Method for producing microcrystalline cellulose from tobacco and related tobacco product

US10334874B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10334874-B2
Application numberUS-201615099971-A
CountryUS
Kind codeB2
Filing dateApr 15, 2016
Priority dateApr 19, 2012
Publication dateJul 2, 2019
Grant dateJul 2, 2019

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Methods for producing dissolving grade pulp and microcrystalline cellulose from tobacco are provided. The methods include chemical pulping a tobacco input to form a tobacco pulp. Chemical pulping the tobacco input includes combining the tobacco input with a strong base defining a weight from about 5% to about 50% of the tobacco input, and heating the tobacco input and the strong base with an H-factor from about 500 to about 3,300. Further, the methods include bleaching the tobacco pulp to produce a dissolving grade pulp. Bleaching the tobacco pulp may include chlorination of the tobacco pulp with a chlorine dioxide solution, and caustic extraction of the tobacco pulp with a second strong base. A related tobacco-derived microcrystalline cellulose product is also provided, which can be used as a binder, a filler, and/or a texturizer in a tobacco product, such as a smokeless tobacco product.

First claim

Opening claim text (preview).

What is claimed is: 1. A dissolving grade pulp derived from tobacco, the dissolving grade pulp characterized by a brightness of at least about 83%, an alpha-cellulose concentration of at least about 88% by weight, a beta and a gamma cellulose content, and a degree of polymerization of about 100 to about 750, wherein the dissolving grade pulp is characterized by a kappa number between about 20 and about 30. 2. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is formed by subjecting a tobacco input to the following operations: chemical pulping the tobacco input to form a tobacco pulp; and bleaching the tobacco pulp. 3. The dissolving grade pulp of claim 2 , wherein chemical pulping the tobacco input comprises: combining the tobacco input with a strong base; and heating the tobacco input and the strong base. 4. The dissolving grade pulp of claim 2 , wherein bleaching the tobacco pulp comprises: chlorination of the tobacco pulp with a chlorine dioxide solution; and caustic extraction of the tobacco pulp with a second strong base. 5. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a quantity of hemicelluloses of about 0.5% to about 10% by weight of the dissolving grade pulp. 6. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a quantity of lignin of about 0% to about 0.2% by weight of the dissolving grade pulp. 7. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a quantity of pentosan of about 0% to about 5% by weight of the dissolving grade pulp. 8. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a quantity of ash of about 0% to about 0.15% by weight of the dissolving grade pulp. 9. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a quantity of alcohol-benzene extractives of about 0% to about 0.5% by weight of the dissolving grade pulp. 10. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a viscosity of about 2 centipoise to about 15 centipoise, the viscosity being measured by a capillary viscometer in a 0.5 wt-% cupriethylenediamine solution. 11. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by a copper number of about 0.1 to about 1.2. 12. The dissolving grade pulp of claim 1 , wherein the dissolving grade pulp is characterized by between about 5% and about 15% of the dissolving grade pulp having a particle size of less than about 10 μm, the particles of the dissolving grade pulp being sized to pass through a screen mesh.

Assignees

Inventors

Classifications

  • Oxycellulose; Hydrocellulose {, e.g. microcrystalline cellulose} · CPC title

  • Lignocellulosic material, e.g. wood, straw or bagasse {(manufacture of articles made from lignocellulosic material by dry processes B27N)} · CPC title

  • C08H8/00Primary

    Macromolecular compounds derived from lignocellulosic materials {(pretreatment thereof B27N)} · CPC title

  • A24B15/302Primary

    by natural substances obtained from animals or plants · CPC title

  • Chemical or chemomechanical {or chemothermomechanical} pulp · CPC title

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What does patent US10334874B2 cover?
Methods for producing dissolving grade pulp and microcrystalline cellulose from tobacco are provided. The methods include chemical pulping a tobacco input to form a tobacco pulp. Chemical pulping the tobacco input includes combining the tobacco input with a strong base defining a weight from about 5% to about 50% of the tobacco input, and heating the tobacco input and the strong base with an H-…
Who is the assignee on this patent?
Reynolds Tobacco Co R, Univ North Carolina State
What technology area does this patent fall under?
Primary CPC classification C08H8/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jul 02 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).