22-Mec-B2 Environmental Control in Buildings · May 2015
Question 7 of 8: Seasonal heating fuel, and a gas furnace versus an air-source heat pump
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. Professional Engineers of Ontario / EGBC
annual examination, 07-Mec-B2 (now 22-Mec-B2) Environmental Control in
Buildings, May 2015 sitting. Three hours, open book.
Eight problems of 20 points each; the candidate is instructed to solve
five and to nominate on the cover of the first workbook which
five are to be graded. Psychrometric charts and a pressure–enthalpy
diagram for the refrigerant are appended to the paper, and candidates are
expected to bring an environmental-control text and steam tables. Instruction
1 invites the candidate to submit a clear statement of any interpretation
assumptions with the answer — that latitude is used explicitly below
wherever the printed data are redundant or incomplete.
All eight problems are worked here. Every psychrometric state has
been recomputed from the ASHRAE formulation for saturation vapour pressure
rather than scaled off a chart, so the numbers below are tighter than a
graphical solution would be; chart-quality agreement (about $\pm 0.2$ K in
temperature and $\pm 0.0002$ kg/kg in humidity ratio) is all that an examiner
expects, and a candidate reading the appended charts should reproduce every
answer to within that band.
Reference texts for this subject.
W. P. Jones, Air Conditioning Engineering, 5th ed.,
Butterworth-Heinemann — the standard reference for this examination
code; Ch. 2–3 (psychrometry), Ch. 6 (cooling loads), Ch. 10 (cooling
towers), Ch. 15 (fans and duct design).
McQuiston, Parker & Spitler, Heating, Ventilating and Air
Conditioning: Analysis and Design, 6th ed., Wiley — Ch. 3 (moist
air), Ch. 8 (energy estimating and degree-day methods), Ch. 12–13 (fluid
flow, fans and duct design).
ASHRAE Handbook – Fundamentals (2021) — Ch. 1
(psychrometrics), Ch. 21 (fans and duct design), Ch. 25–27 (heat, air
and moisture transfer in the envelope), Ch. 30 (refrigerant properties).
Moran, Shapiro, Boettner & Bailey, Fundamentals of Engineering
Thermodynamics, 9th ed., Wiley — Ch. 10 (vapour-compression
refrigeration and heat pumps).
ANSI/ASHRAE Standard 62.1, Ventilation for Acceptable Indoor Air
Quality, and ANSI/ASHRAE Standard 55, Thermal Environmental
Conditions for Human Occupancy.
Canadian frame: National Building Code of Canada 2020 (Part 6, and
Appendix C for design temperatures and degree-days), National Energy Code of
Canada for Buildings 2020, Health Canada Residential Indoor Air Quality
Guidelines, and Environment and Climate Change Canada Canadian Climate
Normals.
Psychrometric relations used throughout. At barometric
pressure $p$ with saturation vapour pressure $p_{ws}(t)$ from the ASHRAE
correlation, the humidity ratio, specific enthalpy and humid volume of moist
air are
with $h$ in kJ per kg of dry air, $t$ in $\,{}^{\circ}$C and $p$ in
kPa. In inch-pound units the enthalpy becomes $h = 0.240\,t + W\,(1061 +
0.444\,t)$ Btu per lb of dry air with $t$ in $\,{}^{\circ}$F. Wet-bulb
temperatures are obtained by solving the adiabatic-saturation equation, not by
eye. Mixing two air streams is exact in moisture and in
enthalpy, so $W$ and $h$ of the mixture are the mass-weighted
averages and the mixed dry bulb follows from them; weighting the dry bulb
directly is the usual shortcut and differs here by about $0.01$ K.
Question 7: Seasonal heating fuel, and a gas furnace versus an air-source heat pump (20 marks)
Given. A small commercial building in Toronto with a known design heating load and design temperature difference, heated by a gas furnace of stated efficiency, and a proposed air-source heat pump alternative.
Given data and stated assumptions
Quantity
Symbol
Value
Design sensible heating load
$\dot{Q}_s$
75 kW
Design latent heating load
$\dot{Q}_l$
12 kW
Indoor design temperature
$t_i$
22 °C
Outdoor design temperature
$t_o$
−20 °C
Furnace thermal efficiency
$\eta_f$
85%
Heat pump COP (compressor shaft)
COP
3.56
Compressor / motor efficiency
$\eta_m$
82%
Assumed: Toronto heating degree-days, base 18 °C
HDD
3520 °C·days (NBC 2020 App. C)
Assumed: degree-day correction factor
$C_D$
0.70
Assumed: natural gas higher heating value
HHV
37.5 MJ/m$^3$
Assumed: delivered natural gas price
—
CAD 0.32/m$^3$
Assumed: delivered electricity price
—
CAD 0.13/kWh
Find. The yearly heating fuel requirement; a schematic of an air-to-air heat pump serving this load; an account of other heat-pump types; and advice to the owner on cost and environmental impact.
Air-to-air heat pump serving the heating load. The outdoor coil acts as the evaporator, absorbing heat from cold outdoor air; the compressor raises the refrigerant pressure and temperature; the indoor coil acts as the condenser, delivering heat to the supply air; the expansion valve completes the cycle. In cooling mode a reversing valve interchanges the two coils.
Approach. Convert the design load and design temperature difference into an overall building conductance, apply the modified degree-day method to get the seasonal heat delivered, divide by the furnace efficiency to get fuel input, and convert to cubic metres of gas. Then repeat the seasonal calculation with the heat pump's system COP and compare cost and emissions on the stated assumptions.
Building conductance at design. The whole design load must be met by the heating plant, so the effective overall conductance including infiltration is$$UA = \frac{\dot{Q}_s + \dot{Q}_l}{t_i - t_o} = \frac{75 + 12}{22 - (-20)} = \frac{87}{42} = 2.0714 \text{ kW/K}$$
Seasonal heat delivered, by the modified degree-day method. Toronto has about 3520 °C·days below 18 °C. The correction factor $C_D$ accounts for the fact that internal and solar gains carry part of the load and that the plant does not run at design efficiency all season; 0.70 is the usual value for a commercial building at these temperatures:$$\dot{Q}_{del} = UA \times \text{HDD} \times 24 \times C_D = 2.0714 \times 3520 \times 24 \times 0.70$$$$\dot{Q}_{del} = 122496 \text{ kWh/year} = 441 \text{ GJ/year}$$
Fuel input to the furnace. At 85% efficiency,$$\dot{Q}_{fuel} = \frac{\dot{Q}_{del}}{\eta_f} = \frac{122496}{0.85} = 144113 \text{ kWh} = 518.8 \text{ GJ}$$
Yearly natural gas requirement. At a higher heating value of 37.5 MJ/m$^3$,$$V_{gas} = \frac{518.8 \times 10^3 \text{ MJ}}{37.5 \text{ MJ/m}^3} = \boxed{13835 \text{ m}^3\text{/year}}$$ At the assumed delivered price of CAD 0.32/m$^3$ this costs about CAD 4427 per year.
Heat pump: system coefficient of performance. The contractor's 3.56 is a shaft-work COP; the electricity actually purchased must also cover the motor losses, so$$\text{COP}_{sys} = \text{COP} \times \eta_m = 3.56 \times 0.82 = 2.919$$$$E_{hp} = \frac{\dot{Q}_{del}}{\text{COP}_{sys}} = \frac{122496}{2.919} = \boxed{41962 \text{ kWh/year}}$$ At CAD 0.13/kWh that is about CAD 5455 per year.
Compare operating cost. On these assumptions the heat pump costs about CAD $1028$ more per year than the furnace — roughly $23$ % more — despite moving heat about three times more efficiently than the furnace burns it. The reason is entirely the price ratio: electricity at CAD 0.13/kWh is $0.13 \div (0.32 \times 3.6/37.5) = 4.2$ times the cost of the same delivered energy in gas, so a COP of about $3.6$ is needed merely to break even. A resistance-heated building would spend CAD $15924$, so the heat pump is still far better than electric baseboards.
Compare environmental impact. Natural gas emits about 1.921 kg CO₂e per cubic metre burned, whereas Ontario's electricity grid is largely nuclear and hydro with an intensity of roughly 30 g CO₂e/kWh:$$\text{gas: } 13835 \times 1.921 = 26577 \text{ kg CO}_2\text{e/y} \qquad \text{heat pump: } 41962 \times 0.030 = 1259 \text{ kg CO}_2\text{e/y}$$ a reduction of about $95$ %, or $25.3$ tonnes of CO₂e per year. This is the decisive difference between the two options, and it is a feature of the Ontario grid specifically — the same comparison in Alberta or Saskatchewan would favour the heat pump far less.
Other types of heat pump. Heat pumps are classified by the source and sink they exchange with. An air-to-air unit, as drawn above, is the cheapest to install but suffers exactly where this building needs it most: capacity and COP both fall as outdoor temperature drops, and periodic defrost cycles impose a further penalty. An air-to-water unit rejects into a hydronic loop and suits buildings with fan-coil or radiant distribution. A ground-source (geothermal) heat pump, water-to-air or water-to-water, exchanges with vertical boreholes, horizontal loops or a pond; because the ground stays near the annual mean temperature, seasonal COP is both higher and far more stable, at the cost of substantial drilling. A water-source machine uses a lake, river, well or a building's own condenser-water loop, and in the water-loop form allows heat rejected by one zone to serve another. Wastewater and sewer-source heat pumps exploit a warm, stable urban resource and are in service in several Canadian district-energy schemes. Finally, absorption heat pumps are driven by heat rather than shaft work and are worth considering where waste heat or cheap gas is available.
Advice to the owner. Four points, in order of importance. First, verify the COP claim at the design condition. A COP of 3.56 is a rating-point or seasonal figure; no ordinary air-source machine achieves it at −20 °C, where COP typically falls to 1.5–2.0 and capacity to roughly half of nameplate. The contractor should be asked for certified capacity and COP tables at −8, −15 and −20 °C. Second, do not remove the furnace. A dual-fuel (hybrid) installation — heat pump as the lead source, existing gas furnace as backup below a changeover temperature chosen on cost or emissions — captures most of the emissions benefit, keeps the design-day capacity the building already has, and avoids the electrical service upgrade that resistance backup would demand. Third, be candid that the operating cost will probably rise. On the assumptions above the heat pump costs about CAD 1028 a year more; the case for it is environmental and, increasingly, regulatory, not financial at today's Ontario price ratio. The owner should test the sensitivity to future carbon pricing and to time-of-use electricity rates before committing. Fourth, look at the envelope first. A 2.07 kW/K conductance on a small commercial building is high; air sealing, attic insulation and glazing upgrades reduce the load for every option simultaneously, and they also let a smaller and cheaper heat pump cover a larger fraction of the season.
Check: every economic and climatic input is an assumption, as the question requires. The paper supplies no degree-days, no fuel heating value and no energy prices, and instruction 1 asks for assumptions to be stated. Those used are: Toronto HDD$_{18}$ = 3520 °C·days (NBC 2020 Appendix C), $C_D$ = 0.70, gas HHV 37.5 MJ/m$^3$, gas CAD 0.32/m$^3$ and electricity CAD 0.13/kWh delivered, gas emission factor 1.921 kg CO₂e/m$^3$ and Ontario grid intensity 30 g CO₂e/kWh. The ranking of the two options on emissions is robust to any plausible variation in these; the ranking on cost is not, and reverses if electricity falls below about CAD 0.106/kWh or gas rises above about CAD 0.39/m$^3$.
Final results
Quantity
Symbol
Result
Overall building conductance
$UA$
2.0714 kW/K
Seasonal heat delivered
$\dot{Q}_{del}$
122496 kWh (441 GJ)
Furnace fuel energy input
$\dot{Q}_{fuel}$
144113 kWh (518.8 GJ)
Yearly natural gas requirement
$V_{gas}$
13835 m$^3$/year
Heat pump system COP
$\text{COP}_{sys}$
2.919
Heat pump yearly electricity
$E_{hp}$
41962 kWh/year
Yearly cost — gas furnace
—
CAD 4427
Yearly cost — heat pump
—
CAD 5455 (CAD 1028 more)
Yearly emissions — gas furnace
—
26.6 t CO₂e
Yearly emissions — heat pump
—
1.3 t CO₂e (95% lower)
Recommendation
—
Dual-fuel: heat pump lead, existing furnace as backup below the changeover temperature