Beverage filtration process

Claim 2

A process for removal of haze precursors from unstable beverages which comprises the step of contacting said beverage in a haze-free condition and at ambient temperature with a positive-charge modified porous medium comprised of fine particulate, the charge being modified with a polyamido-polyamine epichlorhydrin cationic resin, to form a precipitate and removing said precipitate from said beverage at ambient temperature.

Claim 3

The process of claim 1 wherein the beverage is contacted in a haze-free condition with the positive-charge modified porous medium at a temperature within the range of from about 50° F. to about 75° F. and the resulting precipitate is removed at a temperature within the aforesaid range.

Claim 4

A process of stabilizing unstable beverages against haze development which comprises conducting said beverage in a haze-free condition and at ambient temperature through a first filter medium to form haze in said beverage and thereafter filtering the formed haze at ambient temperature with a second filter medium; said first filter medium being comprised of fine particulate and a self-bonding matrix of cellulose fiber, the surfaces of at least one of which are modified with a polyamido-polyamine epichlorhydrin cationic resin to provide a positive Zeta potential, the matrix incorporating beaten cellulose fiber to provide a Canadian Standard Freeness of less than 600 ml.

Claim 5

A process of stabilizing unstable beverages against haze development which comprises conducting said beverage in a haze-free condition and at ambient temperature through a first filter medium to form haze in said beverage and thereafter filtering the formed haze at ambient temperature with a second filter medium; said first filter medium being comprised of fine particulate and a self-bonding matrix of cellulose fiber, the surfaces of at least one of which are modified with a polyamido-polyamine epichlorhydrin cationic resin to provide a positive Zeta potential, the matrix incorporating beaten cellulose fiber to provide a Canadian Standard Freeness of less than 600 ml.

Claim 6

The process of claim 3 wherein the beverage is conducted in a haze-free condition through the first filter medium at a temperature within the range of from about 50° F. to about 75° F. and the resulting haze is filtered through the second filter medium at a temperature within the aforesaid range.

Claim 7

The process according to claim 3 wherein said first filter medium comprises from about 1 to about 3 percent by weight of said cationic resin.

Claim 8

The process according to claim 3 wherein said first filter medium comprises at least 50 percent by weight of diatomaceous earth.

Claim 9

The process according to claim 3 wherein said fine particulate comprises an admixture of diatomaceous earth and perlite.

Claim 10

The process according to claim 3 wherein said fine particulate exhibits an average particulate dimension of less than 10 microns.

Claim 11

The process according to claim 3 wherein said first filter medium is sanitized or sterilized.

Claim 12

The process according to claim 3 wherein said first filter medium is hot water flushed prior to the step of conducting.

Claim 13

The process according to claim 3 wherein said beverage is an alcoholic beverage.

Claim 14

The process according to claim 3 wherein said beverage is straight or blended whiskey, or rum.

Claim 15

The process of precipitating haze precursors from an alcoholic beverage which comprises contacting said beverage in a haze-free condition and at ambient temperature with a positive charge-modified porous medium comprised of fine particulate, the charge being modified with a polyamidopolyamine epichlorhydrin cationic resin.

Claim 16

The process of precipitating haze precursors from an alcoholic beverage which comprises contacting said beverage in a haze-free condition and at ambient temperature with a positive charge-modified porous medium comprised of fine particulate, the charge being modified with a polyamidopolyamine epichlorhydrin cationic resin.

Claim 17

The process of claim 13 wherein the beverage is contacted in a haze-free condition with the positive charge-modified porous medium at a temperature within the range of from 50° F. to about 75° F. to precipitate the haze precursors.

Claim 18

The process of claim 14 wherein the precipitated haze precursors are removed from the beverage at or about the temperature at which the haze precursors are precipitated.