Mike Resetarits holds a bachelor's degree and master's degree in chemical engineering, and also an MBA. Before joining FRI, he worked for Union Carbide, UOP and Koch-Glitsch. Thus far, most of his career was spent doing separations design and research, particularly in the field of distillation, absorption and extraction. In his nearly 40 years in the field, he has been awarded 17 distillation equipment patents. He has authored over 60 separation-related papers.

24 Posts in 20 Topics by 2 members

Topic Posts Last Post
What is the most lean and effective means of concentrating a contaminated spent acid solution of acetic acid and water from 28% to 48%? 4 May 2016 by Anonymous CP Reader 2
How can we increase the rate of vacuum distillation? 26 August 2014 by Anonymous CP Reader 2
Why is the bottom distillation column temperature too high? 10 June 2014 by Anonymous CP Reader 2
What are essential parameters of a multi-pressure distillation system? 26 March 2009 by Michael R. Resetarits 2
Solving Problems with Vacuum Distillation Systems 13 April 2009 by Michael R. Resetarits 2
Why don't ethanol producers use multiple effect distillation to remove ethanol from fermentation broth? 24 June 2009 by Michael R. Resetarits 2
Is vacuum distillation best to recover iso amyl alcohol and manufacturing esters? 19 April 2011 by Michael R. Resetarits 2
Is there a guideline for setting the height of the conical section of a column? 7 December 2011 by Michael R. Resetarits 1
Is there a good way to calculate the height of stage in a distillation column? 6 May 2010 by Michael R. Resetarits 1
How do I calculate the void space in a column? 30 November 2009 by Michael R. Resetarits 1