Patent US4312701A successfully refreshed from Google Patents.
US4312701A
Expired / Lapsed
US
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Method for defibrating waste paper and dispersing contaminants
Assignee: HYDRO-THERMAL Corp MILWAUKEE WIS A CORP OF WIS
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Filing: 1980-11-07
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Granted: 1982-01-26
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Expires: 2000-11-07
Abstract
Abstract A method for defibrating waste paper and dispersing contained asphalt and wax contaminants within the fibers. The waste paper is initially pulped with water and the resulting stock is then contacted with a high pressure stream of steam having a velocity in the range of 1200 to 1600 ft./sec. The mixture of steam and stock is passed through a mixing tube under highly turbulent conditions to defibrate the waste paper and disperse any asphalt, waxes, and other contaminants throughout the separated fibers. The resulting stock can be used in papermaking processes, particularly for the production of paperboard products.
Inventors
- 👤 Robert Campbell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 12:22
CPC Classifications
D; D21; D21B; D21B1/00; D21B1/04; D21B1/12; D21B1/30; D21B1/32; Y; Y02; Y02W; Y02W30/00; Y02W30/50; Y02W30/64
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
88 words
A method of defibrating waste paper and dispersing contained contaminants within the dispersed fibers, comprising the steps of contacting an aqueous stock of waste paper having a fibrous solids content of 1% to 5% by weight with steam at a pressure in excess of 20 psig and at a velocity of 1,200 to 1,600 ft./sec. to provide a steam-stock mixture, and flowing the mixture through a mixing tube under highly turbulent conditions to thereby heat the stock, separate the fibers of the stock and disperse any contained contaminants.
Claim 2
Independent Claim
88 words
A method of defibrating waste paper and dispersing contained contaminants within the dispersed fibers, comprising the steps of contacting an aqueous stock of waste paper having a fibrous solids content of 1% to 5% by weight with steam at a pressure in excess of 20 psig and at a velocity of 1,200 to 1,600 ft./sec. to provide a steam-stock mixture, and flowing the mixture through a mixing tube under highly turbulent conditions to thereby heat the stock, separate the fibers of the stock and disperse any contained contaminants.
Claim 3
Dependent Claim
26 words
The method of claim 1, and including the step of flowing the stock into contact with the steam at a velocity of 14 to 22 ft./sec.
Claim 4
Dependent Claim
39 words
The method of claim 1, and including the step of sensing the temperature of the mixture downstream of the mixing tube, and adjusting the rate of flow of said steam to provide a substantially uniform temperature for the mixture.
Claim 5
Independent Claim
126 words
A method of defibrating waste paper and dispersing contained contaminants within the dispersed ffibers, comprising the steps of passing steam at a pressure in excess of 20 psig through a nozzle in a housing to obtain a steam velocity in the range of 1,200 to 1,600 ft./sec., directing the steam into a mixing tube spaced axially of said nozzle, introducing an aqueous slurry of waste paper having a fibrous solids content of 1% to 5% by weight into the space in the housing between said nozzle and said mixing tube, and subjecting the mixture of steam and slurry to highly turbulent conditions in said mixing tube to thereby heat the slurry, separate the fibers in the slurry and disperse any contained contaminants throughout the separated fibers.
Claim 6
Independent Claim
126 words
A method of defibrating waste paper and dispersing contained contaminants within the dispersed ffibers, comprising the steps of passing steam at a pressure in excess of 20 psig through a nozzle in a housing to obtain a steam velocity in the range of 1,200 to 1,600 ft./sec., directing the steam into a mixing tube spaced axially of said nozzle, introducing an aqueous slurry of waste paper having a fibrous solids content of 1% to 5% by weight into the space in the housing between said nozzle and said mixing tube, and subjecting the mixture of steam and slurry to highly turbulent conditions in said mixing tube to thereby heat the slurry, separate the fibers in the slurry and disperse any contained contaminants throughout the separated fibers.
Claim 7
Dependent Claim
24 words
The method of claim 4, and including the step of flowing the slurry into the housing at a velocity of 5 to 10 ft./sec.
Claim 8
Dependent Claim
36 words
The method of claim 4, and including the step of maintaining the velocity of the mixture of steam and slurry at the downstream end of said mixing tube in the range of 14 to 22 ft./sec.
Claim 9
Dependent Claim
32 words
The method of claim 4, and including the step of adjusting the axial spacing between the nozzle and the mixing tube to establish the velocity of the slurry flowing to said space.
Claim 10
Dependent Claim
27 words
The method of claim 5, and including the step of maintaining the pressure of the steam entering said nozzle at a value of 50 to 100 psig.
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) | 1985-01-25 | 1985-07-27 | 1986-01-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-01-25 | 1989-07-27 | 1990-01-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-01-25 | 1993-07-27 | 1994-01-26 | $7700.00 | Window Closed / Lapsed |