US4643709A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of operating nozzle centrifuges
Assignee: Alfa Laval Inc
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Filing: 1985-05-01
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Granted: 1987-02-17
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Expires: 2005-05-01
Abstract
Abstract In centrifuges for separating solids-liquid slurries and which discharge concentrated solids through nozzles at the periphery of the centrifugal bowl or rotor, it is necessary to maintain a feed or influent rate at least as great as the nozzle discharge rate. According to the present invention, this is accomplished by driving from the centrifuge drive train a pumping means for returning concentrated solids from the nozzles to the centrifuge for recycling through the bowl.
Inventors
- 👤 Chie-Ying Lee
- 👤 James D. West
- 👤 Gerald F. Cole
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 20:01
CPC Classifications
B; B04; B04B; B04B1/00; B04B1/10; B04B1/14
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
123 words
In the operation of a nozzle-type centrifuge for the separation of a slurry into a concentrated solids component and an effluent component, the centrifuge including a centrifugal rotor, the method which comprises feeding said slurry to the rotor while driving the rotor through a drive train to effect said separation, separately discharging said components from the rotor, said concentrated solids component being discharged through nozzles at the peripheral portion of the rotor, recycling a stream of concentrated solids through the rotor from said nozzles by way of a return line including pumping means, and driving said pumping means from said drive train, whereby the rate of driving said pumping means is maintained directly proportional to the rate at which the rotor is driven.
Claim 2
Dependent Claim
123 words
In the operation of a nozzle-type centrifuge for the separation of a slurry into a concentrated solids component and an effluent component, the centrifuge including a centrifugal rotor, the method which comprises feeding said slurry to the rotor while driving the rotor through a drive train to effect said separation, separately discharging said components from the rotor, said concentrated solids component being discharged through nozzles at the peripheral portion of the rotor, recycling a stream of concentrated solids through the rotor from said nozzles by way of a return line including pumping means, and driving said pumping means from said drive train, whereby the rate of driving said pumping means is maintained directly proportional to the rate at which the rotor is driven.
Claim 3
Dependent Claim
21 words
The method of claim 1, in which the pumping means are driven from said drive train through a belt and pulley.
Claim 4
Dependent Claim
40 words
The method of claim 1, comprising also withdrawing concentrated solids from said return line during said recycling, and controlling the rate of said withdrawing to maintain a substantially constant concentration of solids in said solids component discharged from the nozzles.
Claim 5
Dependent Claim
65 words
The method of claim 3, in which the rate of said withdrawing is controlled by decreasing the recycling rate in response to an increase in the concentration of solids discharged through said nozzles, thereby increasing the rate of said withdrawing, and by increasing the recycling rate in response to a decrease in the concentration of said discharged solids, thereby decreasing the rate of said withdrawing.
Claim 6
Dependent Claim
26 words
The method of claim 4, in which said withdrawing is effected by discharging concentrated solids over a weir from a container included in said return line.
Claim 7
Dependent Claim
37 words
The method of claim 1, comprising also withdrawing concentrated solids from said return line during said recycling, said withdrawing being effected by discharging concentrated solids over a weir from a first container included in the return line.
Claim 8
Dependent Claim
51 words
The method of claim 6, comprising also passing effluent discharged from the rotor into a second container during said recycling while withdrawing effluent from the second container, causing effluent to overflow said second container while discontinuing said effluent withdrawing, and passing overflowing effluent from said second container to said return line.
Claim 9
Dependent Claim
21 words
The method of claim 7, in which said overflowing effluent is passed to the return line downstream from said first container.
Claim 10
Dependent Claim
21 words
The method of claim 1, comprising also directing effluent from the rotor into said return line during start-up of the centrifuge.
Claim 11
Dependent Claim
21 words
The method of claim 1, comprising also directing effluent from the rotor into said return line during shut-down of the centrifuge.
Claim 12
Dependent Claim
19 words
The method of claim 1, comprising also injecting a flushing liquid into said return line to displace solids therefrom.
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) | 1990-02-16 | 1990-08-18 | 1991-02-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-02-16 | 1994-08-18 | 1995-02-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-02-16 | 1998-08-18 | 1999-02-17 | $7700.00 | Window Closed / Lapsed |