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.
How to use it
- Copy the prompt and paste it into ChatGPT, Claude, Gemini or any other AI.
- Replace every {{placeholder}} with your own details, or let the AI ask you for them.
- Use the follow-ups below to go deeper.
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
- If any required information is missing, ask for it before proceeding.
- Based on the process description, identify the key selection criteria for the equipment type (e.g., reactor type, column internals, heat exchanger type).
- Perform preliminary sizing calculations using standard engineering correlations (e.g., residence time, number of theoretical stages, heat transfer area).
- Compare at least two feasible options, discussing trade-offs in efficiency, cost, and operability.
- 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?