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24-Bld-A5 Building Science · December 2019

Question 2 of 6

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

07-Bld-A5 Building Science — National Exam, December 2019. Six problems of 20 marks each were printed; per the paper's own NOTES only the first five in the answer book are graded, but all six are answered below as a complete study resource.

Reference texts: ASHRAE Handbook — Fundamentals (Chapters 1 Psychrometrics, 4 Heat Transfer, 14 Climatic Design Information, 16 Ventilation and Infiltration, 25 Thermal and Water Vapor Transmission Data, 26 Heat, Air, and Moisture Control in Building Assemblies); McQuiston, Parker & Spitler, Heating, Ventilating, and Air Conditioning: Analysis and Design; National Building Code of Canada (NBCC).

Question 2 (20 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Part (A)(i) — air-flow models for a wall cavity. Two complementary models are used to analyze air movement through a wall's air space, depending on what drives the flow. The ORIFICE-FLOW (power-law) model treats each leakage path (crack, gap, joint) as a discrete opening and relates volumetric flow to the pressure difference across it by $Q=C(\Delta P)^n$, with the flow exponent n ranging from 0.5 (fully turbulent, sharp-edged orifice) to 1.0 (fully laminar, e.g. flow through a porous batt); this is the standard model for AIR-BARRIER-DRIVEN leakage testing (ASTM E283/E779) and for predicting infiltration through known crack geometries. The POROUS-MEDIUM (Darcy) model instead treats the cavity's fill (insulation batt, loose fibre) as a continuum with an effective air permeability, appropriate when the "leakage path" is distributed through a porous material rather than concentrated at discrete cracks; flow is proportional to $\Delta P$ directly (n=1), consistent with laminar Darcy flow. In parallel, a THERMALLY-DRIVEN convection loop can develop within an open (unfilled or lightly filled) cavity even with zero net pressure difference across the wall, driven purely by the temperature difference between the cavity's warm and cold faces setting up a local buoyancy-driven circulation cell that degrades the nominal R-value of an air space; this natural-convection behaviour is analyzed separately from the pressure-driven orifice/Darcy models using a cavity Rayleigh number.

Part (A)(ii) — what cavity air-flow resistance depends on. Resistance to air flow through a wall cavity is governed by: (1) the cavity's GEOMETRY — its width (gap dimension), continuity, and compartmentalization by vertical/horizontal blocking (fire-stopping also interrupts convective loops); (2) the PERMEABILITY of any fill material occupying the cavity — a lightly-filled or fibrous batt cavity is far more resistant to bulk flow than a truly open air space, but also conducts more convective heat if the fill is loose enough to allow circulation; (3) the ROUGHNESS and TORTUOSITY of the leakage path where flow is concentrated at discrete cracks (orifice model), which sets the flow exponent n and the flow coefficient C; and (4) the PRESSURE DIFFERENTIAL itself and its DRIVER (wind gusting vs. a steady stack-effect gradient), since a turbulent, gusting driver interacts differently with a given cavity geometry than a slow steady one. A well-designed drainage/ventilation cavity behind a rainscreen deliberately balances these: enough resistance to avoid becoming a bulk air-leakage bypass path, but enough continuity to drain and dry (Question 6).

Part (B).

Given.

Wall assembly (exterior → interior) and boundary conditions
Layer / conditionValue
Face brick (exterior)100 mm, k ≈ 0.9 W/(m·K)
Fibreglass blanket100 mm, k = 0.04 W/(m·K) (given)
Gypsum board (interior finish)10 mm, k ≈ 0.16 W/(m·K)
Inside / outside air temperature20 °C (293.15 K) / −15 °C (258.15 K)
Wall area300 m²
Check: the thermal conductivities of face brick and gypsum board are not printed in the question (a materials-properties handout was very likely supplied with this open-book exam) — standard ASHRAE Fundamentals Ch. 26 values are assumed. Standard still-air/24 km/h-wind surface films (Rsi=1/8.29, Rso=1/34 m²K/W) are used since no wind speed is stated.

Find. (i) The total heat loss through the 300 m² wall; (ii) the extra fibreglass thickness needed to cut that heat loss by 20%.

Brick 100 mm Fiberglass batt 100 mm, k=0.04 Gypsum Exterior Interior Composite wall cross-section, Problem 2 (exterior at brick face)
Exterior air → face brick → fibreglass batt → gypsum board → interior air, all in series.

Approach. Sum the four conduction/surface-film resistances in series to get the base total resistance and heat loss, then use the fact that heat loss is inversely proportional to total resistance (area and ΔT fixed) to find how much EXTRA fibreglass resistance — and hence thickness — a 20% cut requires.

  1. Surface and layer resistances. Standard ASHRAE winter-design surface films (still air inside, hi=8.29 W/m²K; 24 km/h wind outside, ho=34 W/m²K) and layer conduction R=L/k: $$R_{si}=\frac{1}{8.29}=0.1206,\ \ R_{brick}=\frac{0.100}{0.9}=0.1111,\ \ R_{fg}=\frac{0.100}{0.04}=2.500,\ \ R_{gyp}=\frac{0.010}{0.16}=0.0625,\ \ R_{so}=\frac{1}{34}=0.0294\ \ (\text{m}^2\text{K/W})$$
  2. Total resistance and heat flux. $$R_{total}=0.1206+0.1111+2.500+0.0625+0.0294=2.824\ \text{m}^2\text{K/W}$$ $$q''=\frac{\Delta T}{R_{total}}=\frac{20-(-15)}{2.824}=12.40\ \text{W/m}^2$$
  3. (i) Total heat loss. $$\boxed{Q = q''\times A = 12.40\times300 = 3719\ \text{W}\approx 3.72\ \text{kW}}$$
  4. (ii) Set up the 20%-reduction condition. With A and ΔT unchanged, $Q\propto 1/R_{total}$, so cutting Q by 20% (to 0.8Q) requires $$R'_{total}=\frac{R_{total}}{0.8}=\frac{2.824}{0.8}=3.530\ \text{m}^2\text{K/W}$$ i.e. an ADDED resistance of $\Delta R = 3.530-2.824=0.706\ \text{m}^2\text{K/W}$, supplied entirely by extra fibreglass thickness (the only layer being changed).
  5. Convert the added resistance to thickness using $\Delta R = \Delta L_{fg}/k_{fg}$: $$\Delta L_{fg} = \Delta R\times k_{fg} = 0.706\times0.04 = 0.0282\ \text{m} = 28.2\ \text{mm}$$ $$\boxed{L_{fg,new} = 100+28.2 = 128.2\ \text{mm (i.e. the fibreglass blanket must roughly, but not quite, double)}}$$
Problem 2B — final results
QuantityValue
Total thermal resistance (base)2.824 m²K/W
(i) Total heat loss (base)3719 W (3.72 kW)
Required total resistance (20% cut)3.530 m²K/W
(ii) New fibreglass thickness128.2 mm (+28.2 mm)