Deepak Patil

I am currently enrolled in a PH.D program in chemical engineering at oklahoma state university in stillwater, USA, Prior to become a graduate research assistant at OSU.I Posses a master"s degree in chemical engineering from Indian Institute of technology ropar. My research focuses on various areas like catalysis, membrane separations.

• Publication, Estimation of Gas Holdup Using the Gassed to Ungassed Power Ratio of an Oxygen–Water System in a Stirred and Sparged Tank Contactor.(ACS Publications, 2020)
• Training Program, Completed Short Term Training Program on 'Unit Operations and Unit Processes' at Rashtriya Chemicals and Fertilizers. Thal , Alibagh, Raigarh., 12/27/2017

• Advanced Transport phenomena
• Advanced Chemical Engineering Thermodynamics
• Chemical Engineering Mathematics
• Advanced Chemical Reaction Engineering
• Engineering applications of Rehology
• Numerical methods For Engineers
• Hetrogeneous Catalysis and Catalytic Reactor
• Interfacial Engineering

• Teaching Assistant, CH230(Chemical Engineering Simulation Lab), Maintained and graded assessments of UG students, 08/03/2021, 10/07/2021
• Teaching Assistant, CH305 (Process Design and Economics), Maintained and graded assessments of UG students, 02/14/2021, 05/10/2021

Hydrodynamics and Mass Transfer Studies In Gas Liquid System Pertaining To LPG Sweetening, Identification Of Regimes, CSIR-Indian Institute Of Petroleum , Dehradun, 01/2019, 06/2019, Mr Sudip K Ganguly (Chief Scientist ,Chemical and Material Sciences Division ,Sweetening Area), 

The objective of this project is to study hydrodynamics and mass transfer studies in gas liquid kinetics pertaining to LPG sweetening for the identification of regimes. The total recirculation regime is known to have maximum mass transfer coefficient (KLa). It is known that gassed to ungassed power ratio(Pg/P0) is an important parameter in G-L mixing responsible for mass transfer. Accordingly, by studying the effect of impeller speed (N0) and volumetric gas flowrate (QG) on gassed to ungassed power ratio (Pg/P0) we have tried to identify various regimes. 

CO2 To Methanol Microkinetic Modelling By CATMAP Software(ongoing), Dr Arghya Banerjee(Department Of Chemical Engineering IIT Ropar)

 Basically In Co2 to methanol microkinetic Modelling , we are trying to make the model such that we get the specific catalyst for which the methanol production rate is higher, also we are studying the Degree of Rate Control in order to find the Rate Determining Step which affect the production rate of methanol.from this catmap software basically Descriptor- based analysis is a powerful tool for understanding the trends across various catalysts.