Blow line addition of thermosettable binder in fiberboard manufacture utilizing cooled nozzle

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 in a pressurized digester-refiner apparatus having a blow line for discharge of said hot and wet fibers from said apparatus, (b) said hot and wet fibers after discharge from said apparatus 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 a thermosettable resin binder to said hot and wet fibers in said blow line by feeding said thermosettable resin through a cooled nozzle secured on and communicating with the interior of said blow line.

Claim 3

The process of claim 1 wherein said thermosettable resin comprises an organic polyisocyanate.

Claim 4

The process of claim 2 wherein said cellulosic material comprises wood furnish.

Claim 5

The process of claim 2 wherein said cellulosic material comprises mixed hardwoods.

Claim 6

The process of claim 2 wherein said polyisocyanate is a polyphenylpolyisocyanate.

Claim 7

The process of claim 2 wherein said polyisocyanate comprises a mixture of diphenylmethane-4,4'-diisocyanate and polymethylene polyphenyl polyisocyanates.

Claim 8

The process of claim 2 wherein said polyisocyanate is applied as a water emulsion to said hot and wet fibers.

Claim 9

The process of claims 2, 4, 5, 6 or 7 wherein said polyisocyanate comprises a self-releasing binder.

Claim 10

The process of claim 2 wherein said polyisocyanate is applied in an amount of about 3 to 6% by weight, based on the total weight of solids.

Claim 11

The process of claim 2 wherein said polyisocyanate is applied in an amount of about 4 to 6% by weight, based on the total weight of solids.

Claim 12

The process of claim 2 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 13

The process of claim 2 wherein said fibers discharged from said pressurized digester-refiner 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.

Claim 14

The process of claim 2 wherein said mat, before said board-forming step, contains about 8 to 16% moisture by weight.

Claim 15

The process of claims 11, 12 or 13 wherein said polyisocyanate is applied in an amount of about 4 to 6% by weight, based on the total weight of solids.

Claim 16

The process of claim 2 wherein (1) said cellulosic material comprises mixed hardwoods, (2) said fibers discharged from said pressurized digester-refiner 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 board-forming step, contains about 8 to 16% moisture by weight.

Claim 17

The process of claim 15 wherein (a) said mixed hardwoods, before said refining step, are treated with paraffinic wax, and (b) said polyphenylpolyisocyanate comprises a mixture of diphenylmethane-4,4'-diisocyanate and polymethylene polyphenyl polyisocyanates.

Claim 18

The process of claims 1, 2, 4, 5, 10, 15 or 16 wherein said cooled nozzle comprises an inner tube having resin inlet and outlet ends, said resin inlet end being adapted to communicate with a resin feed line and said resin outlet end being adapted to communicate with said blow line, and a housing disposed about said inner tube to define an enclosed jacketed area about said inner tube, said housing having at least one cooling fluid inlet means adjacent the one end of said housing located to the exterior of said resin outlet end of said inner tube, said at least one cooling fluid inlet means being adapted to communicate with a cooling fluid feed line, and at least one cooling fluid outlet means adjacent the other end of said housing located to the exterior of said resin inlet end of said inner tube, said at least one cooling fluid outlet means being adapted to communicate with a cooling fluid discharge line.

Claim 19

The process of claim 17 wherein said resin outlet end of said inner tube and said one end of said housing located to the exterior of said resin outlet end are attached to the wall of said blow line, and said resin inlet end of said inner tube extends a short distance outwardly of said other end of said housing.

Claim 20

The process of claim 18 wherein (a) said at least one cooling fluid inlet means comprises a feed pipe secured to said housing and communicating with said enclosed jacketed area, said feed pipe being angularly positioned on said housing to direct the flow of cooling fluid from said feed pipe toward the region where said inner tube is attached to said blow line wall and to promote swirling of said cooling fluid about said inner tube, and (b) said at least one cooling fluid outlet means comprises an exit pipe secured to said housing and communicating with said enclosed jacketed area, said exit pipe being angularly positioned on said housing to enhance cooling fluid circulation.

Claim 21

The process of claim 17 wherein said enclosed jacketed area is provided with at least one baffle means to increase fluid turbulence.

Claim 22

The process of claim 17 wherein the surface of said inner tube facing said enclosed jacketed area is threaded or knurled to increase the surface area and thereby improve heat transfer.