23-Chem-B10 Life Cycle Assessment (LCA) · December 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exam 04-Chem-B10, Life Cycle Assessment (LCA) — December 2014. 3 hours, Closed-Book Exam (approved calculator and one double-sided aid sheet permitted). Question 1 is mandatory; any three (3) of the remaining four (Questions 2–5) constitute a complete 100-mark paper, and only the first four questions as they appear in the answer book are marked. All five questions are solved below for completeness.
Reference texts: Baumann & Tillman, The Hitch Hiker's Guide to LCA; Graedel & Allenby, Industrial Ecology and Sustainable Engineering; Allen & Shonnard, Green Engineering; Kemp, Pinch Analysis and Process Integration, 2nd ed.; Mackay, Multimedia Environmental Models: The Fugacity Approach, 2nd ed.; Davis & Cornwell, Introduction to Environmental Engineering.
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.
A Life Cycle Assessment is only as meaningful as the boundary drawn around the system being studied and the basis chosen for comparing alternatives. The system boundary defines which life-cycle stages, unit processes, and even geographic/temporal scope are included in the inventory — common choices are cradle-to-gate (raw material extraction through the factory gate), gate-to-gate (a single process step), and cradle-to-grave (extraction through end-of-life disposal or recycling). The functional unit is the quantified performance basis on which competing systems are compared, and it must represent an equivalent unit of service each alternative actually provides, not merely a convenient physical count of one of them.
Worked example — a 100%-recycled-content vs. virgin-stock aluminum beverage can. If the system boundary is drawn narrowly as gate-to-gate can manufacture and the functional unit is naively taken as "one can produced," the two look nearly identical: both are stamped from aluminum sheet on the same line, using essentially the same forming energy. A study stopped there finds no meaningful difference. But primary (virgin) aluminum smelting is one of the most electricity-intensive industrial processes in existence (Hall-Héroult electrolysis), while remelting recycled aluminum requires roughly 5–10% of that smelting energy. Extending the boundary to cradle-to-gate (including the upstream metal-production stage) and keeping the functional unit correctly scaled as "delivering 1000 L of beverage in cans" reverses the conclusion sharply: the recycled-content can's embodied energy and GHG burden can be an order of magnitude lower than the virgin-stock can's, driven entirely by a production stage the narrow gate-to-gate boundary excluded. This demonstrates that boundary and functional-unit selection are not bookkeeping details: they can determine which alternative appears superior, and a report that omits or buries these choices is not defensible engineering judgement.
The general phases associated with a product's development and distribution are: (1) raw material acquisition (extraction/harvesting of virgin or recycled feedstocks); (2) materials processing (refining/converting feedstocks into engineering materials, e.g. aluminum ingot, resin pellets, sheet metal); (3) manufacturing/assembly of the product itself; (4) distribution/transportation to the point of sale or use; (5) use phase (operation, maintenance, consumption by the end user); and (6) end-of-life management (reuse, recycling, energy recovery, or landfill disposal).
Continuing the beverage-can example, consider the materials processing phase. Inputs to investigate for the virgin-stock route include bauxite ore, caustic soda (Bayer process refining to alumina), and the very large electricity draw of the Hall-Héroult smelting cell; outputs include red-mud residue from alumina refining (a caustic, metal-bearing waste requiring long-term containment) and, historically, perfluorocarbon (PFC) emissions from the smelting cells (a potent greenhouse gas, now substantially reduced by modern cell technology but still a process to scrutinize). For the recycled-content route, the input is simply scrap aluminum plus the (much smaller) remelting energy, with sorting/de-coating losses as the main output to track; there is no bauxite mining, no red-mud generation, and negligible PFC emission.
Working from the materials-processing inventory built in (b): Classification sorts each inventory flow into the impact category (or categories) it contributes to — smelting-cell electricity (via the grid's generation mix) and any residual PFC emissions classify under global warming; red-mud disposal classifies under resource depletion/land use and potential ecotoxicity if containment fails; and Bayer-process caustic soda manufacture classifies under both global warming (energy-intensive) and eutrophication/aquatic toxicity if effluent is poorly managed. Characterization converts each classified flow into a common unit within its category using established equivalency factors — PFC emissions (e.g. CF4) are multiplied by their extremely high 100-year Global Warming Potential (in the thousands, relative to CO2) to build a single "kg CO2-equivalent" score, and grid electricity is multiplied by the local emissions-intensity factor (kg CO2-eq/kWh). Evaluation (normalization and weighting) then combines the several characterized category scores into an overall comparative judgement, e.g. normalizing each category against a regional per-capita reference load and weighting global warming vs. resource depletion vs. ecotoxicity, so that a single relative ranking of "recycled-content can" vs. "virgin-stock can" per 1000 L delivered can be reported.
Assumptions to state explicitly: a specific regional electricity-grid emissions factor for the smelting/remelting energy (the single most sensitive parameter in this comparison, since a low-carbon grid narrows the gap considerably); a 100-year GWP time horizon; an assumed modern (post-PFC-abatement) smelter technology rather than a legacy facility; and equal severity weighting between global-warming and resource-depletion categories unless a specific regional priority (e.g. local land-use conflict from bauxite mining) justifies otherwise.
| Compound | Primary environmental concern |
|---|---|
| CO2 | Principal anthropogenic greenhouse gas; long atmospheric residence time (centuries) drives global climate change via radiative forcing. Used as the reference (GWP = 1) for all other greenhouse gases. |
| NOx (NO, NO2) | Precursor to ground-level (tropospheric) ozone and photochemical smog via reaction with VOCs in sunlight; contributes to acid rain (nitric acid formation) and is itself a respiratory irritant at ambient concentrations. |
| SOx (mainly SO2) | Oxidizes in the atmosphere to sulfuric acid, the dominant historical cause of acid rain/acid deposition (soil and surface-water acidification, forest and aquatic ecosystem damage); also a direct respiratory irritant and fine-particulate (sulfate aerosol) precursor. |
| VOC's | Precursor (with NOx) to photochemical smog and ground-level ozone; many individual VOC species (e.g. benzene, formaldehyde) are additionally toxic or carcinogenic in their own right, so VOC control addresses both a regional smog concern and, for specific compounds, a direct human-health concern. |