Condensation Analysis
Condensation Analysis
Condensation occurs when moist air contacts surfaces below the dewpoint temperature or when vapor pressure exceeds saturation pressure within building assemblies. Condensation analysis predicts moisture accumulation locations, quantifies condensation rates, and verifies adequate drying potential to prevent long-term moisture damage.
Dewpoint Temperature Fundamentals
The dewpoint temperature Td represents the temperature at which air becomes saturated (100% RH) at constant pressure. When surfaces drop below dewpoint, water vapor condenses on those surfaces.
Dewpoint Calculation Methods
Method 1: Psychrometric Chart Read dewpoint directly from chart at intersection of dry-bulb temperature and relative humidity lines.
Method 2: Magnus-Tetens Formula (accurate for -40°C to 50°C):
Td = (b × α(T,RH))/(a - α(T,RH))
where:
α(T,RH) = (a × T)/(b + T) + ln(RH/100)
a = 17.27
b = 237.7°C (for Td in °C)
For T in °F:
a = 17.27
b = 427.86°F
Method 3: Partial Vapor Pressure Approach:
First, calculate partial vapor pressure:
pv = RH × psat(T)
Then find dewpoint from inverse saturation equation:
Td = C2/(ln(C1/pv) + C3)
where:
C1 = 0.0866 (imperial units, psi)
C2 = 4030.18
C3 = 235
Example Dewpoint Calculation
Interior conditions: 70°F, 40% RH
Step 1: Find saturation pressure at 70°F
psat(70°F) = 0.3631 psi (from steam tables)
Step 2: Calculate partial vapor pressure
pv = 0.40 × 0.3631 = 0.1452 psi
Step 3: Calculate dewpoint
Td = 4030.18/(ln(0.0866/0.1452) + 235)
Td = 4030.18/(−0.517 + 235) = 17.2°C = 45.0°F
Any surface below 45°F experiences condensation with these interior conditions.
Surface Condensation
Surface condensation occurs on interior surfaces when surface temperature falls below dewpoint. High humidity, cold outdoor temperatures, and poor insulation create condensation risk.
Surface Temperature Calculation
Interior surface temperature follows from heat transfer analysis:
Tsi = Ti - Q × Rsi
where:
Tsi = interior surface temperature (°F)
Ti = interior air temperature (°F)
Q = heat flux through assembly (Btu/hr·ft²)
Rsi = interior surface resistance (typically 0.68 hr·ft²·°F/Btu)
Heat flux through assembly:
Q = (Ti - To)/(Rtotal)
where:
To = outdoor temperature (°F)
Rtotal = total assembly R-value including surface resistances
Combining equations:
Tsi = Ti - ((Ti - To)/(Rtotal)) × Rsi
Tsi = Ti - (Ti - To) × (Rsi/Rtotal)
Condensation Risk Factor
Temperature ratio TR quantifies condensation risk:
TR = (Tsi - To)/(Ti - To)
Higher TR indicates better performance (warmer interior surface)
TR > 0.70 generally prevents condensation for typical interior conditions
Example Surface Condensation Analysis
Wall assembly:
- R-value: R-20 total (includes Rsi = 0.68, Rso = 0.17)
- Interior: 70°F, 40% RH (dewpoint = 45°F)
- Exterior: 10°F
Tsi = 70 - (70 - 10) × (0.68/20)
Tsi = 70 - 60 × 0.034 = 67.96°F
Surface temperature (67.96°F) exceeds dewpoint (45°F) - no condensation occurs.
For poorly insulated wall (R-5):
Tsi = 70 - (70 - 10) × (0.68/5)
Tsi = 70 - 8.16 = 61.84°F
Still no condensation, but closer to dewpoint with less safety margin.
Thermal Bridge Condensation
Thermal bridges (studs, joists, shelf angles) locally reduce R-value, creating cold spots prone to condensation. 2D/3D heat transfer analysis or infrared thermography identifies bridge locations.
Temperature at thermal bridge:
Tbridge = Ti - (Ti - To) × (Rsi/Rbridge)
where Rbridge accounts for reduced insulation at framing member
Steel studs create severe thermal bridges (R-value ≈ R-5 at stud vs. R-20 at cavity), requiring thermal breaks or exterior insulation.
Interstitial Condensation
Interstitial condensation occurs within building assemblies when vapor pressure exceeds saturation pressure at a given temperature plane. This hidden condensation accumulates in insulation cavities, degrading thermal performance and causing material decay.
Temperature Profile Calculation
Temperature distribution through multilayer assembly follows from thermal resistance ratio:
T(x) = Ti - (Ti - To) × (ΣR(x)/Rtotal)
where:
T(x) = temperature at position x
ΣR(x) = cumulative R-value from interior to position x
Rtotal = total assembly R-value
For discrete layers:
Tn = Ti - (Ti - To) × ((Rsi + R1 + R2 + ... + Rn)/(Rtotal))
Vapor Pressure Profile
Vapor pressure profile depends on boundary conditions and material permeances:
Steady-state vapor flow:
ṁ = (pv,i - pv,o)/(ΣZ)
where:
Z = vapor resistance = 1/μ (reperm)
ΣZ = Z1 + Z2 + ... + Zn
Vapor pressure at interface n:
pv,n = pv,i - ṁ × (Z1 + Z2 + ... + Zn)
Condensation Location
Condensation occurs where vapor pressure exceeds saturation pressure:
If pv(x) > psat(T(x)) → condensation at location x
Condensation plane typically occurs:
- Cold climates: Within or at exterior face of insulation
- Hot-humid climates: At interior face of insulation
- Mixed climates: Seasonally variable location
Example Interstitial Condensation Analysis
2×6 wall assembly (interior to exterior):
- Gypsum board: 1/2 in., R-0.45, μ = 50 perm
- Polyethylene vapor retarder: 6 mil, R-0, μ = 0.05 perm
- Fiberglass insulation: 5-1/2 in., R-19, μ = 100 perm (air-permeable)
- OSB sheathing: 1/2 in., R-0.62, μ = 2 perm
- Housewrap: R-0, μ = 50 perm
Conditions:
- Interior: 70°F, 40% RH → pv,i = 0.145 psi
- Exterior: 20°F, 70% RH → pv,o = 0.021 psi
Total vapor resistance:
ΣZ = 1/50 + 1/0.05 + 1/100 + 1/2 + 1/50
ΣZ = 0.02 + 20.0 + 0.01 + 0.5 + 0.02 = 20.55 reperm
Vapor flow rate:
ṁ = (0.145 - 0.021)/20.55 = 0.00604 grain/(hr·ft²)
Vapor pressure at OSB interior face (after poly and insulation):
pv,osb = 0.145 - 0.00604 × (20.0 + 0.01) = 0.024 psi
Temperature at OSB interior face:
Rtotal = 0.68 + 0.45 + 19 + 0.62 + 0.17 = 20.92
R to OSB interior = 0.68 + 0.45 + 19 = 20.13
T_osb = 70 - (70 - 20) × (20.13/20.92) = 22.1°F
psat(22.1°F) = 0.046 psi
Since pv (0.024 psi) < psat (0.046 psi), no condensation occurs in this assembly despite the cold sheathing temperature.
The polyethylene vapor retarder (0.05 perm) effectively limits vapor flow to the cold sheathing.
Glaser Method
The Glaser method provides simplified steady-state interstitial condensation analysis, comparing vapor pressure and saturation pressure profiles through assemblies.
Glaser Procedure
- Calculate temperature profile through assembly layers
- Calculate saturation vapor pressure at each interface using psat(T)
- Calculate actual vapor pressure profile based on boundary conditions and vapor resistances
- Identify condensation zones where pv > psat
- Quantify condensation rate in affected zones
- Calculate monthly accumulation/drying to verify annual moisture balance
Monthly Condensation Analysis
Condensation rate in affected layer:
ṁcond = A × [(pv,1 - psat) × μ1 + (psat - pv,2) × μ2]
where:
A = wall area (ft²)
pv,1 = vapor pressure entering layer
pv,2 = vapor pressure exiting layer
psat = saturation pressure at condensing plane
μ1, μ2 = permeances before and after condensing plane
Monthly accumulation:
Mmonth = ṁcond × hours_per_month
Annual moisture balance requires:
Σ(Mdrying months) ≥ Σ(Mwetting months)
Glaser Method Limitations
The Glaser method assumes:
- Steady-state conditions (actual assemblies experience transient behavior)
- One-dimensional moisture flow (ignores lateral redistribution)
- No moisture storage in materials
- No air leakage
- No solar radiation effects
- No wind-driven rain
These limitations produce conservative predictions for vapor diffusion-driven condensation but miss dynamic phenomena captured by advanced hygrothermal modeling.
Dynamic Hygrothermal Modeling
Advanced simulation tools (WUFI, MOISTURE-EXPERT, hygIRC) solve coupled heat and moisture transport equations with transient boundary conditions.
Governing Equations
Heat transfer:
ρ × c × (∂T/∂t) = ∇·(λ∇T) + hv × ∇·(δp∇(φ × psat))
where:
ρ = density
c = specific heat
λ = thermal conductivity
hv = latent heat of evaporation
δp = vapor permeability
φ = relative humidity
Moisture transfer:
∂w/∂t = ∇·(Dw∇w + δp∇(φ × psat))
where:
w = moisture content
Dw = liquid diffusivity
Model Inputs
Material properties:
- Thermal conductivity λ(w,T)
- Vapor permeability δ(w,T)
- Liquid diffusivity Dw(w)
- Moisture storage function w(φ)
- Sorption isotherms
Boundary conditions:
- Hourly weather data (temperature, RH, solar radiation, wind-driven rain)
- Interior temperature and humidity schedules
- Surface transfer coefficients
Model Outputs
- Temperature and moisture content at each node over time
- Relative humidity profiles
- Condensation/evaporation rates
- Mold growth risk indicators
- Annual moisture balance
Validation Requirements
ASHRAE Standard 160 specifies acceptance criteria:
- 30-day running average surface RH ≤ 80% at T > 41°F
- No sustained elevated moisture content in materials
- Adequate drying between wetting events
Condensation Prevention Strategies
Cold Climates
Interior vapor retarder (Class I or II) on warm side of insulation:
- Limits vapor flow to cold surfaces
- Prevents interstitial condensation in insulation
- Allows outward drying during summer
Exterior insulation:
- Warms sheathing temperature
- Reduces condensation risk
- Increases temperature ratio TR
Hot-Humid Climates
Avoid interior vapor retarders:
- Interior cooling surfaces require inward drying capability
- Vapor-impermeable interior finishes trap moisture
Exterior vapor control:
- Low-perm exterior insulation (foil-faced polyiso)
- Limits inward vapor drive
- Interior must remain above dewpoint
Mixed Climates
Semi-permeable assemblies (Class III vapor retarders):
- Allow bidirectional drying
- Avoid vapor-impermeable layers on either side
- Variable-permeance membranes adapt to seasonal conditions
Measurement and Monitoring
Surface temperature: Infrared thermography identifies cold surfaces below dewpoint
Interstitial conditions: In-situ RH/temperature sensors monitor assembly performance
Moisture content: Pin-type or capacitance moisture meters detect elevated moisture in materials
Mold inspection: Visual examination during construction or renovation
Related Topics
- Dewpoint Temperature - Calculation methods and psychrometric relationships
- Surface Condensation - Interior surface temperature analysis
- Interstitial Condensation - Within-assembly moisture accumulation
- Drying Potential - Moisture removal capacity of assemblies
Condensation analysis requires integrated thermal and moisture analysis to predict surface and interstitial condensation risk across seasonal operating conditions.
Sections
Dew Point Temperature
Comprehensive analysis of dew point temperature in building envelope condensation analysis, including psychrometric relationships, calculation methods, saturation physics, and application to moisture control strategies in HVAC systems.
Surface Condensation
Comprehensive analysis of surface condensation in building envelopes, including thermal bridge effects, surface temperature calculations, condensation risk assessment, and prevention strategies for HVAC professionals
Interstitial Condensation
Analysis of moisture condensation within building envelope assemblies using vapor pressure profiles, dew point calculations, and transient moisture transport modeling for preventing moisture damage in wall and roof systems
Condensation Risk Assessment
Comprehensive methodology for evaluating condensation risk in building envelopes using temperature factor analysis, thermal resistance ratios, moisture accumulation calculations, and ASHRAE 160 criteria for mold growth prevention.