Fiberboard manufacturing method and fiberboard
US-12163284-B2 · Dec 10, 2024 · US
US10201911B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10201911-B2 |
| Application number | US-201515502441-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 5, 2015 |
| Priority date | Aug 8, 2014 |
| Publication date | Feb 12, 2019 |
| Grant date | Feb 12, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A continuous process forms a unitary mat on a line having at least two conveyors spaced from each other. The process includes combining the isocyanate, an isocyanate catalyst, and a plurality of lignocellulosic particles to form a mixture and a self-polymerization product of the isocyanate in-situ in the mixture. The process also includes forming the unitary mat from the mixture on a first conveyer and transferring the unitary mat from the first conveyor to a second conveyor across a predetermined distance while maintaining structural integrity of the unitary mat. The lignocellulosic particles have a moisture content of 0.5 to 30 weight percent of water. Moreover, the continuous process is free of a step of adding water to the isocyanate, the isocyanate catalyst, the lignocellulosic particles, and/or the unitary mat.
Opening claim text (preview).
What is claimed is: 1. A continuous process for forming unitary mats on a line having at least two conveyors spaced from each other, said process comprising the steps of: A. combining an isocyanate, an isocyanate catalyst, triethyl phosphate, and a plurality of lignocellulosic particles to form a mixture and a self-polymerization product of the isocyanate in-situ in the mixture; B. forming one of the unitary mats from the mixture on a first conveyer; C. transferring the unitary mat from the first conveyor to a second conveyor across a distance while maintaining structural integrity of the unitary mat; and D. continuously forming the unitary mats by steps (A)-(C) on said line having at least two conveyors, wherein the lignocellulosic particles have a moisture content of 0.5 to 30 weight percent of water, and wherein said continuous process is free of a step of adding water to the isocyanate or the isocyanate catalyst. 2. The continuous process of claim 1 wherein the at least two conveyors are spaced apart from each other by the predetermined distance of from 5 to 20 cm. 3. The continuous process of claim 1 wherein the isocyanate is polymeric methylene-4,4′-diphenyl diisocyanate. 4. The continuous process of claim 1 wherein the isocyanate catalyst is present in a carrier polyol. 5. The continuous process of claim 4 wherein the carrier polyol has a weight average molecular weight of from 50 to 2000 g/mol and is optionally a polyether polyol. 6. The continuous process of claim 1 wherein the mixture further comprises a polyurethane, polyurea, or combinations thereof. 7. The continuous process of claim 1 wherein the mixture comprises less than 1 weight percent of water. 8. The continuous process of claim 1 wherein the plurality of lignocellulosic particles comprises 0.5 to 20 weight percent of water. 9. The continuous process of claim 1 wherein the step of combining occurs at a temperature of from 140° F. to 180° F. 10. The continuous process of claim 1 wherein the step of forming the mat occurs at a temperature of from 325° F. to 375° F. such that a thermoset polyurethane and/or polyurea is formed. 11. The continuous process of claim 1 wherein the mixture comprises a reactive intermediate of an isocyanate polymerization reaction formed in-situ prior to the step of forming the mat. 12. The continuous process of claim 1 wherein the mixture comprises a biuret of polymeric methylene-4,4′-diphenyl diisocyanate during said step of forming the mat from the mixture. 13. The continuous process of claim 1 wherein the mixture is free of a formaldehyde resin. 14. The continuous process of claim 1 wherein the mixture is free of a tackifying compound and/or adhesive, different from the isocyanate and/or the self-polymerization product of the isocyanate. 15. A unitary mat having a length and width and comprising: a plurality of lignocellulosic particles; a self-polymerization product of an isocyanate; and triethyl phosphate; wherein said plurality of lignocellulosic particles has a moisture content of 0.5 to 30 weight percent of water; and wherein said mat is free of a tackifying agent and/or adhesive different from said self-polymerization product of said isocyanate. 16. The unitary mat of claim 15 that maintains structural integrity when transferred from a first conveyor to a second conveyor across a distance during a continuous process of forming. 17. The unitary mat of claim 15 that is free of a formaldehyde resin and/or a reaction product of a formaldehyde resin and an isocyanate.
with hydroxyaryl compounds · CPC title
Manufacture of substantially flat articles, e.g. boards, from particles or fibres · CPC title
Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step · CPC title
containing only one alkylene bisphenyl group · CPC title
Manufacture of polymers by continuous processes (C08G18/0838 takes precedence) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.