Method of multilayer coating

Claim 2

In the process of applying a multilayer liquid coating to a moving web as distinct superposed continuous layers that are thinned as they are drawn down on the web, the improvement which comprises applying as the layer next to the web a shear thinning carrier layer of pseudoplastic liquid having a viscosity between 20 and 200 centipoises at a shear rate of 100 sec -1 and a viscosity below 10 centipoises at a shear rate of 100,000 sec -1 .

Claim 3

The process of claim 1, in which the viscosity of said carrier layer is below 5 centipoises at a shear rate of 10,000 sec -1 .

Claim 4

The process of claim 1, in which said carrier layer comprises an aqueous solution of a shear thinning thickening agent.

Claim 5

The process of claim 3, in which said thickening agent is sodium cellulose sulfate.

Claim 6

The process of claim 3, in which said solution contains gelatin.

Claim 7

In the process of simultaneously applying a plurality of aqueous layers to a moving web as distinct superposed continuous layers that are thinned as they are drawn down on the web, the improvement which comprises applying as the first layer next to the web an aqueous pseudoplastic having a consistency m>50 and a flow behavior index n<0.7 and a viscosity substantially given by η = m (dγ/dτ) .sup.n-1 where η is viscosity and dγ/dτ is the shear rate and η is less than 5 centipoises at a shear rate of 100,000 sec -1 , and applying as the second layer next to said first layer a liquid containing at least 10 percent of solids by weight of solution and having a viscosity greater than 50 centipoises at 42° C. at a shear rate of 100 sec -1 .

Claim 8

In the process of simultaneously applying a plurality of aqueous layers to a moving web as distinct superposed continuous layers that are thinned as they are drawn down on the web, the improvement which comprises applying as the first layer next to the web an aqueous pseudoplastic having a consistency m>50 and a flow behavior index n<0.7 and a viscosity substantially given by η = m (dγ/dτ) .sup.n-1 where η is viscosity and dγ/dτ is the shear rate and η is less than 5 centipoises at a shear rate of 100,000 sec -1 , and applying as the second layer next to said first layer a liquid containing at least 10 percent of solids by weight of solution and having a viscosity greater than 50 centipoises at 42° C. at a shear rate of 100 sec -1 .