Patent US4357208A successfully refreshed from Google Patents.
US4357208A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of making pulp
Assignee: SCA Development AB
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Filing: 1979-01-18
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Granted: 1982-11-02
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Expires: 1999-01-18
Abstract
Abstract Lignocellulose material is pretreated with steam, heat, lignin softening chemicals or combinations thereof. The pretreated material is then refined in a disc refiner. Water is added to the material in the refining zone of the disc refiner to form a suspension at concentration of 8-15% at the point of discharge from the gap between the discs of the refiner. Steam development and steam backflow from the gap is reduced.
Inventors
- 👤 Per V. Peterson
- 👤 Hans E. Hoglund
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 18:25
CPC Classifications
D; D21; D21D; D21D1/00; D21D1/20; D21D1/30
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
240 words
A method for refining lignocellulose containing material comprising the steps of pretreating the lignocellulose containing material with a medium selected from steam, heat, lignin-softening chemicals and combinations thereof; refining the pre-treated lignocellulose containing material in a refining zone of a disc refiner containing refiner discs and a housing surrounding said refiner zone, wherein during said refining step water is added to said lignocellulose containing material and the lignocellulose containing material is passed through a gap between the refining discs so as to form a suspension containing said lignocellulose containing material in a concentraion of from 8% to 15% at the point of discharge of said suspension from said gap and so as to substantially reduce the steam development in said gap, thereby reducing the steam flow backwards against the lignocellulose containing material coming into said refining zone; and passing said suspension into said housing surrounding the refiner discs, wherein water is supplied to said refiner housing to form a diluted suspension such that the concentration of the refined lignocellulose containing material in said diluted suspension exiting the refiner from the housing is in the range of from 1% to 6% and wherein said refiner housing is maintained filled with said diluted suspension to increase the retention time of the material in said gap by breaking the acceleration of the material coming through said gap, to condense steam flowing through said gap, and to conduct heat away from said refining zone.
Claim 2
Independent Claim
240 words
A method for refining lignocellulose containing material comprising the steps of pretreating the lignocellulose containing material with a medium selected from steam, heat, lignin-softening chemicals and combinations thereof; refining the pre-treated lignocellulose containing material in a refining zone of a disc refiner containing refiner discs and a housing surrounding said refiner zone, wherein during said refining step water is added to said lignocellulose containing material and the lignocellulose containing material is passed through a gap between the refining discs so as to form a suspension containing said lignocellulose containing material in a concentraion of from 8% to 15% at the point of discharge of said suspension from said gap and so as to substantially reduce the steam development in said gap, thereby reducing the steam flow backwards against the lignocellulose containing material coming into said refining zone; and passing said suspension into said housing surrounding the refiner discs, wherein water is supplied to said refiner housing to form a diluted suspension such that the concentration of the refined lignocellulose containing material in said diluted suspension exiting the refiner from the housing is in the range of from 1% to 6% and wherein said refiner housing is maintained filled with said diluted suspension to increase the retention time of the material in said gap by breaking the acceleration of the material coming through said gap, to condense steam flowing through said gap, and to conduct heat away from said refining zone.
Claim 3
Dependent Claim
24 words
A method according to claim 1, wherein an overpressure is maintained at the entrance of said material into the gap between said refining discs.
Claim 4
Dependent Claim
19 words
A method according to claim 2, wherein the same overpressure is maintained in refiner housing surrounding the refining discs.
Claim 5
Dependent Claim
18 words
A method according to claim 2 or 3, wherein said overpressure is maintained between 20 and 140 kPa.
Claim 6
Dependent Claim
46 words
A method according to claim 1 or 2, wherein a material concentration in the gap between the refining discs is maintained by adding water to the material as the material enters the gap between the refining discs and by controlling the amount of water so supplied.
Claim 7
Dependent Claim
43 words
A method according to claim 1 or 2, wherein the water for diluting the material in the refiner housing is supplied to a lower portion of the refiner housing and said diluted suspension is discharged from the upper portion of said refiner housing.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-11-01 | 1986-05-03 | 1986-11-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-11-01 | 1990-05-03 | 1990-11-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-11-01 | 1994-05-03 | 1994-11-02 | $7700.00 | Window Closed / Lapsed |