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U.S. Department of Energy
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Reducing NO sub x emissions from FCC regenerators by segregated cracking of feed

Patent ·
OSTI ID:6024222
This patent describes improvement in a fluidized catalytic cracking process wherein a fresh feed mixture of high and low nitrogen containing hydrocarbon feeds contact a source of hot regenerated catalyst in the base of a riser cracking reactor means to produce catalytically cracked products and spent catalyst containing coke contaminated with nitrogen compounds, wherein the spent catalyst is stripped in a catalyst stripping means to produce stripped catalyst which is regenerated in a catalyst regeneration means to produce a regenerated catalyst which is recycled to the cracking reactor means, and wherein a flue gas comprising nitrogen oxides (NO{sub {ital x}}) is withdrawn from the regenerator. The improvement comprises: segregating the fresh feed mixture into at least two different fresh feed fractions having different nitrogen contents, the segregated feed fractions comprising a low nitrogen content fresh feed and a high nitrogen content fresh feed having at least a 50% greater concentration of nitrogen than the low nitrogen content fresh feed, adding the high nitrogen content fresh feed via a feed addition means at an elevation in the base of the riser reactor, and separately adding the low nitrogen content fresh feed to the riser reactor at a higher elevation in the riser reactor and downstream of the point of addition of the high nitrogen content fresh feed, whereby the NO{sub {ital x}} content of the flue gas is reduced relative to operation with a feed comprising a mixture of the high and the low nitrogen containing feedstocks.
Assignee:
Mobil Oil Corp., Fairfax, VA (USA)
Patent Number(s):
A; US 4985133
Application Number:
PPN: US 7-479308
OSTI ID:
6024222
Country of Publication:
United States
Language:
English