- The operating conditions were 25 °C, 1 atm for the diffusing of Oxygen through a non- diffusing water. The equilibrium equation: y 1.4 x, the individual mass transfer coefficient of the gas phase Kc and the bulk gas concentration are (1.15*10$ kmol/s.m2, 0.6) respectively. The individual mass transfer coefficient of the liquid phase KL and the bulk liquid concentration are (1.32*105 kmol/s.m2, 0.15) respectively. Find the interface concentration in gas and liquid phase and then find the percent resistance in liquid phase.

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Hazard Analysis and Design in Chemical Engineering

Hazard is the intrinsic property of a material or process which harms the people, buildings, or environment. Health, safety, hazard, risk assessment, loss prevention, and environmental consideration play an important role while designing a chemical processing plant. Hazard is often confused with risk. Risk measures the magnitude of loss and injury of likelihood incidents or the consequence and frequency of incidents.