US4003822A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Main column separation of FCC product effluent
Assignee: Honeywell UOP LLC
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Filing: 1976-01-26
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Granted: 1977-01-18
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Expires: 1996-01-26
Abstract
Abstract Separation of the catalyst-containing product effluent from a fluid catalytic cracking unit is effected in the main column by a technique which involves removing a light naphtha fraction as the single overhead stream and separately withdrawing a heavy naphtha fraction as a lower side-cut. The latter is stripped of light naphtha (for recycle to the main column) and recovered as a product stream. Preferably a portion of the heavy naphtha fraction (as withdrawn) is cooled and combined with the light naphtha overhead reflux stream.
Inventors
- 👤 Hong-Kyu Jo
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 16:47
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
249 words
In a fluid catalytic cracking process, wherein a hydrocarbonaceous charge stock is converted into lower-boiling hydrocarbons in contact with finely-divided catalyst particles, the method of separating catalyst-containing, catalytically-cracked product effluent which comprises the steps of: a. introducing said product effluent into a first fractionation column through a first locus in the bottom portion thereof; b. withdrawing a light naphtha fraction from a second locus in the upper portion of said column, condensing and separating said light naphtha fraction to provide (i) a first vaporous phase and, (ii) a liquid phase; c. recycling a first portion of said liquid phase, as a reflux stream, to said first column through a third locus below said second locus, and introducing a second portion into a second fractionation column; d. separating said second portion to provide (i) a second vaporous phase and, (ii) a light naphtha product stream; e. withdrawing a heavy naphtha fraction from said first column, through a fourth locus below said third locus, and introducing at least a portion thereof into a third fractionation column; f. separating the portion of said heavy naphtha fraction to provide (i) a heavy naphtha bottoms product stream substantially free from light naphtha and, (ii) a light naphtha containing overhead stream; g. introducing at least a portion of said overhead stream into said first column through a fifth locus intermediate said third and fourth loci; and, h. withdrawing a catalyst-containing slurry oil fraction from said first column through a sixth locus below said first locus.
Claim 2
Dependent Claim
249 words
In a fluid catalytic cracking process, wherein a hydrocarbonaceous charge stock is converted into lower-boiling hydrocarbons in contact with finely-divided catalyst particles, the method of separating catalyst-containing, catalytically-cracked product effluent which comprises the steps of: a. introducing said product effluent into a first fractionation column through a first locus in the bottom portion thereof; b. withdrawing a light naphtha fraction from a second locus in the upper portion of said column, condensing and separating said light naphtha fraction to provide (i) a first vaporous phase and, (ii) a liquid phase; c. recycling a first portion of said liquid phase, as a reflux stream, to said first column through a third locus below said second locus, and introducing a second portion into a second fractionation column; d. separating said second portion to provide (i) a second vaporous phase and, (ii) a light naphtha product stream; e. withdrawing a heavy naphtha fraction from said first column, through a fourth locus below said third locus, and introducing at least a portion thereof into a third fractionation column; f. separating the portion of said heavy naphtha fraction to provide (i) a heavy naphtha bottoms product stream substantially free from light naphtha and, (ii) a light naphtha containing overhead stream; g. introducing at least a portion of said overhead stream into said first column through a fifth locus intermediate said third and fourth loci; and, h. withdrawing a catalyst-containing slurry oil fraction from said first column through a sixth locus below said first locus.
Claim 3
Dependent Claim
35 words
The method of claim 1 further characterized in that a portion of said withdrawn heavy naphtha fraction is cooled and combined with said reflux stream for introduction into said first column through said third locus.
Claim 4
Dependent Claim
32 words
The method of claim 1 further characterized in that said first vaporous phase is separated, at an elevated pressure, to provide (i) a third vaporous phase and, (ii) a second liquid phase.
Claim 5
Dependent Claim
20 words
The method of claim 3 further characterized in that said second liquid phase is introduced into said second fractionation column.
Claim 6
Dependent Claim
51 words
The method of claim 1 further characterized in that said second vaporous phase is condensed and separated to provide (i) a third liquid phase and, (ii) a fourth vaporous phase, and at least a portion of said third liquid phase is recycled to said second fractionation column as a reflux stream.
Claim 7
Dependent Claim
55 words
The method of claim 1 further characterized in that a light cycle oil fraction, containing heavy naphtha, is withdrawn from said first fractionation column through a seventh locus below said fourth locus, said heavy naphtha is separated therefrom and returned to said first fractionation column through an eighth locus intermediate said fourth and seventh loci.
Claim 8
Dependent Claim
38 words
The method of claim 6 further characterized in that a portion of said heavy naphtha-containing light cycle oil fraction is cooled and returned to said first fractionation column through a ninth locus intermediate said fourth and eighth loci.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-01-18 | 1980-07-19 | 1981-01-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-18 | 1984-07-19 | 1985-01-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-18 | 1988-07-19 | 1989-01-18 | $7700.00 | Window Closed / Lapsed |