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| HCN and NOx control strategies in the FCC |
Xunhua Mo, Bart De Graaf, Charles Radcliffe and Paul Diddams, Johnson Matthey, Process Technologies, Intercat Additives |
2014 / Catalysis |
Results of resesarch into emissions from the FCC, plus guidance on how to obtain the minimum level of NOx
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| Capturing maximum value with tight oil feeds in the FCC |
Alexis Shackleford, BASF Catalysts |
2014 / Catalysis |
FCCs processing tight oil feeds require catalyst choices to deal with higher conversion, heat balance concerns, and higher sodium, calcium and iron
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| Maximising distillate while minimising bottoms |
Allen Hansen, Adrian Humphries, Stephen McGovern and Barry Speronello, Rive Technology Inc |
2014 / Catalysis |
An FCC catalyst with reduced resistance to diffusion raises diesel output without the traditional bottoms penalty
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| Dewaxing challenging paraffinic feeds |
Renata Szynkarczuk, Criterion Catalysts & Technologies
Michelle Robinson and Laurent Huve, Shell Global Solutions International |
2014 / Catalysis |
Catalytic dewaxing using recent developments in dewaxing catalysts provides an alternative method for cold flow improvement in diesel and lube oil
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| Maximising distillate and alkylation feed from the FCC |
Alan Kramer, George Yaluris, Albemarle Corporation |
2014 / Catalysis |
The tight oil revolution has changed FCC priorities. Operators can maximise profitability by adopting new catalysts to target their yield profile
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| Optimising hydroprocessing catalyst systems |
Woody Shiflett, Charles Olsen, Dan Torchia, Advanced Refining Technologies
David Brossard, Chevron Lummus Global |
2014 / Catalysis |
Flexibility in catalyst technology and processing tactics optimises hydrocracker and ULSD operations to meet diesel and gasoil production targets
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