US4840703A
Expired / Lapsed
US
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Method for controlling an oxygen bleaching
Assignee: Repola Oy
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Filing: 1988-06-29
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Granted: 1989-06-20
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Expires: 2008-06-29
Abstract
Abstract A method for controlling an oxygen-bleaching process of lignocellulosic pulp to a desired degree of delignification. The pulp is passed at a substantially constant temperature into a bleaching reactor wherein the pulp has a substantially constant level at its outlet. The hydrostatic pressure is measured and the quantity of oxygen fed into the reactor is adjusted to reach a desired degree of delignification.
Inventors
- 👤 Erkki Malmsten
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 02:59
CPC Classifications
D; D21; D21C; D21C9/00; D21C9/10; D21C9/1026; D21C9/1052; D21C9/147
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
116 words
Method for controlling an oxygen-bleaching process of lignocellulose pulp stock to a desired degree of delignification comprising adding alkali oxygen at a desired ratio to the pulp stock, passing the pulp at a desired substantially constant temperature into and out of the bleaching reactor wherein the pulp has a substantially constant level at its outlet measuring the hydrostatic pressure at the bottom of the reactor and adjusting the quantity of feed of oxygen in response to the measured hydrostatic pressure, to a value to reach the desired degree of delignification; and adjusting the amount of alkali added in response to the adjusted amount of oxygen to maintain the alkali and oxygen ratio at the desired ratio.
Claim 2
Dependent Claim
116 words
Method for controlling an oxygen-bleaching process of lignocellulose pulp stock to a desired degree of delignification comprising adding alkali oxygen at a desired ratio to the pulp stock, passing the pulp at a desired substantially constant temperature into and out of the bleaching reactor wherein the pulp has a substantially constant level at its outlet measuring the hydrostatic pressure at the bottom of the reactor and adjusting the quantity of feed of oxygen in response to the measured hydrostatic pressure, to a value to reach the desired degree of delignification; and adjusting the amount of alkali added in response to the adjusted amount of oxygen to maintain the alkali and oxygen ratio at the desired ratio.
Claim 3
Dependent Claim
29 words
Method as claimed in claim 1, wherein the pulp flow is passed into the flow reactor through its bottom end and out of the reactor through its upper end.
Claim 4
Dependent Claim
34 words
Method as claimed in claim 1 further comprising measuring the pH of the pulp flow passed into the reactor and adjusting the quantity of alkali in accordance with the changes in the measured pH.
Claim 5
Dependent Claim
34 words
Method as claimed in claim 2 further comprising measuring the pH of the pulp flow passed into the reactor and adjusting the quantity of alkali in accordance with the changes in the measured pH.
References Cited (Backward Citations)
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Cited
US3579417A
Cited
US3832276A
Cited
SU445033A1
Cited
US4198266A
Cited
US4419184A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-06-19 | 1992-12-19 | 1993-06-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-06-19 | 1996-12-19 | 1997-06-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-06-19 | 2000-12-19 | 2001-06-20 | $7700.00 | Window Closed / Lapsed |