Blow line addition of isocyanate binder in fiberboard manufacture

Claim 2

In a process of producing a synthetic board from cellulosic material and a binder wherein (a) said cellulosic material is subjected to the action of steam under pressure and refined to hot and wet fibers, (b) said hot and wet fibers are partially dewatered, (c) said partially dewatered fibers are formed into a mat, and (d) said mat is subjected to heat and pressure to form said synthetic board, the improvement comprising applying an organic polyisocyanate binder to said hot and wet fibers from said refining step (a).

Claim 3

The process of claim 1 wherein said cellulosic material comprises wood furnish.

Claim 4

The process of claim 1 wherein said cellulosic material comprises mixed hardwoods.

Claim 5

The process of claim 1 wherein said polyisocyanate is a polyphenylpolyisocyanate.

Claim 6

The process of claim 1 wherein said polyisocyanate comprises a mixture of diphenylmethane-4,4'-diisocyanate and polymethylene polyphenyl polyisocyanates.

Claim 7

The process of claim 1 wherein said polyisocyanate is applied as a water emulsion to said hot and wet fibers.

Claim 8

The process of claims 1, 3, 4, 5 or 6 wherein said polyisocyanate comprises a self-releasing binder.

Claim 9

The process of claim 1 wherein said polyisocyanate is applied in an amount of about 3 to 6% by weight, based on the total weight of solids.

Claim 10

The process of claim 1 wherein said polyisocyanate is applied to an amount of about 4 to 6% by weight, based on the total weight of solids.

Claim 11

The process of claim 1 wherein said cellulosic material comprises mixed hardwoods, said polyisocyanate comprises a mixture of diphenylmethane-4,4'-diisocyanate and polymethylene polyphenyl polyisocyanates, and said mixture is applied as a water emulsion to said hot and wet fibers.

Claim 12

The process of claim 1 wherein (a) said refining step (a) is accomplished in a pressurized digester-refiner apparatus having a blow line for discharge of said hot and wet fibers from said apparatus, (b) said fibers discharged from said apparatus are propelled through said blow line at a moisture content of about 50% or higher by weight, and a temperature of at least about 212° to 260° F., and (c) said polyisocyanate is applied to said fibers in said blow line.

Claim 13

The process of claim 1 wherein said mat, before said step (d), contains about 8 to 16% moisture by weight.

Claim 14

The process of claims 10, 11 or 12 wherein said polyisocyanate is applied in an amount of about 4 to 6% by weight, based on the total weight of solids.

Claim 15

The process of claim 1 wherein (1) said cellulosic material comprises mixed hardwoods and said mixed hardwoods are subjected to the action of steam under pressure and refined to hot and wet fibers in a pressurized digester-refiner apparatus having a blow line for discharge of said hot and wet fibers from said apparatus, (2) said fibers discharged from said apparatus are propelled through said blow line at a moisture content of about 50% or higher by weight, and a temperature of at least about 212° to 260° F., (3) said polyisocyanate comprises a polyphenylpolyisocyanate, and said polyphenylpolyisocyanate is applied as a water emulsion to said fibers in said blow line, said polyphenylpolyisocyanate comprising about 4 to 6% by weight, based on the total weight of solids, and (4) said mat, before said step (d), contains about 8 to 16% moisture by weight.

Claim 16

The process of claim 14 wherein (a) said mixed hardwoods, before said step (1), are treated with paraffinic wax, and (b) said polyphenylpolyisocyanate comprises a mixture of diphenylmethane-4,4'-diisocyanate and polymethylene polyphenyl polyisocyanates.