Determination of grain refiners in phosphate conversion coating baths

Claim 2

A process for determining the concentration of a phosphorous containing organic grain refiner in an aqueous, acidic conversion coating bath which includes an inorganic divalent metal phosphate comprising, determining the chemical oxygen demand of the bath, precipitating the grain refiner from a portion of the bath by raising the pH to above about 4.0 in the presence of excess metal ion, determining the chemical oxygen demand of the precipitated portion of the bath, and determining the concentration of grain refiner in the bath from the difference between the chemical oxygen demand of the bath and the precipitated portion of the bath.

Claim 3

The process of claim 1 wherein the grain refiner is precipitated by adding a base to raise the pH to at least about 4.0 in the presence of a metal ion which forms an insoluble salt with the organic phosphorous compound.

Claim 4

The process of claim 2 wherein the grain refiner is precipitated by raising the pH to at least about 6.5.

Claim 5

The process of claim 3 wherein the metal ion is selected from the group consisting of zinc, nickel, magnesium, calcium, manganese, bismuth, lead and mixtures thereof.

Claim 6

The process of claim 1 wherein the phosphate is zinc phosphate.

Claim 7

The process of claim 5 wherein the grain refiner is selected from the group consisting of acidic organic phosphates and phosphonates having at least one free hydroxyl group.

Claim 8

The process of claim 6 wherein the grain refiner is 1-hydroxyethylidene-1,1-diphosphonic acid.

Claim 9

In a process for forming a metal phosphate conversion coating on a metal surface which comprises contacting the metal surface with a heated, acidic, aqueous bath which includes a divalent metal phosphate, an oxidizing accelerator and a grain refiner selected from the group consisting of acidic organic phosphates and phosphonates having at least one free hydroxyl group, the improvement comprising monitoring the amount of grain refiner in the bath by periodically determining the chemical oxygen demand of the bath, precipitating the grain refiner from a portion of the bath by raising the pH to above about 4.0 in the presence of excess metal ion, determining the chemical oxygen demand of the precipitated portion of the bath, determining the concentration of grain refiner in the bath from the difference between the chemical oxygen demand of the bath and the precipitated bath sample and adjusting the amount of grain refiner in the bath to bring it to a desired concentration.

Claim 10

In a process for forming a metal phosphate conversion coating on a metal surface which comprises contacting the metal surface with a heated, acidic, aqueous bath which includes a divalent metal phosphate, an oxidizing accelerator and a grain refiner selected from the group consisting of acidic organic phosphates and phosphonates having at least one free hydroxyl group, the improvement comprising monitoring the amount of grain refiner in the bath by periodically determining the chemical oxygen demand of the bath, precipitating the grain refiner from a portion of the bath by raising the pH to above about 4.0 in the presence of excess metal ion, determining the chemical oxygen demand of the precipitated portion of the bath, determining the concentration of grain refiner in the bath from the difference between the chemical oxygen demand of the bath and the precipitated bath sample and adjusting the amount of grain refiner in the bath to bring it to a desired concentration.

Claim 11

The process of claim 8 wherein the grain refiner is precipitated by adding a base to raise the pH to at least about 4.0 in the presence of a metal ion which forms an insoluble salt with the organic phosphorous compound.

Claim 12

The process of claim 9 wherein the grain refiner is precipitated by raising the pH to at least about 6.5.

Claim 13

The process of claim 10 wherein the metal ion is selected from the group consisting of zinc, nickel, magnesium, calcium, manganese, bismuth, lead and mixtures thereof.

Claim 14

The process of claim 8 wherein the phosphate is zinc phosphate.

Claim 15

The process of claim 12 wherein the grain refiner is selected from the group consisting of acidic organic phosphates and phosphonates having at least one free hydroxyl group.

Claim 16

The process of claim 13 wherein the grain refiner is 1-hydroxyethylidene-1,1-diphosphonic acid.