📋 Case Study

Small-Scale Analytical Process Monitoring Implementation

High batch-to-batch variability (>8% CV in crystal size distribution) due to undetected supersaturation excursions and delayed feedback from offline HPLC analysis (45–90 min lag), leading to rework of ~12% of production runs.

🏗️ Project Overview

A specialty chemical manufacturer in Dayton, Ohio implemented real-time analytical process monitoring on a pilot-scale continuous crystallization unit (0.5 m³ reactor volume) producing pharmaceutical-grade sodium citrate. The project spanned 12 weeks and involved integration of inline Raman spectroscopy, temperature/pressure sensors, and a compact edge-computing platform.

🎯 Challenge

High batch-to-batch variability (>8% CV in crystal size distribution) due to undetected supersaturation excursions and delayed feedback from offline HPLC analysis (45–90 min lag), leading to rework of ~12% of production runs.

🔧 Design Approach

Model-based multivariate statistical process control (MSPC) using partial least squares regression (PLSR) calibrated against reference HPLC and laser diffraction data; deployed via ISA-88/ISA-95 compliant modular architecture with OPC UA communication to existing DCS.

📐 Design Diagram

Challenge• ΔCV >8% in CSD• 45–90 min HPLC lag• 12% reworkControl LoopPM = 63°τ_max = 187 msPLSRModelOPC UAISA-88/95DCSLegacyΔS_min = 0.022 g/g(Raman 1025 cm⁻¹)SensorArray

AI-generated project design illustration

📐 Key Calculations

Minimum detectable supersaturation shift

ΔS_min = (3 × σ_noise) / |∂Raman_1025cm⁻¹/∂S|
Result: 0.022 g/g solvent
Enabled detection of nucleation onset 92 seconds earlier than prior methods, reducing uncontrolled growth periods.

Control loop stability margin (phase margin)

PM = 180° + ∠G(jω_c) where ω_c is crossover frequency
Result: 63°
Ensured robust closed-loop response under variable feed concentration (±15%) without oscillation or instability.

Data synchronization latency budget

τ_max = T_sample − (t_proc + t_comm)
Result: 187 ms
Guaranteed sub-second end-to-end monitoring cycle (target: ≤250 ms), critical for capturing transient metastable zone width events.

📊 Results

Metrics: Crystal size distribution CV reduced from 8.3% to 2.1%, Offline assay dependency decreased by 94%, Mean time to corrective action reduced from 6.8 min to 42 s
The system achieved real-time, predictive control of crystallization kinetics, eliminating off-spec batches and saving $210K annually in rework and analytical labor.

💡 Lessons Learned

  • Calibration transfer between lab and inline Raman probes required daily water-peak normalization due to thermal lensing drift
  • Operator acceptance increased only after co-designing intuitive alarm dashboards with color-coded supersaturation zones

Key Takeaways

  • 1Small-scale analytical monitoring succeeds when sensor fidelity, control theory, and human factors are co-optimized—not just instrumented