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August 22, 2026Next MaterialsOpen Access

Integrated process design and safety analysis for caprolactam production via the cyclohexanone route: Oxime reactor balancing, beckmann rearrangement, and packed bed reactor mechanical engineering

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Authors

VSVipin Kumar SharmaSRM Institute of Science and Technology

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Implication

Engineering design analysis models integrated reactor kinetics, thermal management, and mechanical vessel integrity for caprolactam synthesis, highlighting improved industrial plant safety.

Key Points

  • Develop an integrated chemical process and mechanical engineering design framework to safely model cyclohexanone oximation, Beckmann rearrangement, and reactor vessel sizing for caprolactam production.
  • Calculated continuous oxime reactor volume using first-order kinetics (rate constant of 0.096 per hour at 150–200 °C) with a 20% safety margin and quantified heat loads relative to a 25 °C datum.
  • Applied thin-walled pressure vessel theory, stress concentration factors for torispherical heads, and lug support equations under wind and operational weights for mechanical sizing.
  • Sized the agitation system using turbulent flow power number correlations to maintain uniform heat transfer and mixing.
  • Coupled continuous oximation kinetics with energy balance modeling to size thermal cooling systems capable of managing highly exothermic reaction loads.
  • Established structural specifications for reactor shell thickness, head geometry, and lug supports to ensure mechanical integrity under combined operational and wind stresses.

Cite This Study

Vipin Kumar Sharma (2026) studied this question.

synapsesocial.com/papers/6a895fe4ca7ade938187ee4dhttps://doi.org/10.1016/j.nxmate.2026.103256
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