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U.S. Department of Energy
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Catalytic cracking process with isolated catalyst for conversion of NOx in FCC regenerator

Patent ·
OSTI ID:5676843
This patent describes improvement in a process for the catalytic cracking of a nitrogen-containing hydrocarbon feed to lighter products by contacting the feed with a supply of hot, regenerated cracking catalyst in a fluidized catalytic cracking (FCC) reactor means to produce cracked products and spent cracking catalyst containing nitrogen compounds, wherein the spent cracking catalyst is regenerated in a catalyst regeneration means by contact with oxygen or an oxygen-containing gas at catalyst regeneration conditions to produce hot regenerated cracking catalyst and regenerator flue gas containing nitrogen oxides (NO{sub x}). The improvement comprises: reducing the amount of NO{sub x} in the flue gas by adding to the catalyst regeneration means a catalytically effective amount of a DeNO{sub x} catalyst in an amount sufficient to reduce the NO{sub x} content of the flue gas and in a form whereby the DeNO{sub x} catalyst has an extended residence time in the regenerator relative to the cracking catalyst.
Assignee:
Mobil Oil Corp., Fairfax, VA (USA)
Patent Number(s):
US 5037538; A
Application Number:
PPN: US 7-484989
OSTI ID:
5676843
Country of Publication:
United States
Language:
English