13.2 Profitability Analysis, Depreciation, and Break-Even
Key Takeaways
- Capital cost estimation distinguishes between Fixed Capital Investment (physical assets) and Working Capital (operating funds).
- Cost indices (such as CEPCI and M&S) adjust historical costs for inflation, while the six-tenths power law scales costs with equipment capacity.
- Straight-line and MACRS are key depreciation methods; MACRS neglects salvage value and uses NCEES table factors with a half-year convention.
- After-tax cash flows include a depreciation tax shield because depreciation is a non-cash expense that reduces taxable income.
- Break-even analysis determines the production volume where total revenue equals total costs, while public projects utilize the benefit-cost (B/C) ratio.
13.2 Profitability Analysis, Depreciation, and Break-Even
Quick Answer: Profitability analysis in chemical plants hinges on cost estimation, depreciation methods (Straight-Line and MACRS), tax effects, and break-even analysis. Equipment costs are scaled over time using cost indices like the Chemical Engineering Plant Cost Index (CEPCI) and scaled by capacity using the six-tenths power rule. After-tax cash flows are boosted by the depreciation tax shield because depreciation is a non-cash expense that reduces taxable income. Public projects are evaluated using the benefit-cost ratio (B/C), and decisions under uncertainty use expected value (EV).
Cost Estimation and Scaling in Chemical Engineering
Estimating the cost of a chemical process facility occurs in stages, ranging from rough order-of-magnitude estimates to detailed engineering designs. The total capital investment consists of two main parts:
- Fixed Capital Investment (FCI): The capital required to design, purchase, and construct the physical plant (equipment, piping, instrumentation, buildings, land).
- Working Capital (WC): The funds required to start up the plant and maintain day-to-day operations (raw materials inventory, salaries, accounts receivable). It is typically 10% to 20% of the FCI and is fully recovered at the end of the project's life.
Cost Indices and Capacity Scaling
Because equipment prices change over time due to inflation and economic conditions, engineers update historical cost data using cost indices. The two most common indices in chemical engineering are the Chemical Engineering Plant Cost Index (CEPCI) and the Marshall & Swift (M&S) Equipment Cost Index. The cost at a new time (Year 2) is calculated from the cost at an earlier time (Year 1) as:
\[C_2 = C_1 \left( \frac{I_2}{I_1} \right)\]
where \(I_1\) and \(I_2\) are the index values for Year 1 and Year 2.
To estimate the cost of a different equipment capacity, the six-tenths power law (or sizing scaling law) is used:
\[C_B = C_A \left( \frac{S_B}{S_A} \right)^n\]
where \(C_A\) and \(C_B\) are the costs of equipment with capacities \(S_A\) and \(S_B\), and \(n\) is the scaling exponent. If the exponent \(n\) is not specified, it is assumed to be \(0.6\) (the "six-tenths rule"). Combining both capacity scaling and inflation index updates yields:
\[C_{B,2} = C_{A,1} \left( \frac{S_B}{S_A} \right)^n \left( \frac{I_2}{I_1} \right)\]
Depreciation and Book Value
Depreciation is the systematic allocation of the cost of a tangible asset over its useful life. It is a non-cash expense that reduces taxable income.
Straight-Line (SL) Depreciation
Under straight-line depreciation, the asset depreciates by the same amount each year. The annual depreciation charge \(D_t\) is:
\[D_t = \frac{C - S_n}{n}\]
where \(C\) is the initial cost, \(S_n\) is the salvage value, and \(n\) is the recovery period (in years). The book value \(BV_t\) at the end of year \(t\) is:
\[BV_t = C - t \cdot D_t\]
Modified Accelerated Cost Recovery System (MACRS)
For U.S. federal tax purposes, the Modified Accelerated Cost Recovery System (MACRS) is standard. MACRS ignores salvage value in its calculations (salvage value is assumed to be zero for depreciation calculations, although selling the asset later can result in taxable gains). Under MACRS, the depreciation charge in year \(t\) is:
\[D_t = C \times Factor_t\]
where the recovery factors are obtained from NCEES interest tables. MACRS uses a half-year convention, which assumes assets are placed in service in the middle of the first year. Therefore, a property with an \(n\)-year recovery period is depreciated over \(n+1\) tax years. The book value is updated as:
\[BV_t = BV_{t-1} - D_t\]
Tax Effects on Cash Flows
Taxes reduce the cash flows generated by a project. Understanding the flow from revenue to after-tax cash flow is critical:
\[Taxable\ Income = Revenues - Operating\ Expenses - Depreciation\]
\[Income\ Tax = Taxable\ Income \times Tax\ Rate\ (t)\]
The net cash flow after tax (CFAT) is the actual cash generated by the project:
\[CFAT = Revenues - Operating\ Expenses - Income\ Tax\]
Substituting the equations, we get:
\[CFAT = (Revenues - Operating\ Expenses)(1 - t) + t \cdot Depreciation\]
The term \(t \cdot Depreciation\) represents the depreciation tax shield. Because depreciation is a paper expense, it reduces taxable income and saves the company cash equal to the tax rate multiplied by the depreciation charge.
Break-Even Analysis
Break-even analysis identifies the production volume \(Q\) where total revenue equals total cost. Total cost consists of fixed costs \(FC\) (independent of production volume) and variable costs \(VC\) per unit (dependent on production volume).
\[Total\ Revenue = Price\ (P) \times Quantity\ (Q)\]
\[Total\ Cost = Fixed\ Cost\ (FC) + Variable\ Cost\ (VC) \times Quantity\ (Q)\]
Setting Total Revenue equal to Total Cost yields the break-even quantity \(Q_{BE}\):
\[Q_{BE} = \frac{FC}{P - VC}\]
The term \((P - VC)\) is the contribution margin per unit. The plant must operate above \(Q_{BE}\) to turn a profit.
Benefit-Cost Ratio (B/C)
Public works projects are often evaluated using the Benefit-Cost (B/C) Ratio rather than private profitability metrics. The B/C ratio is defined as:
\[B/C = \frac{PW(Benefits)}{PW(Costs)} = \frac{AW(Benefits)}{AW(Costs)}\]
where benefits are the positive outcomes to the public, and costs are the expenditures incurred by the government. Sometimes, disbenefits (negative consequences to the public) are subtracted from benefits:
\[B/C = \frac{PW(Benefits) - PW(Disbenefits)}{PW(Costs)}\]
A project is considered economically acceptable if \(B/C \ge 1.0\). For choosing between multiple mutually exclusive public alternatives, an incremental B/C analysis must be performed. The alternatives are ranked by cost, and the ratio of incremental benefits to incremental costs (\(\Delta B / \Delta C\)) is calculated. If the incremental ratio is greater than or equal to 1.0, the higher-cost alternative is preferred.
Expected Value and Risk in Decision-Making
Under uncertainty, cash flows are modeled as random variables with associated probabilities. The Expected Value (EV) or expected profit is the probability-weighted sum of all possible outcomes:
\[E(X) = \sum_{i=1}^k P_i X_i\]
where \(i\) is the index of each outcome, \(P_i\) is the probability of outcome \(X_i\). Engineers use decision trees to evaluate sequential decisions under risk, choosing the path that maximizes the expected present worth.
Worked Examples
Example 1: Capacity Scaling and Cost Index Update
A chemical reactor with a capacity of 10,000 liters cost \$150,000 in 2018 when the CEPCI index was 567.5. Estimate the cost of a similar reactor with a capacity of 25,000 liters in 2026, when the CEPCI index is 845.2. Assume a capacity scaling exponent of 0.65.
Solution: Using the combined scaling and cost index equation: \[C_{2026} = C_{2018} \left( \frac{S_{2026}}{S_{2018}} \right)^{0.65} \left( \frac{I_{2026}}{I_{2018}} \right)\] \[C_{2026} = 150,000 \left( \frac{25,000}{10,000} \right)^{0.65} \left( \frac{845.2}{567.5} \right)\] \[\left( \frac{25,000}{10,000} \right)^{0.65} = 2.5^{0.65} \approx 1.8157\] \[\frac{845.2}{567.5} \approx 1.4893\] \[C_{2026} = 150,000 \times 1.8157 \times 1.4893 = 150,000 \times 2.7041 = \$405,615\]
Conclusion: The estimated cost of the larger reactor in 2026 is \$405,615.
Example 2: MACRS Depreciation and After-Tax Cash Flow
A company purchases a distillation column for \$100,000. It is classified as a 5-year MACRS property. The corporate tax rate is 21%. In Year 2, the column generates \$40,000 in revenues and incurs \$15,000 in operating expenses. The MACRS depreciation factor for a 5-year property in Year 2 is 32.00%. Calculate the after-tax cash flow for Year 2.
Solution: First, calculate the Year 2 depreciation charge: \[Depreciation\ (D_2) = \$100,000 \times 0.3200 = \$32,000\] Next, calculate taxable income: \[Taxable\ Income = Revenues - Operating\ Expenses - Depreciation\] \[Taxable\ Income = 40,000 - 15,000 - 32,000 = -$7,000\] Since the taxable income is negative, the company experiences a tax savings (assuming it has other profitable operations to offset this loss): \[Tax\ (T) = -$7,000 \times 0.21 = -$1,470\] Now, calculate the net cash flow after tax (CFAT): \[CFAT = (Revenues - Operating\ Expenses)(1 - t) + t \cdot Depreciation\] \[CFAT = (40,000 - 15,000)(1 - 0.21) + 0.21 \times 32,000\] \[CFAT = 25,000 \times 0.79 + 6,720 = 19,750 + 6,720 = \$26,470\] Alternatively: \[CFAT = Revenues - Operating\ Expenses - Tax\] \[CFAT = 40,000 - 15,000 - (-1,470) = 25,000 + 1,470 = \$26,470\]
Conclusion: The after-tax cash flow in Year 2 is \$26,470.
A chemical plant operates a spray dryer with a fixed annual cost of $200,000. The dryer processes a product that sells for $5.00 per kilogram. The variable cost of production is $2.50 per kilogram. What is the annual production quantity required to break even?
Under the MACRS depreciation method, how does the treatment of salvage value differ from that in the Straight-Line depreciation method when calculating the annual depreciation charge?
A chemical company is evaluating a project with a 21% tax rate. In a given year, the project generates $50,000 in taxable income before depreciation. If the depreciation charge for the year is $10,000, what is the net after-tax cash flow (CFAT) for that year?