# US 4,395,325 A · Reducing sulfur trioxide concentration in regeneration zone flue gas

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- Number: US 4,395,325 A
- Document ID: US4395325A
- Status: Granted
- Kind: A
- Application number: 06/298,404
- Filed: 1981-09-01
- Granted: 1983-07-26
- Earliest claimed: 1981-09-01
- Assignees: Mobil Oil Corporation
- Inventors: Stephen J. McGovern; Peter J. Owens; Michael J. Dolan
- Web page: https://patentgrep.com/patent/US4395325A

## CPC

- C10G 11/187: {Controlling or regulating}
- Y10S 208/01: Automatic control
- C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

Sulfur trioxide concentration in the flue gas of catalytic cracking regenerators is maintained at a predetermined level by controlling the flow rate of oxygen-containing regeneration gas into the regenerator, and, optionally, the amount of carbon monoxide combustion promoter in the regenerator.

## Claims

### Claim 1

In a catalytic cracking process comprising:
contacting a hydrocarbonaceous feed with a cracking catalyst to produce cracked hydrocarbon vapors and deactivated catalyst containing carbonaceous deposits;
separating the deactivated catalyst from the hydrocarbon vapors and conducting the deactivated catalyst to a regeneration vessel;
at least partially removing the carbonaceous deposits from the deactivated catalyst in the regeneration vessel by means of an oxygen-containing gas introduced into the regeneration vessel, thereby forming a flue gas comprising oxygen, sulfur dioxide, sulfur trioxide, carbon monoxide and carbon dioxide;
the improvement which comprises monitoring the sulfur trioxide and the oxygen concentration in the flue gas from the regeneration vessel; and
adjusting the amount of the oxygen-containing gas in the regeneration vessel in relation to the concentration of the sulfur trioxide to maintain the concentration by volume of the sulfur trioxide in the flue gas such that the ratio SO.sub.3 /SO.sub.x in the flue gas is less than 5%, thereby preventing the appearance of a visible condensation plume in the flue gas.

### Claim 2 (depends on 1)

A process according to claim 1 wherein the cracking catalyst also contains a carbon monoxide combustion promoter.

### Claim 3 (depends on 2)

A process according to claim 2 wherein the amount of the carbon monoxide combustion promoter is also adjusted to maintain the concentration by volume of the SO.sub.3 in the flue gas such that the ratio SO.sub.3 /SO.sub.x in the flue gas is less than 5%, thereby preventing the appearance of a visible condensation plume in the flue gas.

### Claim 4 (depends on 3)

A process according to claim 3 wherein the concentration of oxygen in the flue gas is about 0.0 to 1% by mole.

### Claim 5 (depends on 4)

A process according to claim 4 wherein the carbon monoxide combustion promoter is selected from the group consisting of Pt, Pd, Rh, Ir, Os and Re.

### Claim 6 (depends on 5)

A process according to claim 5 wherein the carbon monoxide combustion promoter is Pt.

### Claim 7 (depends on 5)

A process according to claims 5 of 6 wherein the amount of the combustion promoter in the regeneration vessel is about 0 to about 2 parts per million by weight of elemental metal, based on the total weight of the catalyst.

### Claim 8 (depends on 7)

A process according to claim 7 wherein the amount of the combustion promoter in the regeneration vessel is about 0.1 to about 1 parts per million by weight of elemental metal, based on the total weight of the catalyst.

### Claim 9 (depends on 8)

A process according to claim 8 wherein the concentration of oxygen in the flue gas is less than 0.5% by mole.