Vaneric Edward Stein
Air Products & Chemicals
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Greenhouse Gas Control Technologies 7#R##N#Proceedings of the 7th International Conference on Greenhouse Gas Control Technologies 5– September 2004, Vancouver, Canada | 2005
Rodney John Allam; Colin McDonald; Vince White; Vaneric Edward Stein; Mark Simmonds
Publisher Summary This chapter discusses that the CO2 capture project (CCP) is a joint initiative to address problems of CO2 emissions that have the potential to cause climate change. Its objective is to provide significant reductions in CO2 capture and storage costs compared to existing technologies, by developing a range of technology options applied to several real world scenarios. The CCP sponsored feasibility study reported the application of oxyfuel technology on a refinery-wide basis at a typical European refinery. The chapter highlights the technical challenges and costs involved in converting process heaters and boilers to oxyfuel operation using todays commercially proven cryogenic oxygen generation technology and goes on to identify the cost reduction opportunities available from using the next generation of oxygen separation technology: ion transport membranes (ITMs). This new technology, which is integrated with gas turbines, results in a reduction of avoided CO2 cost of from 15% to 50% depending upon the level of integration with the current steam generation within the refinery site.
Carbon Dioxide Capture for Storage in Deep Geologic Formations#R##N#Results from the CO2 Capture Project | 2005
Rodney John Allam; Vince White; Vaneric Edward Stein; Colin McDonald; Neil Ivens; Mark Simmonds
This chapter presents ion transport membranes (ITM) oxygen process, which is based on ceramic membranes that selectively transport oxygen ions when operated at high temperatures. Under the influence of an oxygen partial pressure driving force, the ITM achieves a high flux, high purity (99+ mol%) separation of oxygen from a compressed-air stream. By integrating the non-permeate stream with a gas turbine system, the overall process co-produces high purity oxygen, power, and steam if desired. The chapter investigates three cases; the base case is presented and costed and involves the supply of the complete oxyfuel system with installation and startup and includes all required utilities. In order to provide the hot air for the ITM oxygen process, two Siemens V94.2 combined cycle gas turbines are used and excess power is exported to the local electricity grid. Other cases also use two Siemens V94.2 gas turbines plus a heat recovery steam generator (HRSG) for producing steam.
Archive | 2007
Vaneric Edward Stein; Michael Francis Carolan; Christopher M. Chen; Phillip Andrew Armstrong; Harold W. Wahle; Theodore R. Ohrn; Kurt E. Kneidel; Keith Gerard Rackers; James Erik Blake; Shankar Nataraj; Rene Van Doorn; Merrill Anderson Wilson
Archive | 2012
John Michael Repasky; Michael Francis Carolan; Vaneric Edward Stein; Christopher M. Chen
Archive | 2004
Phillip Andrew Armstrong; James Eric Blake; Michael Francis Carolan; Christopher M. Chen; Kurt E. Kneidel; Shankar Nataraj; Theodore R. Ohrn; Keith Gerard Rackers; Vaneric Edward Stein; Doorn Rene Hendrik Elias Van; Harold W. Wahle; Merrill Anderson Wilson
Archive | 2001
Vaneric Edward Stein; Robin Edward Richards; David Douglas Schnecksville Brengel; Michael Francis Carolan
Archive | 2012
John Michael Repasky; Lori L. Anderson; Vaneric Edward Stein
Archive | 2011
Lori L. Anderson; Phillip Andrew Armstrong; John Michael Repasky; Vaneric Edward Stein
Archive | 2001
Robin Edward Richards; Peter R. Armstrong; Michael Francis Carolan; Vaneric Edward Stein; Richard Cutler; John Gordon; David M. J. Taylor
Archive | 2014
William S. Rollins; Vaneric Edward Stein