Metallic ion removal from phosphoric acid

Claim 2

A process for the removal of at least one metallic ion impurity from phosphoric acid comprising the steps of: (a) adding to the acid a sludge precipitant comprising at least 50% by weight calcium fluoride on a dry basis; (b) allowing the formation of a precipitate containing the impurity; and (c) separating the precipitate from the acid.

Claim 3

The process of claim 1 wherein said metallic ion impurity comprises divalent magnesium.

Claim 4

The process of claim 1 wherein said metallic ion impurity comprises trivalent aluminum.

Claim 5

The process of claim 1 wherein said precipitant comprises a precipitated sludge obtained by treatment of wet process phosphoric acid plant pond water with a calcium compound to remove fluoride therefrom.

Claim 6

The process of claim 1 wherein, at least after addition of said precipitant, said impure phosphoric acid is maintained at a temperature in the range of about 115° to 140° F. for sufficient time to permit said precipitation to occur.

Claim 7

The process of claim 5 wherein said period of time is in the range of about 2 to 3 days.

Claim 8

The process of claim 1 wherein sulphuric acid is added to said phosphoric acid in an amount effective to increase the rate of precipitation of said impurities.

Claim 9

The process of claim 1 wherein said phosphoric acid is a wet process acid analyzing in the range of 38 to 54% P 2 O 5 .

Claim 10

The process of claim 8 wherein said acid is produced by a hemihydrate process.

Claim 11

The process of claim 1 wherein the molar ratio of calcium to fluorine in the precipitant is about 1:2.

Claim 12

Process for removal of magnesium ions from impure wet process phosphoric acid, said process comprising adding to the acid a precipitant comprising the sludge comprising calcium and fluoride ions obtained by addition of calcium ions to a fluoride containing pond water, said sludge also containing compounds of phosphorous, magnesium, iron, aluminum, sodium, silica and sulfur and, having a weight ratio MgO to F in the range of about 1 to 23 to about 1 to 260 and a molar ratio of calcium to fluorine of about 1:2; maintaining said acid, after adding said precipitant, at a temperature in the range of about 115° to 160° F. for sufficient time to permit a precipitate to form; and, separating said precipitate from the purified acid.

Claim 13

Process for removal of magnesium ions from impure wet process phosphoric acid, said process comprising adding to the acid a precipitant comprising the sludge comprising calcium and fluoride ions obtained by addition of calcium ions to a fluoride containing pond water, said sludge also containing compounds of phosphorous, magnesium, iron, aluminum, sodium, silica and sulfur and, having a weight ratio MgO to F in the range of about 1 to 23 to about 1 to 260 and a molar ratio of calcium to fluorine of about 1:2; maintaining said acid, after adding said precipitant, at a temperature in the range of about 115° to 160° F. for sufficient time to permit a precipitate to form; and, separating said precipitate from the purified acid.

Claim 14

The process of claim 11 wherein sulfuric acid is added to said phosphoric acid in an amount effective to increase the rate of formation of said precipitate.

Claim 15

The process of claim 12 wherein sulfuric acid is added to said phosphoric acid in an amount stoichiometric to the fluorine added to the phosphoric acid.

Claim 16

A process for removing magnesium ions and aluminum ions from phosphoric acid comprising the steps of: (a) treating phosphoric acid containing aluminum and magnesium ions by adding to the phosphoric acid a wetted precipitant comprising calcium and fluorine in a molar ratio of fluorine to calcium of about 2:1 in an amount sufficient to yield a molar ratio of fluorine ions to magnesium ions in the treated phosphoric acid mixture of from 3.8 to 5; (b) maintaining the treated phosphoric acid at an elevated temperature for a sufficient time to form a precipitate containing magnesium and aluminum; and (c) separating formed precipitate from the treated phosphoric acid.

Claim 17

A process for removing magnesium ions and aluminum ions from phosphoric acid comprising the steps of: (a) treating phosphoric acid containing aluminum and magnesium ions by adding to the phosphoric acid a wetted precipitant comprising calcium and fluorine in a molar ratio of fluorine to calcium of about 2:1 in an amount sufficient to yield a molar ratio of fluorine ions to magnesium ions in the treated phosphoric acid mixture of from 3.8 to 5; (b) maintaining the treated phosphoric acid at an elevated temperature for a sufficient time to form a precipitate containing magnesium and aluminum; and (c) separating formed precipitate from the treated phosphoric acid.

Claim 18

The process of claim 14 wherein the precipitant comprises a precipitated sludge obtained by treatment of wet process phosphoric acid plant pond water containing fluoride with a calcium compound.

Claim 19

The process of claim 14 wherein the treated phosphoric acid is maintained at an elevated temperature in the range of about 115° to 140° F.

Claim 20

The process of claim 16 wherein the treated phosphoric acid is maintained at an elevated temperature for a period of time in the range of about 2 to 6 days.

Claim 21

The process of claim 14 wherein the treated phosphoric acid is maintained at an elevated temperature for a period of time in the range of about 2 to 6 days.

Claim 22

The process of claim 14 wherein sulfuric acid is added to the phosphoric acid in an amount stoichoimetric to the fluorine added to the phosphoric acid.

Claim 23

The method of claim 14 in which the separated formed precipitate of step (c) comprises Ralstonite.

Claim 24

A process for removing impurities from wet process phosphoric acid comprising 38 to 54% by weight P 2 O 5 , 0.3 to 1.75% by weight MgO, as well as sodium, iron, and aluminum, comprising the steps of: (a) precipitating sludge from a fluoride containing wet process phosphoric acid plant pond water by adding a calcium compound to the pond water, the sludge comprising calcium and fluoride ions in a molar ratio of calcium to fluoride ions of about 1:2, and also containing compounds of phosphorus, magnesium, iron, aluminum, sodium, silica and sulfur, and having a weight ratio of MgO to F in the range of about 1:23 to about 1:260; (b) treating the phosphoric acid by combining the phosphoric acid with a sufficient quantity of such sludge for forming a precipitate; (c) maintaining the treated phosphoric acid at a temperature in the range of about 115° to 140° F. for a period of time in the range of about 2 to 6 days for forming a precipitate comprising sodium, aluminum, and magnesium; and (d) removing formed precipitate from the phosphoric acid.

Claim 25

A process for removing impurities from wet process phosphoric acid comprising 38 to 54% by weight P 2 O 5 , 0.3 to 1.75% by weight MgO, as well as sodium, iron, and aluminum, comprising the steps of: (a) precipitating sludge from a fluoride containing wet process phosphoric acid plant pond water by adding a calcium compound to the pond water, the sludge comprising calcium and fluoride ions in a molar ratio of calcium to fluoride ions of about 1:2, and also containing compounds of phosphorus, magnesium, iron, aluminum, sodium, silica and sulfur, and having a weight ratio of MgO to F in the range of about 1:23 to about 1:260; (b) treating the phosphoric acid by combining the phosphoric acid with a sufficient quantity of such sludge for forming a precipitate; (c) maintaining the treated phosphoric acid at a temperature in the range of about 115° to 140° F. for a period of time in the range of about 2 to 6 days for forming a precipitate comprising sodium, aluminum, and magnesium; and (d) removing formed precipitate from the phosphoric acid.