23-Chem-A5 Chemical Plant Design and Economics · December 2014
Question 2 of 6: Cost Estimation
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — December 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. Question 1 is a conceptual process-design question answered with a flow sheet and organised prose; questions 2, 3 and 4 mix a short essay with numerical work (turnover-ratio pricing, sinking-fund depreciation, and simple/compound loan interest); question 5 combines profitability and risk discussion with a return-and-payout calculation; question 6 is a safety, optimization and environmental essay.
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 and payout 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, and environmental practice from the Canadian Environmental Protection Act (CEPA) and provincial air-quality regulation.
(a) The five components of total capital investment
The total capital investment (TCI) of a plant is the sum of the fixed capital that buys the physical installation and the working capital that keeps it running; the five categories named in the question map onto that split as follows:
(i) Battery-limits investment. The capital for the processing units inside the plant's defined boundary ("inside battery limits", ISBL) — reactors, columns, exchangers, pumps and their installation. It is the core, directly productive investment and normally the largest single block, so it anchors every factored cost estimate.
(ii) Utility investment. The capital for on-site utility generation and distribution — steam boilers, cooling water, refrigeration, power, instrument air. Without it the process units cannot run; its size depends on how much utility is bought over the fence versus generated in-house.
(iii) Off-site investment. The "outside battery limits" (OSBL) facilities that support production but sit outside the process boundary — storage, tank farms, roads, buildings, effluent treatment, site preparation. It is essential to a workable plant and is easy to underestimate in early estimates.
(iv) Engineering fees. The cost of process and detailed engineering, design, drafting, project management and the constructor's overhead and profit. It is an indirect but unavoidable fixed-capital cost, typically taken as a percentage of the direct plant cost.
(v) Working capital. The money tied up in operating the plant once built — raw-material and product inventories, cash for wages and payables, accounts receivable. Unlike the fixed-capital items it is recovered at the end of the project life, but it must be financed throughout and so is part of the TCI.
Items (i)–(iv) together make up the fixed-capital investment (FCI); adding (v) gives the total capital investment, $\text{TCI}=\text{FCI}+\text{WC}$. Distinguishing them matters because depreciation is charged on the fixed capital only, whereas working capital is returned intact.
(b) Selling price for a turnover ratio of 1.0
Given. Total capital investment $\text{TCI}=\$50{,}000{,}000$; working capital $\text{WC}=\$1{,}000{,}000$; capacity $=24$ t/day; operating time $=360$ days/yr; target turnover ratio $=1.0$.
Find. The selling price per kilogram of cement.
Approach. Peters & Timmerhaus define the turnover ratio as gross annual sales divided by the fixed-capital investment; so first strip working capital out of the TCI to get the FCI, set annual sales equal to the turnover ratio times FCI, then divide those sales by the annual production in kilograms.
Fixed-capital investment. Working capital is not part of the fixed plant, so
$$\text{FCI} = \text{TCI} - \text{WC} = \$50\text{M} - \$1\text{M} = \boxed{\$49\text{ million}}$$
Required gross annual sales. The turnover ratio is $\text{TR}=\dfrac{\text{annual sales}}{\text{FCI}}$, so for $\text{TR}=1.0$
$$\text{Sales} = \text{TR}\times\text{FCI} = 1.0\times\$49\text{M} = \$49\text{ million/yr}$$
Annual production. At 24 t/day for 360 days,
$$\dot m = 24\ \tfrac{\text{t}}{\text{day}}\times360\ \tfrac{\text{day}}{\text{yr}} = 8640\ \tfrac{\text{t}}{\text{yr}} = 8{,}640{,}000\ \tfrac{\text{kg}}{\text{yr}}$$
Selling price. Dividing the required sales by the production,
$$P = \frac{\text{Sales}}{\dot m} = \frac{\$49{,}000{,}000}{8{,}640{,}000\ \text{kg}} = \boxed{\$5.67\text{/kg}}$$
The cement must sell for about $\$5.67$ per kilogram to return a turnover ratio of one.
Quantity
Value
Fixed-capital investment (TCI − WC)
$\$49$ million
Required gross annual sales (TR = 1.0)
$\$49$ million/yr
Annual production
$8640$ t = $8.64\times10^{6}$ kg
Selling price
$\$5.67$/kg
Check: the working capital is quoted separately precisely so it can be removed — the P&T turnover ratio is referenced to the fixed-capital investment, not the total. Had sales been set on the full $\$50$M TCI the price would be $\$5.79$/kg; the $\$1$M of working capital is what makes the difference. (For a mundane commodity like cement a real selling price is far below $\$5.67$/kg, so a turnover ratio of 1.0 is unrealistically low here — but the question fixes it as a given.)