Product and processes from an integrated forest biorefinery
US-2016168791-A1 · Jun 16, 2016 · US
US9683329B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9683329-B2 |
| Application number | US-201615051742-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 24, 2016 |
| Priority date | Apr 20, 2004 |
| Publication date | Jun 20, 2017 |
| Grant date | Jun 20, 2017 |
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An omnibus process of pulping and bleaching lignocellulosic materials in which a charge of a lignocellulosic material is biopulped and/or water extracted prior to pulping and bleaching. The lignocellulosic material may be mechanically pulped and bleached in the presence of an enzyme that breaks lignin-carbohydrate complexes.
Opening claim text (preview).
What is claimed is: 1. A method of producing a pulp, the method comprising: (a) providing a charge of lignocellulosic material; (b) contacting the charge of lignocellulosic material with water, the water and charge of lignocellulosic material maintained at a temperature in the range of between about 130° C. and about 200° C. and lowering the pH to between about 3 and about 6.9 by producing acid from the reaction of the water and lignocellulosic material for a period in the range of between about 15 minutes and about 240 minutes, wherein an aqueous extract and extracted lignocellulosic materials are obtained and wherein the acid comprises acetic acid; and (c) pulping the extracted lignocellulosic materials to produce the pulp, wherein the pulp has a viscosity of greater than about 30 cP. 2. The method of claim 1 , wherein the water and charge of lignocellulosic material are maintained at a temperature in the range of between about 145° C. and about 185° C. 3. The method of claim 1 , wherein the pulp has a viscosity of greater than about 40 cP. 4. The method of claim 1 , wherein the pulping step produces individual fibers and fiber bundles having a kappa number of at most about 18 after about 15 minutes. 5. The method of claim 1 , wherein the pulping step produces individual fibers and fiber bundles having a kappa number of at most about 11 after about 30 minutes. 6. The method of claim 1 , wherein the pulping step produces individual fibers and fiber bundles having a kappa number of at most about 7 after about 60 minutes. 7. The method of claim 1 , wherein oxygen delignification reduces a kappa number of the pulp by at least 40%. 8. The method of claim 1 further comprising a step (d) a bleaching step, wherein said bleaching step is effectuated by contacting said pulp of said step (c) with an oxidizing agent selected from the group consisting of oxygen, hydrogen peroxide, ozone, peracetic acid, chlorine, chlorine dioxide, a hypochlorite anion and mixtures thereof, to form a bleached pulp. 9. The method of claim 8 , wherein the bleached pulp has a brightness of greater than 90%. 10. The method of claim 8 , wherein the bleached pulp has a brightness of greater than 91%.
with water or steam · CPC title
with inorganic bases or alkaline reacting compounds, e.g. sulfate processes · CPC title
Use of compounds accelerating the pulping processes · CPC title
Bleaching agents (bleaching cellulose pulp D21C9/10) · CPC title
Mixtures of chemical and mechanical pulp · CPC title
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