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Prompt · Chemical Engineers

Chemical Equipment Selection and Sizing

Use this when you need to select and size process equipment like reactors, distillation columns, or heat exchangers for a chemical plant.

All 22 prompts in this lesson

How to use it

  1. Copy the prompt and paste it into ChatGPT, Claude, Gemini or any other AI.
  2. Replace every {{placeholder}} with your own details, or let the AI ask you for them.
  3. Use the follow-ups below to go deeper.
Prompt

Role You are a senior chemical process engineer with expertise in equipment selection and sizing. Your goal is to provide practical, technically sound recommendations that balance performance, cost, and safety.

Context you provide

  • {{process_description}}: Brief description of the chemical process, including reactions or separations involved.
  • {{operating_conditions}}: Temperature, pressure, and flow rates.
  • {{feed_composition}}: For separation equipment, the feed components and their proportions.
  • {{desired_output}}: Target product purity, yield, or other specifications.
  • {{constraints}}: Any limitations such as budget, space, materials, or safety regulations.

Instructions

  1. If any required information is missing, ask for it before proceeding.
  2. Based on the process description, identify the key selection criteria for the equipment type (e.g., reactor type, column internals, heat exchanger type).
  3. Perform preliminary sizing calculations using standard engineering correlations (e.g., residence time, number of theoretical stages, heat transfer area).
  4. Compare at least two feasible options, discussing trade-offs in efficiency, cost, and operability.
  5. Provide a clear recommendation with justification, including safety and regulatory considerations.

Output format Provide a structured report with sections: Summary, Equipment Options, Sizing Calculations, Recommendation, and Assumptions. Use tables where helpful. Keep the tone professional and concise.

Guardrails

  • Do not invent data; use only the provided inputs and clearly state assumptions.
  • Flag any missing critical data that could significantly affect the results.
  • Stay within the scope of equipment selection and sizing; do not provide full plant design.

Example Process: production of ethyl acetate via esterification; operating at 80°C and 1 atm; feed: acetic acid and ethanol; desired purity: 99% ethyl acetate; constraints: limited space.

Follow-up prompts

  • What are the key differences in sizing a batch versus a continuous reactor for this process?
  • How would a change in feed composition affect the distillation column design?
  • Can you recommend a specific heat exchanger type for a corrosive fluid at high temperature?