Chemical Processes


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  1. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses the isomeriser and chemical reactions within a glucose isomerase plant.

  2. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses the interactions between chemical engineering and the environment.

  3. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses energy conservation in relation to the high fructose corn syrup plant and chemical engineering.

  4. Professor Channing Robertson of the Stanford University Chemical Engineering Department gives an introductory lecture, outline, and background for the course.

  5. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses the design and function of an apheresis machine.

  6. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses scaling, focusing on dimensionless analysis.

  7. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses the functioning of a kidney dialysis machine and clinic.

  8. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses pharmacokinetics by using a virtual human body as a model.

  9. Professor Channing Robertson of the Stanford University Chemical Engineering Department continues his discussion on scaling by touching upon a pharmacokinetics problem.

  10. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses units, comparing the different methods and systems of measuring different variables.

  11. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses energy conservation in further depth, focusing on the design of heat exchangers.

  12. Professor Channing Robertson of the Stanford University Chemical Engineering Department discusses balancing equations and the conservation of mass in relation to process design.

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