US4579563A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for fluidizing coal tar sludge
Assignee: Individual
•
Filing: 1985-04-15
•
Granted: 1986-04-01
•
Expires: 2005-04-15
Abstract
Abstract A method and apparatus fluidizes solid deposits of coal tar sludge, such as coal tar decanter sludge or coal tar tank sludge to a relatively homogeneous mixture of solids dispersed in liquid. The coal tar decanter sludge received from the coke oven, including approximately 10 to 50% by weight coal and coke solids, is conveyed into a sludge mixing vessel where it is deposited onto a liquid-permeable support member or screen having a predetermined maximum screen size. A suitable coal tar solvent in the sludge mixing vessel is heated to a temperature sufficient to partially solubilize and reduce the viscosity of the coal tar portion of the coal tar decanter sludge to provide a pumpable dispersion of solids dispersed in a diluted coal tar mixture. Agglomerates of coal and coke solids held together with coal tar fall through the screen when sufficient coal tar has solubilized and the solid agglomerates then are reduced in size for recirculation to the sludge mixing vessel. The diluted coal tar mixture is pumped to recirculate it to the sludge mixing vessel after impacting and shearing the solid agglomerates to reduce the solids particle size.
Inventors
- 👤 Kenneth D. Burnside
- 👤 Daniel C. Deer, III
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 20:44
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/32; C10L1/322
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
210 words
A method of fluidizing solid agglomerates of coal tar sludge, comprising solid particles of coal and/or coke adhered together with coal tar, into a relatively homogeneous form comprising: depositing solid agglomerates of coal tar sludge onto a liquid-permeable screen within a sludge mixing vessel; contacting the coal tar sludge in the mixing vessel with a liquid diluent capable of and in an amount sufficient for fluidizing a portion of the coal tar sludge at elevated temperature reducing the viscosity of the sludge sufficiently to form a diluted coal tar sludge mixture capable of pumping for recirculation; heating the diluted coal tar sludge mixture to a temperature sufficient to fluidize a portion of the coal tar sludge and to reduce the viscosity of the diluted coal tar sludge mixture to a degree sufficient for recirculation through a pump; impacting solid agglomerates of the diluted coal tar sludge to physically break agglomerates in the diluted mixture, to reduce the particle size of the agglomerates to a degree sufficient to pass through a pump for recirculation, and to increase the contact area of the solid agglomerages with the liquid diluent; conveying the diluted coal tar sludge mixture through said pump; and recirculating the diluted mixture from the pump to the sludge mixing vessel.
Claim 2
Independent Claim
210 words
A method of fluidizing solid agglomerates of coal tar sludge, comprising solid particles of coal and/or coke adhered together with coal tar, into a relatively homogeneous form comprising: depositing solid agglomerates of coal tar sludge onto a liquid-permeable screen within a sludge mixing vessel; contacting the coal tar sludge in the mixing vessel with a liquid diluent capable of and in an amount sufficient for fluidizing a portion of the coal tar sludge at elevated temperature reducing the viscosity of the sludge sufficiently to form a diluted coal tar sludge mixture capable of pumping for recirculation; heating the diluted coal tar sludge mixture to a temperature sufficient to fluidize a portion of the coal tar sludge and to reduce the viscosity of the diluted coal tar sludge mixture to a degree sufficient for recirculation through a pump; impacting solid agglomerates of the diluted coal tar sludge to physically break agglomerates in the diluted mixture, to reduce the particle size of the agglomerates to a degree sufficient to pass through a pump for recirculation, and to increase the contact area of the solid agglomerages with the liquid diluent; conveying the diluted coal tar sludge mixture through said pump; and recirculating the diluted mixture from the pump to the sludge mixing vessel.
Claim 3
Dependent Claim
10 words
The method of claim 1 including shearing the solid agglomerates.
Claim 4
Dependent Claim
25 words
The method of claim 1 including shearing the agglomerates by rotating an impeller blade closely adjacent fluid openings in an outlet side of the pump.
Claim 5
Dependent Claim
20 words
The method of claim 1 wherein the fluidized liquid is heated to a temperature of 130° F. to 250° F.
Claim 6
Dependent Claim
18 words
The method of claim 3 including impacting the agglomerates by contacting the agglomerates with a rotating impact blade.
Claim 7
Dependent Claim
18 words
The method of claim 5 including rotating the impact blade and the impeller blade at the same speed.
Claim 8
Dependent Claim
23 words
The method of claim 6 including rotating the impact blade and the impeller blade at a speed of 1100 R.P.M. to 1800 R.P.M.
Claim 9
Dependent Claim
17 words
The method of claim 1 wherein the liquid diluent is a naptha derived from refining crude oil.
Claim 10
Dependent Claim
20 words
The method of claim 1 wherein the liquid diluent is an aromatic solvent having a flash temperature of 150°-250° F.
Claim 11
Dependent Claim
14 words
The method of claim 1 wherein the coal tar sludge comprises tar decanter sludge.
References Cited (Backward Citations)
US1390232A
Cited
US4149854A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-03-31 | 1989-09-30 | 1990-04-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-03-31 | 1993-09-30 | 1994-04-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-03-31 | 1997-09-30 | 1998-04-01 | $7700.00 | Window Closed / Lapsed |