← Back to Patent Explorer
US4080249A Expired / Lapsed US ⏱️ 0.0 years remaining

Delignification and bleaching of a lignocellulosic pulp slurry with ozone

Assignee: International Paper Co
•
Filing: 1976-07-16
•
Granted: 1978-03-21
•
Expires: 1996-07-16
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for the delignification and bleaching of a lignocellulosic pulp slurry, having a consistency between about 1% and 10%, by weight of oven-dried pulp, and a pH between about 1 and 7, while at a temperature between about 0° C. and 70° C., with a gaseous mixture selected from the group consisting of ozone/oxygen, ozone/air, and a mixture thereof. The ozone containing gaseous mixture, which has an ozone concentration of from about 0.1% to about 20%, by weight of oxygen or air, is bubbled into the pulp slurry, while agitating the pulp slurry at a rate of about 0.01 to 5.0 horsepower-days per ton of pulp.

Inventors

  • 👤 Arthur W. Kempf
  • 👤 Richard B. Phillips

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 06:34
CPC Classifications
D; D21; D21C; D21C9/00; D21C9/10; D21C9/1073

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 133 words
A process for delignifying and bleaching lignocellulosic pulp, which comprises reacting a lignocellulosic pulp slurry, having a consistency of from about 1% to about 10%, by weight of oven-dried pulp, and a pH within the range of from about 1 to about 7 and a temperature between about 0° C. and about 70° C., with a gaseous mixture selected from the group consisting of ozone/oxygen, ozone/air, and a mixture thereof, in a reaction vessel, said gaseous mixture being in the form of bubbles substantially all of which are about 1/8 inch or less in diameter and having an ozone concentration of from about 0.1% to about 20%, by weight of oxygen or air, while agitating the pulp slurry at a rate of from about 0.01 to about 5.0 horsepower-days per ton of pulp.
Claim 2
Dependent Claim 133 words
A process for delignifying and bleaching lignocellulosic pulp, which comprises reacting a lignocellulosic pulp slurry, having a consistency of from about 1% to about 10%, by weight of oven-dried pulp, and a pH within the range of from about 1 to about 7 and a temperature between about 0° C. and about 70° C., with a gaseous mixture selected from the group consisting of ozone/oxygen, ozone/air, and a mixture thereof, in a reaction vessel, said gaseous mixture being in the form of bubbles substantially all of which are about 1/8 inch or less in diameter and having an ozone concentration of from about 0.1% to about 20%, by weight of oxygen or air, while agitating the pulp slurry at a rate of from about 0.01 to about 5.0 horsepower-days per ton of pulp.
Claim 3
Dependent Claim 26 words
A process of accordance with claim 1 wherein the concentration of the ozone is from about 2.0% to about 3.0%, by weight of oxygen or air.
Claim 4
Dependent Claim 26 words
A process in accordance with claim 1 wherein from about 0.1% to about 5.0% ozone, by weight of oven-dried pulp, is applied to the pulp slurry.
Claim 5
Dependent Claim 21 words
A process in accordance with claim 1 wherein the time of reaction is from about 1 minute to about 60 minutes.
Claim 6
Dependent Claim 24 words
A process in accordance with claim 1 wherein the agitation utilizes between about 0.1 horsepower-days to about 1.0 horsepower-days per ton of lignocellulosic pulp.
Claim 7
Dependent Claim 23 words
A process in accordance with claim 1 wherein the pulp consistency is from about 2% to about 3%, by weight of oven-dried pulp.
Claim 8
Dependent Claim 22 words
A process in accordance with claim 1 wherein the temperature of the slurry is from about 20° C to about 30° C.
Claim 9
Dependent Claim 20 words
A process in accordance with claim 1 wherein the pH of the pulp slurry is between about 3 and 5.
Claim 10
Dependent Claim 27 words
A process in accordance with claim 1 wherein said pulp slurry is subjected to oxygen bleaching in the presence of alkali prior to said reaction with ozone.
Claim 11
Dependent Claim 17 words
A process in accordance with claim 1 wherein said pulp slurry is subsequently bleached with peracetic acid.
Claim 12
Dependent Claim 18 words
A process in accordance with claim 1 wherein said pulp slurry is subsequently bleached with a peroxide compound.
Claim 13
Dependent Claim 47 words
A process in accordance with claim 1 wherein said pulp slurry, subsequent to said zone reacting, is subjected to the following bleaching sequence: extraction with sodium hydroxide or water, bleaching with an ozone containing gaseous mixture in accordance with claim 1 and then bleaching with peracetic acid.
Claim 14
Dependent Claim 48 words
A process in accordance with claim 1 wherein said pulp slurry, subsequent to said ozone reacting, is subjected to the following bleaching sequence: extraction with sodium hydroxide or water, bleaching with an ozone containing gaseous mixture in accordance with claim 1 and then bleaching with a peroxide compound.
Claim 15
Dependent Claim 47 words
A process in accordance with claim 1 wherein said pulp slurry, subsequent to said ozone reacting, is subjected to the following bleaching sequence: extraction with sodium hydroxide or water, bleaching with an ozone containing gaseous mixture in accordance with claim 1 and then bleaching with chlorine dioxide.
Claim 16
Dependent Claim 48 words
A process in accordance with claim 1 wherein said pulp slurry, subsequent to said ozone reacting, is subjected to the following bleaching sequence: extraction with sodium hydroxide or water, bleaching with an ozone containing gaseous mixture in accordance with claim 1 and then bleaching with a hypochlorite compound.

References Cited (Backward Citations)

US3318657A Cited
US3352642A Cited
US3829357A Cited
US3619350A Cited
US3663357A Cited
CA902861A Cited
CA970111A Cited
US3806404A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-03-20 1981-09-19 1982-03-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-03-20 1985-09-19 1986-03-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-03-20 1989-09-19 1990-03-21 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag