreviations

Plain-English meaning of the HVAC terms used in this module.

TermWhat it means (plain English)
HVACHeating, Ventilation & Air Conditioning.
Cooling loadThe rate of heat (kW or TR) that must be removed to keep a space at its design temperature.
TR (ton of refrigeration)A unit of cooling power; 1 TR = 3.517 kW.
Sensible vs latent heatSensible = heat that changes temperature; latent = heat tied up in moisture (humidity). Coils remove both.
EnthalpyTotal heat content of air (sensible + latent), in kJ/kg.
PsychrometricsThe science of air + moisture — how temperature and humidity change as we condition air.
Dry-bulb / wet-bulbDry-bulb = ordinary air temperature; wet-bulb = temperature accounting for evaporation (relates to humidity).
RH (relative humidity)How "full" the air is with moisture, as a % of its maximum at that temperature.
ΔT (delta-T)A temperature difference — e.g. between chilled-water supply and return.
CHWChilled Water — the cold water (≈6 °C) that carries cooling around the building.
COP / IPLVCOP = efficiency (cooling out ÷ power in); IPLV = a weighted efficiency over part-load operation.
AHU / FCUAir-Handling Unit (big central air unit) / Fan-Coil Unit (small local room unit).
VAVVariable-Air-Volume box — throttles airflow to a zone to match its load.
DOASDedicated Outdoor-Air System — treats only the fresh air, often with energy recovery.
VRF / VRVVariable Refrigerant Flow — one outdoor unit serving many indoor units via refrigerant.
DXDirect Expansion — cooling made by refrigerant in the unit itself (splits, packaged units).
RTU / CRACRooftop (packaged) Unit / Computer-Room Air Conditioner (precision cooling for IT rooms).
Heat exchanger (HX)A device that passes heat between two fluids without mixing them (used to break tall CHW risers into zones).
SHGC / U-valueSHGC = fraction of solar heat passing through glass; U-value = how easily heat conducts through a wall/glass (lower = better).
ESP / face velocityESP = external static pressure a fan must overcome (ductwork); face velocity = air speed across a coil.
Kv / CvA valve's flow coefficient — used to size control valves (not just match the pipe).
NC (noise criteria)A rating of how quiet a space is; lower NC = quieter (e.g. NC 30 for a bedroom).
PICVPressure-Independent Control Valve — holds a set flow regardless of pressure swings.
Smoke control / pressurisationUsing fans to keep stairs & lobbies free of smoke in a fire.

References & software map

TaskSoftwareGoverning code/standard
Cooling/heating load & energyCarrier HAP (or Trane TRACE 3D Plus)ASHRAE Fundamentals; ASHRAE 90.1 / SBC 601; 62.1
Chiller / AHU / FCU / tower / pump / valve / diffuser selectionManufacturer selection tools (Carrier ECAT, Daikin, BAC, Grundfos, Belimo, Titus…)AHRI 550/590, 430, 440; CTI ATC-105; ISO 16890
Pipe & duct modelling/sizing & coordinationRevit MEP + NavisworksASME B31.9; SMACNA; ASHRAE Duct Fitting DB
CHW/CW network hydraulics & surgeAFT Fathom; Bentley HAMMER / AFT ImpulseHydraulic Institute; ASHRAE
Smoke control / stack effectCONTAM (NIST)NFPA 92 / 101; SBC 801
  • ASHRAE Handbook — Fundamentals, HVAC Systems & Equipment, HVAC Applications.
  • ASHRAE Standards 90.1, 62.1, 55, 15 & 34, 70, 202, Guideline 0.
  • SBC 501 (Mechanical), SBC 601 (Energy), SBC 801 (Fire) — 2018.
  • NFPA 90A, 92, 101, 72 (editions as referenced by SBC 801).
  • SMACNA HVAC Duct Construction; AHRI & AHRI-certified rating standards; CTI ATC-105; CIBSE Guides B & C.
Note
Worked numbers are realistic teaching values to show the method — not stamped project calculations. Confirm code editions/clauses against the live SBC and the project specification, and select real equipment in the manufacturers' certified software.
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