US4686048A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for treating cat cracker bottoms sludge
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1981-12-23
•
Granted: 1987-08-11
•
Expires: 2001-12-23
Abstract
Abstract A process is disclosed for treating cat cracker bottoms sludge to remove the cat cracker bottoms hydrocarbons from the catalyst fines in the sludge to provide treated fines which are environmentally safe for landfill. The process involves mixing the sludge with a hydrocarbon diluent, separating the fines from the diluent-sludge mixture, then mixing the separated fines and remaining diluent with water and distilling off the remaining diluent to obtain the treated fines.
Inventors
- 👤 George A. Atherton
- 👤 Ghazi B. Dickakian
- 👤 Edward D. Grant, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 11:11
CPC Classifications
C; C10; C10G; C10G31/00; C10G31/09; C10G55/00; C10G55/02; C10G55/06
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
169 words
A process for treating cat cracker bottoms sludge to remove the cat cracker bottoms hydrocarbons from the catalyst fines in the sludge which comprises: mixing the cat cracker bottoms sludge with a liquid hydrocarbon diluent selected from the group consisting of heptane, benzene and toluene which have azeotropic boiling points with water of 150° F. to 210° F.; separating the fines from the diluent-sludge mixture by filtration and washing the fines with additional diluent in an amount of 20% to 500% by weight of said hydrocarbons in said sludge; mixing the separated fines and remaining diluent with water in an amount of 250% to 700% by weight of said separated fines and diluent remaining in said fines said mixing being conducted at a temperature below the boiling point of the diluent and within the range of ambient of 210° F.; and removing the remaining diluent by distillation of the fines, diluent and water to obtain the treated fines which have a hydrocarbon content of less than 5% by weight.
Claim 2
Dependent Claim
169 words
A process for treating cat cracker bottoms sludge to remove the cat cracker bottoms hydrocarbons from the catalyst fines in the sludge which comprises: mixing the cat cracker bottoms sludge with a liquid hydrocarbon diluent selected from the group consisting of heptane, benzene and toluene which have azeotropic boiling points with water of 150° F. to 210° F.; separating the fines from the diluent-sludge mixture by filtration and washing the fines with additional diluent in an amount of 20% to 500% by weight of said hydrocarbons in said sludge; mixing the separated fines and remaining diluent with water in an amount of 250% to 700% by weight of said separated fines and diluent remaining in said fines said mixing being conducted at a temperature below the boiling point of the diluent and within the range of ambient of 210° F.; and removing the remaining diluent by distillation of the fines, diluent and water to obtain the treated fines which have a hydrocarbon content of less than 5% by weight.
Claim 3
Dependent Claim
34 words
Process of claim 1 further comprising prior to mixing the sludge with diluent, concentrating the catalyst fines in the cat cracker bottoms by settling the fines and drawing off the cat cracker bottoms hydrocarbons.
Claim 4
Dependent Claim
32 words
Process of claim 2 wherein the cat cracker bottoms sludge has an ash content of about 10% to 40% by weight and a hydrocarbon content of about 60% to 90% by weight.
Claim 5
Dependent Claim
58 words
Process of claim 3 wherein the treated fines have a catalyst fines content of at least about 55% by weight, a hydrocarbon content of up to 5% by weight, and a water content of up to about 40% by weight, and wherein at least 95% by weight of the cat cracker bottoms hydrocarbons are removed from the sludge.
Claim 6
Dependent Claim
9 words
Process of claim 4 wherein the diluent is heptane.
Claim 7
Dependent Claim
15 words
Process of claim 5 further comprising separating the fines from the water slurry after distillation.
Claim 8
Dependent Claim
15 words
Process of claim 6 wherein the fines are separated from the water slurry by filtration.
Claim 9
Dependent Claim
24 words
Process of claim 5 wherein the diluent when combined with water has a boiling point within the range of 150° F. to 210° F.
Claim 10
Dependent Claim
13 words
Process of claim 5 further comprising adding an antifoaming agent to the slurry.
Claim 11
Dependent Claim
21 words
Process of claim 1 wherein the water in the form of steam is mixed with the separated fines and remaining diluent.
Claim 12
Dependent Claim
26 words
Process of claim 10 wherein the amount of steam is within the range of 3% to 25% by weight of the separated fines and remaining diluent.
Claim 13
Dependent Claim
60 words
Process of claims 6 or 11 wherein the treated fines have a catalyst fines content of at least about 65% by weight, a hydrocarbon content of up to about 2% by weight and a water content of up to 35% by weight, and wherein at least 99% by weight of the cat cracker bottoms hydrocarbons are removed from the sludge.
Claim 14
Dependent Claim
17 words
Process of claim 12 wherein the diluent is selected from the group consisting of n-heptane and toluene.
Claim 15
Dependent Claim
20 words
Process of claim 1 further comprising adding a separation aid to the diluent-sludge mixture which accelerates separation of the fines.
Claim 16
Dependent Claim
27 words
Process of claim 1 further comprising prior to mixing the sludge with the diluent, concentrating the catalyst fines in the cat cracker bottoms sludge by dielectrophoretic separation.
Claim 17
Dependent Claim
30 words
Process of claim 1 further comprising recovering and isolating from each other the water, the diluent, and the cat cracker bottoms hydrocarbons which were separated and distilled from the fines.
References Cited (Backward Citations)
US3696021A
Cited
US3692668A
Cited
US3835021A
Cited
US4123357A
Cited
US4206001A
Cited
US4260489A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-08-10 | 1991-02-09 | 1991-08-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-08-10 | 1995-02-09 | 1995-08-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-08-10 | 1999-02-09 | 1999-08-11 | $7700.00 | Window Closed / Lapsed |