- 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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A:

Q: 3- What is the purpose of determining the boiling point ?

A: Purpose of determining Boiling point is-

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Q: 1. What is the importance of firing in traditional ceramic processing?

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A: Latent heat of steam=2257 kJ/kgMass flowrate of steam= 105 kg/hrThus amount of heat transffered= 225...

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Q: I have attached a formula sheet which might help.

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Q: 100 kg of a gaseous mixture occupying 80 m at 68 °F. This gas was analyzed and found to have the fol...

A:

Q: Calculate the fugacity of benzene at 100 bar and 320 K.

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Q: 2- What is the definition of boiling point ?

A: It is the temperature at which liquid changes into vapor form.

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Q: Principles of Spherical separator?

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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.