About this document
Distillation Column Design Calculations by mynurul is a document available to read on EtoBox.
This document discusses estimating dew point and bubble point using Excel to determine the feasibility of distillation. It calculates the dew point of the distillate to be 79.05°C and bubble point of the bottom product to be 119.67°C at a system pressure of 20 kPa. Using equations from a textbook, it determines the minimum theoretical number of stages required is 21 to produce 75,000 metric tons/year of cyclohexanol.
- Author
- mynurul
- Language
- EN