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MCSGP Economic Calculator

Model the economics of large-scale peptide and oligonucleotide manufacturing. Compare conventional batch chromatography with ChromaCon’s MCSGP / AutoPeak® continuous process and see the impact on cost per gram, solvent and waste, profit, payback and ROI for your own production scenario.

MCSGP Cost & ROI Calculator
Batch vs MCSGP / AutoPeak® continuous chromatography — peptides & oligonucleotides
⚠ Charts could not be loaded. All figures and tables below are still fully calculated.

Inputs

Drives process mass intensity and synthesis cost. 39 = tirzepatide.
Cost scenario i
Plant scenario i
Distinct molecules sharing the plant. Sizes the system so campaigns fill the operating year (~320 days).
Yield & productivity assumptions
Advanced process inputs

Using the Productivity batch / MCSGP values from the main panel above.

Calibration (locked model constants)
Source-of-truth constants. Edits here are live but in-session only (reset on reload).
Generic-tier discount factors (New Drug → Generic)

Manufacturing cost per gram

Total and downstream-only cost of API

BatchMCSGP

Profit at scale

Annual profit per product vs production amount

Steps mark where the recommended column / system size changes as production grows.

Solvent & waste

Annual solvent cost (bars) and waste mass

BatchMCSGP

Quality-control burden

In-process controls per year

BatchMCSGP

Cost breakdown — at the selected annual amount

Sensitivity — what moves MCSGP profit

Each bar spans MCSGP profit as the input varies ±20% (others held at base)

Model assumptions & provenance

Validation status. The peptide model is calibrated to within 0.2% of YMC ChromaCon’s internal peptide business case (Senn Chemicals 2014 synthesis fit; “Western New” GLP-1 API price fit). Oligonucleotide constants are provisional public-literature estimates (single-strand PS ASO / GalNAc-siRNA, 2026 sources) pending a validated oligo business case. Every constant is editable in the Calibration panel.

API price. Model curve = factor × Aexp ($/g, A = kg/yr), capturing economies of scale, or a user-entered flat $/g. Generic tier applies published cost-competitive multipliers to the innovator basis. A per-modality price floor ($50/g above 1000 kg/yr) keeps the high-volume tail plausible; any point where modeled price falls below modeled cost is flagged in-chart.

Synthesis cost. 84.55 × (A/yield)−0.15 $/g (peptide, from the business case). This exponent is intentionally gentler than the −0.22 in the workbook synthesis sheets; the two agree near 100 kg/yr and diverge away from it. Synthesis dominates COGS (~70%), so productivity/CAPEX effects on the per-product P&L are modest by construction.

Availability. Two independent factors, each applied once: effective productivity (3.5 batch / 6.0 MCSGP g/L/h) already embeds a 75% within-run duty; and the calendar figure operatingDays = 320 (365 minus ~45 days/yr for maintenance and changeover) is used uniformly for multi-product sizing, campaign feasibility and maximum output.

In-process control (QC). IPCs/kg scale with column volume as base × (30/i.D.)², clamped at a 30 cm reference to prevent a non-physical reversal at small diameters (batch base 81, MCSGP 3.2 IPCs/kg; Bachem bivalirudin case).

Capital & basis. System list prices are rounded, indicative figures (CAPEX is a minor COGS component). Total equipment = TWIN system + columns. Shared once-a-year plant costs — system depreciation, the annual resin fill, and staff training — are recovered across the N products sharing the plant: a single product (products/year = 1) carries them in full; N equal products carry 1/N each. Variable costs (synthesis, solvent, disposal, IPC, plant labour) and maintenance are per product (maintenance in proportion to campaign runtime). The cost breakdown, $/g, MCSGP profit and the discounted economics (NPV, IRR, payback) are all shown per product (the profit card also prints the ×N plant total). ROI and payback are ratios and read the same per product or plant-wide; NPV is this product’s share of the incremental value. ROI, payback and NPV use total equipment (system + columns). The batch comparator is priced on a single-column prep system, not a Contichrom TWIN.

Discounted economics. NPV, IRR and discounted payback are computed on the incremental case (MCSGP vs batch): the extra equipment cost is taken at year 0, and the incremental operating cash flow (with depreciation added back, so capital is not double-counted) runs over the depreciation horizon at the chosen discount rate. Sensitivity bars show how MCSGP profit moves when API price, synthesis cost, MCSGP yield or productivity each vary ±20%.

Use. Illustrative model estimates only — not a validated tool. See the disclaimer below.

Disclaimer. This calculator is provided by YMC ChromaCon for general informational purposes only and does not constitute technical, financial, legal or regulatory advice. All figures are illustrative model estimates based on assumptions that may not reflect any specific project; actual results will vary. This is not a validated tool and must not be used as the sole basis for any investment, procurement or operational decision. To the maximum extent permitted by law, YMC ChromaCon accepts no liability for any loss or damage arising from its use. Users should make their own independent assessment and seek appropriate professional advice.
Contichrom, AutoPeak, ChromIQ and CaptureSMB are trademarks of YMC ChromaCon. AutoPeak contains patented technology. © 2026 YMC ChromaCon.
Model version 34 · constants last reviewed August 2026.
Charts rendered with Chart.js © Chart.js Contributors, used under the MIT License.
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