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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.

Last updated: July 2026

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:

  1. Fixed Capital Investment (FCI): The capital required to design, purchase, and construct the physical plant (equipment, piping, instrumentation, buildings, land).
  2. 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:

C2=C1(I2I1)C_2 = C_1 \left( \frac{I_2}{I_1} \right)

where I1I_1 and I2I_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:

CB=CA(SBSA)nC_B = C_A \left( \frac{S_B}{S_A} \right)^n

where CAC_A and CBC_B are the costs of equipment with capacities SAS_A and SBS_B, and nn is the scaling exponent. If the exponent nn is not specified, it is assumed to be 0.60.6 (the "six-tenths rule"). Combining both capacity scaling and inflation index updates yields:

CB,2=CA,1(SBSA)n(I2I1)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 DtD_t is:

Dt=C−SnnD_t = \frac{C - S_n}{n}

where CC is the initial cost, SnS_n is the salvage value, and nn is the recovery period (in years). The book value BVtBV_t at the end of year tt is:

BVt=C−t⋅DtBV_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 tt is:

Dt=C×FactortD_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 nn-year recovery period is depreciated over n+1n+1 tax years. The book value is updated as:

BVt=BVt−1−DtBV_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−DepreciationTaxable\ Income = Revenues - Operating\ Expenses - Depreciation Income Tax=Taxable Income×Tax Rate (t)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 TaxCFAT = Revenues - Operating\ Expenses - Income\ Tax

Substituting the equations, we get:

CFAT=(Revenues−Operating Expenses)(1−t)+t⋅DepreciationCFAT = (Revenues - Operating\ Expenses)(1 - t) + t \cdot Depreciation

The term t⋅Depreciationt \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 QQ where total revenue equals total cost. Total cost consists of fixed costs FCFC (independent of production volume) and variable costs VCVC per unit (dependent on production volume).

Total Revenue=Price (P)×Quantity (Q)Total\ Revenue = Price\ (P) \times Quantity\ (Q) Total Cost=Fixed Cost (FC)+Variable Cost (VC)×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 QBEQ_{BE}:

QBE=FCP−VCQ_{BE} = \frac{FC}{P - VC}

The term (P−VC)(P - VC) is the contribution margin per unit. The plant must operate above QBEQ_{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=PW(Benefits)PW(Costs)=AW(Benefits)AW(Costs)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=PW(Benefits)−PW(Disbenefits)PW(Costs)B/C = \frac{PW(Benefits) - PW(Disbenefits)}{PW(Costs)}

A project is considered economically acceptable if B/C≥1.0B/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 (ΔB/ΔC\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)=∑i=1kPiXiE(X) = \sum_{i=1}^k P_i X_i

where ii is the index of each outcome, PiP_i is the probability of outcome XiX_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:

C2026=C2018(S2026S2018)0.65(I2026I2018)C_{2026} = C_{2018} \left( \frac{S_{2026}}{S_{2018}} \right)^{0.65} \left( \frac{I_{2026}}{I_{2018}} \right) C2026=150,000(25,00010,000)0.65(845.2567.5)C_{2026} = 150,000 \left( \frac{25,000}{10,000} \right)^{0.65} \left( \frac{845.2}{567.5} \right) (25,00010,000)0.65=2.50.65≈1.8157\left( \frac{25,000}{10,000} \right)^{0.65} = 2.5^{0.65} \approx 1.8157 845.2567.5≈1.4893\frac{845.2}{567.5} \approx 1.4893 C2026=150,000×1.8157×1.4893=150,000×2.7041=$405,615C_{2026} = 150,000 \times 1.8157 \times 1.4893 = 150,000 \times 2.7041 = \text{\textdollar}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 (D2)=$100,000×0.3200=$32,000Depreciation\ (D_2) = \text{\textdollar}100,000 \times 0.3200 = \text{\textdollar}32,000

Next, calculate taxable income:

Taxable Income=Revenues−Operating Expenses−DepreciationTaxable\ Income = Revenues - Operating\ Expenses - Depreciation Taxable Income=40,000−15,000−32,000=−$7,000Taxable\ Income = 40,000 - 15,000 - 32,000 = -\text{\textdollar}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)=−$7,000×0.21=−$1,470Tax\ (T) = -\text{\textdollar}7,000 \times 0.21 = -\text{\textdollar}1,470

Now, calculate the net cash flow after tax (CFAT):

CFAT=(Revenues−Operating Expenses)(1−t)+t⋅DepreciationCFAT = (Revenues - Operating\ Expenses)(1 - t) + t \cdot Depreciation CFAT=(40,000−15,000)(1−0.21)+0.21×32,000CFAT = (40,000 - 15,000)(1 - 0.21) + 0.21 \times 32,000 CFAT=25,000×0.79+6,720=19,750+6,720=$26,470CFAT = 25,000 \times 0.79 + 6,720 = 19,750 + 6,720 = \text{\textdollar}26,470

Alternatively:

CFAT=Revenues−Operating Expenses−TaxCFAT = Revenues - Operating\ Expenses - Tax CFAT=40,000−15,000−(−1,470)=25,000+1,470=$26,470CFAT = 40,000 - 15,000 - (-1,470) = 25,000 + 1,470 = \text{\textdollar}26,470

Conclusion: The after-tax cash flow in Year 2 is $26,470.

Test Your Knowledge

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?

A

40,000 kg

B

50,000 kg

C

60,000 kg

D

80,000 kg

Test Your Knowledge

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

MACRS deducts the salvage value from the initial cost first, similar to the straight-line method, but uses accelerated rates.

B

MACRS requires multiplying the salvage value by tax rate before deducting it from the basis.

C

MACRS assumes the salvage value is zero for the purpose of calculating depreciation charges, whereas the straight-line method deducts the salvage value from the initial cost.

D

MACRS uses the salvage value to determine the recovery period length instead of the depreciation basis.

Test Your Knowledge

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?

A

$31,600

B

$41,600

C

$39,500

D

$29,500

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