
OLI Consortia Corrosion Simulation Program, CSP Phase
III OLI Corrosion Consortium OLI is continuing the CSP Consortium with Phase III, to help fund and steer the further development of the Corrosion Simulation Program. OLI continues to benefit greatly from a $2M award from the US Department of Commerce, under the NIST ATP Program to support this work. Included in this funding is $750,000, which is supporting essential laboratory work being carried out at The Southwest Research Institute in San Antonio, Texas. The CSP Project Vision document in our Resource Center provides substantial details concerning the projected additional features, which are being pursued for CSP as part of Phase III. Your participation in this Consortium will assure that the new technology can be applied to your most pressing applications at the earliest possible date. Phase I and II of CSP achievements 1. A comprehensive facility for producing thermodynamically-based, real solution stability diagrams for any bulk phase aqueous solution simulated by OLI in contact with almost any metal or alloy including a model for non-ideality within the alloy. 2. A general, first-principles model for general (uniform) corrosion. This model, which combines thermodynamics, kinetics and transport, has a supporting databank, which covers considerable bulk phase aqueous chemistry in contact with a growing list of alloys including most mild steels, 304, 316, and Cr13 stainless, aluminum, etc. 3. The first deliverables from our work on localized corrosion, including a model for computing repassivation potentials. 4. A full Windows implementation, Corrosion Analyzer of all of the principal facilities of CSP. Phase III CSP plans In Phase III of CSP, we plan to complete and implement our predictive model for localized corrosion. The first major deliverable occurred already, applicable to seawater chemistry in contact with selected alloys. Following the completion of our NIST ATP Project in November 2003, we are now able to expand our coverage for both the bulk solution phase as well as the alloys. In addition,
in Phase III, we will be completing an extensive roster of alloys for our model
of general corrosion. CSP Consortium benefits Consortium members would receive a number of unique benefits based upon their participation. The benefits include:
CSP III begins the 2nd of three years. You can join this group. For more information, contact OLI. Why join an OLI Consortia?
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OLI Mixed Solvent
Electrolytes OLI's new mixed solvent electrolyte (MSE) model, developed with partial support of the MSE Consortium Phase I, has already proven to be a significant advancement for chemical process simulation. The model is effective in addressing problems that, until now, could not be addressed using any commercial simulators. The continued development of the MSE model and databank promises many new benefits for industry users of the technology. OLI is continuing the MSE Consortium, via a Phase II, to help fund and steer the further development of the mixed solvent electrolyte framework and databank. OLI has benefited greatly from funding from the USDOE, which has provided about $0.5M to support this work. In addition, OLI has also benefited from industry funding through the MSE Consortium Phase I. The MSE Project Vision document in our Resource Center provides substantial details concerning
the projected additional features, which are being pursued for MSE as part of
Phase II. Your participation in this Consortium will assure
that the new technology can be applied to your most pressing applications at
the earliest possible date. Phase I of MSE achievements
Phase II MSE plans In Phase II of MSE, we plan to implement the following, based upon the level of funding we achieve and the priorities expressed by our supporters:
MSE Consortium benefits Consortium members would receive a number of unique benefits based upon their participation. The benefits include:
MSE II begins the 2nd of three years. You can join this group. For more information, contact OLI.
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