SYNOPSIS – Synthesis of Operable Process Intensification

This project looks to achieve the aggressive goal of discovering potential MCPI process configurations that are both safe and operable based on using existing modeling approaches. The team will link together and expand upon existing modeling tools that are in various stages of development to create an environment that can define potential MCPI solutions without needing to define potential process schemes. This approach to process synthesis is high risk, but could create unanticipated and highly valuable solutions.

Investigators

Stratos Pistikopoulos
Director, Texas A&M Energy Institute Professor and Dow Chemical Chair, Department of Chemical Engineering

Date approved

November 01, 2017
Current TRL
3

Modular Mechanical Vapor Compression-Membrane Distillation (MVC-MD) for Treatment of High TDS Produced Water

This projects aims to integrate mechanical vapor compression with membrane distillation (MVC-MD) to intensify the treatment of produced water resulted from hydraulic fracturing of shale oil and gas. In particular, membrane distillation offers a viable pathway to treat concentrated brine streams with high salinity brines, and it has the potential to be utilized for near-zero liquid discharge. However, MD in its current state is handicapped by significant energy intensity due to loss of heat of evaporation, and scaling (fouling).

Investigators

Mahdi Malmali
Assistant professor of Chemical Engineering

Date approved

July 01, 2018
Current TRL
6

RAPID MCPI - Energy Efficient Technology for Metals Separation

This project addresses the demonstration of a low-cost and low-energy pathway for the separation of metals from mixed scrap based on ionic liquids. The goal of the project is to develop and demonstrate a novel electrochemical process for the separation of metals from mixed scrap using ionic liquids (ILs) at low temperatures.

Investigators

Ramana Reddy
Professor of Metallurgical and Materials Engineering

Date approved

November 01, 2017
Current TRL
5

Multiphase Microchannel Separator

In conventional two-phase separation, mass transport between the two phases can be intensified via increased surface area, usually in the form of smaller droplets or bubbles. The increase in the interfacial surface area typically results in higher energy cost due to agitation or mixing and slower processing time as the smaller droplet phase requires more time to separate. One can increase processing speed in centrifugal extractors but this, in turn, increases energy requirements significantly.

Investigators

Goran Jovanovic
Professor, Chemical Engineering

Partner Organizations

Oregon State University

Date approved

November 01, 2017
Current TRL
4

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