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23-Chem-A5 Chemical Plant Design and Economics · May 2014

Question 2 of 6: Cost Estimation

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

Notes on this paper

National Exams — May 2014 — 04-Chem-A5 Chemical Plant Design and Economics. Three-hour, closed-book exam; any non-communicating calculator permitted. Six equally weighted (20-mark) questions are posed and the candidate answers any five; only the first five are marked. All six are answered below for completeness. Questions 1, 5 and 6 are conceptual design / management / safety questions answered as organised prose; questions 2, 3(i) and 4 contain the numerical work (cost–capacity scaling of a heat exchanger, sinking-fund depreciation, and simple/compound loan interest), and every boxed figure.

Reference texts: M.S. Peters, K.D. Timmerhaus & R.E. West, Plant Design and Economics for Chemical Engineers (5th ed., McGraw-Hill) — the exam's named primary text (cost estimation Ch. 6, interest and investment Ch. 7, depreciation Ch. 9, profitability Ch. 10, optimum design Ch. 11, plant safety and loss prevention); R. Turton et al., Analysis, Synthesis, and Design of Chemical Processes (4th ed., Prentice Hall) — flowsheet synthesis and process development; T.M. Duncan & J.A. Reimer, Chemical Engineering Design and Analysis (Cambridge, 1998) — the source of the boiling-point data used in Question 1; supporting Canadian tax practice from the Canada Revenue Agency Capital Cost Allowance classes and the half-year rule.

Question 2: Cost Estimation (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.

Given. Target exchanger area $A_2 = 800~\text{ft}^2$. A geometrically similar exchanger of one-quarter that area, $A_1 = 800/4 = 200~\text{ft}^2$, costs $\$4000$ (both in 2014, so no cost-index escalation is needed). Cost–capacity exponent $n = 0.60$ over 100–400 ft2 and $n = 0.81$ over 400–2000 ft2.

Find. The 2014 purchase cost of the 800 ft2 exchanger.

Approach. Apply the power-law ("six-tenths") cost–capacity rule, but because the reference (200 ft2) and the target (800 ft2) sit on opposite sides of the 400 ft2 exponent break, scale in two steps that meet at 400 ft2, using the correct exponent in each range.

  1. State the cost–capacity rule. For similar equipment the purchase cost scales with size raised to a capacity exponent: $$C_2 = C_1\left(\frac{A_2}{A_1}\right)^{n}$$ where $C_1$ is the known cost at area $A_1$ and $n$ is the exponent valid over that size range. Here the reference size is $A_1 = 200~\text{ft}^2$ at $C_1 = \$4000$.
  2. Scale 200 → 400 ft2 at $n = 0.60$. This step stays entirely inside the 100–400 ft2 band, so use $n = 0.60$: $$C_{400} = \$4000\left(\frac{400}{200}\right)^{0.60} = \$4000\,(2)^{0.60} = \$4000(1.5157) = \boxed{\$6063}$$
  3. Scale 400 → 800 ft2 at $n = 0.81$. This step lies inside the 400–2000 ft2 band, so switch to $n = 0.81$ and start from the just-computed $C_{400}$: $$C_{800} = \$6063\left(\frac{800}{400}\right)^{0.81} = \$6063\,(2)^{0.81} = \$6063(1.7532) = \boxed{\$10{,}630}$$ The purchase cost of the 800 ft2 exchanger in 2014 is therefore about $\$10{,}630$.
QuantityValue
Reference area / cost200 ft2 / $\$4000$
Cost at 400 ft2 (via $n=0.60$)$\$6063$
Cost at 800 ft2 (via $n=0.81$)$\$10{,}630$
Check: the two-step bridge is essential. Applying the single exponent $n=0.81$ blindly over the full four-fold jump, $\$4000\,(800/200)^{0.81}=\$4000(4)^{0.81}=\$12{,}295$, over-states the cost by about 16 % because it wrongly charges the steeper large-area exponent to the 200–400 ft2 portion, where the shallower $n=0.60$ actually applies.