Metallic ion removal from phosphoric acid

Claim 2

A process for the removal of at least one metallic ion impurity from impure phosphoric acid comprising the steps of: (a) adding to the impure phosphoric acid a solid precipitant comprising calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said precipitant prepared by treatment of wet process phosphoric acid plant pond water with a calcium containing compound; (b) allowing the formation of a precipitate containing the impurity to yield a purified phosphoric acid; and (c) separating at least a portion of the precipitate from the purified phosphoric acid.

Claim 3

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 4

The process of claim 2 wherein said period of time is in the range of about 2 to 6 days.

Claim 5

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

Claim 6

The process of claim 4 wherein said impure phosphoric acid is produced by a hemihydrate process.

Claim 7

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

Claim 8

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

Claim 9

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

Claim 10

The process of claim 1 wherein the precipitant contains, on analysis, calcium to F in a molar ratio of about 1:2.

Claim 11

A process as claimed in claim 1 in which the solid precipitant comprises calcium fluoride.

Claim 12

A process for removal of magnesium ions from impure wet process phosphoric acid, said process comprising: adding to the acid a precipitant comprising a sludge comprising calcium and fluoride ions obtained by addition of calcium ions to a fluoride containing pond water, to form calcium and fluorine containing solids having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said sludge 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 and a molar ratio of calcium to F 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 yield a purified phosphorus acid; and separating said precipitate from the purified phosphoric acid.

Claim 13

A process for removal of magnesium ions from impure wet process phosphoric acid, said process comprising: adding to the acid a precipitant comprising a sludge comprising calcium and fluoride ions obtained by addition of calcium ions to a fluoride containing pond water, to form calcium and fluorine containing solids having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said sludge 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 and a molar ratio of calcium to F 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 yield a purified phosphorus acid; and separating said precipitate from the purified phosphoric acid.

Claim 14

The process of claim 11 wherein sulfuric acid is added to said impure wet process 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 impure wet process 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 precipitant comprising calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said precipitant prepared by treatment of wet process phosphoric acid plant pond water with a calcium containing compound, in an amount sufficient to yield a molar ratio of F ions to magnesium ions in the treated phosphoric acid of from 3.8:1 to 5:1; (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 the 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 precipitant comprising calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said precipitant prepared by treatment of wet process phosphoric acid plant pond water with a calcium containing compound, in an amount sufficient to yield a molar ratio of F ions to magnesium ions in the treated phosphoric acid of from 3.8:1 to 5:1; (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 the formed precipitate from the treated phosphoric acid.

Claim 18

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

Claim 19

The process of claim 15 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 20

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 21

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

Claim 22

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

Claim 23

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 to form solids containing calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, 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 wet process phosphoric acid by combining the wet process phosphoric acid with a sufficient quantity of 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 treated wet process phosphoric acid.

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 to form solids containing calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, 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 wet process phosphoric acid by combining the wet process phosphoric acid with a sufficient quantity of 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 treated wet process phosphoric acid.

Claim 25

In a hemi-hydrate wet-process for producing phosphoric acid wherein a slurry comprising phosphoric acid and calcium sulfate is formed, and an impure phosphoric acid containing at least 38% by weight P 2 O 5 is recovered from the slurry, the improvement for removal of at least one metallic ion impurity from the impure phosphoric acid comprising the steps of: (a) adding a solid precipitant comprising calcium and fluorine to the impure phosphoric acid; (b) allowing formation of a precipitate containing the metallic ion impurity to yield a purified phosphoric acid; and (c) separating at least a portion of the precipitate from the purified phosphoric acid.

Claim 26

In a hemi-hydrate wet-process for producing phosphoric acid wherein a slurry comprising phosphoric acid and calcium sulfate is formed, and an impure phosphoric acid containing at least 38% by weight P 2 O 5 is recovered from the slurry, the improvement for removal of at least one metallic ion impurity from the impure phosphoric acid comprising the steps of: (a) adding a solid precipitant comprising calcium and fluorine to the impure phosphoric acid; (b) allowing formation of a precipitate containing the metallic ion impurity to yield a purified phosphoric acid; and (c) separating at least a portion of the precipitate from the purified phosphoric acid.

Claim 27

The process of claim 21 wherein said metallic ion impurity comprises divalent magnesium.

Claim 28

The process of claim 21 wherein said metallic ion impurity comprises trivalent aluminum.

Claim 29

The process of claim 21 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 30

The process of claim 21 wherein sulfuric acid is added to said phosphoric acid in an amount effective to increase the rate of precipitation of said impurity.

Claim 31

The process of claim 21 wherein the molar ratio of calcium to fluorine in the precipitant is about 1:2.

Claim 32

A process as claimed in claim 21 in which the solid precipitant comprises calcium fluoride.

Claim 33

A batch process for reducing the magnesium content of phosphoric acid produced by a dihydrate process and containing from about 46 to about 54% by weight P 2 O 5 , to a low weight ratio of MgO to P 2 O 5 , soluble, which comprises the steps of: (a) adding to the phosphoric acid a solid precipitant containing calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said precipitant prepared by treatment of wet process phosphoric acid plant pond water with a calcium-containing compound; (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a low weight ratio of MgO:P 2 O 5 , soluble.

Claim 34

A batch process for reducing the magnesium content of phosphoric acid produced by a dihydrate process and containing from about 46 to about 54% by weight P 2 O 5 , to a low weight ratio of MgO to P 2 O 5 , soluble, which comprises the steps of: (a) adding to the phosphoric acid a solid precipitant containing calcium and fluorine and having a dry basis analysis of at least 20% by weight calcium oxide and at least 19% by weight F, said precipitant prepared by treatment of wet process phosphoric acid plant pond water with a calcium-containing compound; (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a low weight ratio of MgO:P 2 O 5 , soluble.

Claim 35

A process as claimed in claim 28 in which the solid precipitant comprises calcium fluoride.

Claim 36

A process for the removal of at least one metallic ion impurity contained in impure phosphoric acid which comprises the steps of (a) adding to the impure phosphoric acid a precipitant which is a solids-containing sludge, the sludge containing about 50% by weight water and the solids of the sludge providing a dry basis, by weight analysis of: P, 3 to 10%; Mg, 0.05 to 0.3%; Ca, 20 to 35%; Fe, 0.3 to 3.0%; Al, 1 to 5%; Na, 0.7 to 3.0%; Si, 0.5 to 8.0%; F, 13 to 30% and SO 4 , 3 to 15%; (b) allowing the formation of a precipitate containing the metallic ion impurity to form a purified phosphoric acid; (c) separating at least a portion of the precipitate from the purified phosphoric acid.

Claim 37

A process for the removal of at least one metallic ion impurity contained in impure phosphoric acid which comprises the steps of (a) adding to the impure phosphoric acid a precipitant which is a solids-containing sludge, the sludge containing about 50% by weight water and the solids of the sludge providing a dry basis, by weight analysis of: P, 3 to 10%; Mg, 0.05 to 0.3%; Ca, 20 to 35%; Fe, 0.3 to 3.0%; Al, 1 to 5%; Na, 0.7 to 3.0%; Si, 0.5 to 8.0%; F, 13 to 30% and SO 4 , 3 to 15%; (b) allowing the formation of a precipitate containing the metallic ion impurity to form a purified phosphoric acid; (c) separating at least a portion of the precipitate from the purified phosphoric acid.

Claim 38

The process of claim 30 wherein said impure phosphoric acid is a wet process acid analyzing in the range of 38% to 54% by weight P 2 O 5 .

Claim 39

The process of claim 31 wherein said impure phosphoric acid is produced by a hemi-hydrate process.

Claim 40

The process of claim 30 wherein said metallic ion impurity comprises divalent magnesium.

Claim 41

The process of claim 30 wherein said metallic ion impurity comprises trivalent aluminum.

Claim 42

The process of claim 30 wherein, at least after addition of said precipitant, said impure phosphoric acid is maintained at a temperature in the range of about 115° F. to 140° F. for sufficient time to permit said precipitation to occur.

Claim 43

The process of claim 30 wherein said period of time is in the range of about 2 to 6 days.

Claim 44

A process as claimed in claim 30 wherein sulfuric acid is added to the impure phosphoric acid in an amount effective to increase the rate of precipitation of the metallic ion impurity.

Claim 45

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) adding to the impure phosphoric acid a precipitant which is a solids containing sludge, the sludge containing about 50% by weight water and the solids of the sludge providing a dry basis, by weight analysis of: P, 3 to 10%; Mg, 0.05 to 0.3%; Ca, 20 to 35%; Fe, 0.3 to 3.0%; Al, 1 to 5%; Na, 0.7 to 3.0%; Si, 0.5 to 8.0%; F, 13 to 30% and SO 4 , 3 to 15%; (b) maintaining the treated phosphoric acid at a temperature in the range of about 115° F. to 140° F. for a period of time in the range of about 2 to 6 days to form a precipitate comprising sodium, aluminum, and magnesium; and (c) removing the formed precipitate from the phosphoric acid.

Claim 46

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) adding to the impure phosphoric acid a precipitant which is a solids containing sludge, the sludge containing about 50% by weight water and the solids of the sludge providing a dry basis, by weight analysis of: P, 3 to 10%; Mg, 0.05 to 0.3%; Ca, 20 to 35%; Fe, 0.3 to 3.0%; Al, 1 to 5%; Na, 0.7 to 3.0%; Si, 0.5 to 8.0%; F, 13 to 30% and SO 4 , 3 to 15%; (b) maintaining the treated phosphoric acid at a temperature in the range of about 115° F. to 140° F. for a period of time in the range of about 2 to 6 days to form a precipitate comprising sodium, aluminum, and magnesium; and (c) removing the formed precipitate from the phosphoric acid.

Claim 47

A process as claimed in claim 38 in which the wet process phosphoric acid is produced by a hemihydrate process.

Claim 48

A process as claimed in claim 38 wherein sulfuric acid is added to the wet process phosphoric acid in an amount effective to increase the rate of formation of the precipitate.

Claim 49

A batch process for reducing the magnesium content of phosphoric acid produced by a hemi-hydrate process and containing from about 46% to about 54% by weight P 2 O 5 so that the weight ratio of MgO to P 2 O 5 ,soluble, is no greater than a selected value which comprises the steps of: (a) adding to the phosphoric acid a solid precipitant containing at least 50% by weight calcium and F prepared by treatment of wet process phosphoric acid plant pond water with a calcium-containing compound, the amount of precipitant added being sufficient to substantially satisfy the equation: ##EQU6## where, [SNS]=the amount of precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated and in the range of 0% ≦[SNS]≦10%; Y=the final ratio of MgO to P 2 O 5 soluble expressed as 100 [MgO]/[P 2 O 5 ]; and X=the initial ratio of MgO to P 2 O 5 , initial total expressed as 100 [MgO]/[P 2 O 5 ]; (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a weight ratio of MgO:P 2 O 5 , soluble, of less than about Y.

Claim 50

A batch process for reducing the magnesium content of phosphoric acid produced by a hemi-hydrate process and containing from about 46% to about 54% by weight P 2 O 5 so that the weight ratio of MgO to P 2 O 5 ,soluble, is no greater than a selected value which comprises the steps of: (a) adding to the phosphoric acid a solid precipitant containing at least 50% by weight calcium and F prepared by treatment of wet process phosphoric acid plant pond water with a calcium-containing compound, the amount of precipitant added being sufficient to substantially satisfy the equation: ##EQU6## where, [SNS]=the amount of precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated and in the range of 0% ≦[SNS]≦10%; Y=the final ratio of MgO to P 2 O 5 soluble expressed as 100 [MgO]/[P 2 O 5 ]; and X=the initial ratio of MgO to P 2 O 5 , initial total expressed as 100 [MgO]/[P 2 O 5 ]; (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a weight ratio of MgO:P 2 O 5 , soluble, of less than about Y.

Claim 51

A process as claimed in claim 41 in which the solid precipitant comprises calcium fluoride.

Claim 52

A three-stage continuous-stirred tank process for reducing the magnesium content of phosphoric acid produced by a hemi-hydrate process and containing from about 46% to about 54% by weight P 2 O 5 , so that the weight ratio of MgO to P 2 O 5 , soluble, is no greater than a selected value which comprises the steps of: (a) adding to the phosphoric acid a solid precipitant containing at least 50% by weight calcium and F prepared by treatment of wet process phosphoric acid plant pond water with a calcium-containing compound, the amount of precipitant added being sufficint to substantially satisfy the equation: ##EQU7## where, [SNS]=the amount of precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated and in the range of 0% ≦[SNS]≦10%; Y=the final ratio of MgO to P 2 O 5 soluble expressed as 100 [MgO]/[P 2 O 5 , initial total expressed as 100 [MgO]/[P 2 O 5 ]; (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a weight ratio of MgO:P 2 O 5 , soluble, of less than about Y.

Claim 53

A three-stage continuous-stirred tank process for reducing the magnesium content of phosphoric acid produced by a hemi-hydrate process and containing from about 46% to about 54% by weight P 2 O 5 , so that the weight ratio of MgO to P 2 O 5 , soluble, is no greater than a selected value which comprises the steps of: (a) adding to the phosphoric acid a solid precipitant containing at least 50% by weight calcium and F prepared by treatment of wet process phosphoric acid plant pond water with a calcium-containing compound, the amount of precipitant added being sufficint to substantially satisfy the equation: ##EQU7## where, [SNS]=the amount of precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated and in the range of 0% ≦[SNS]≦10%; Y=the final ratio of MgO to P 2 O 5 soluble expressed as 100 [MgO]/[P 2 O 5 , initial total expressed as 100 [MgO]/[P 2 O 5 ]; (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a weight ratio of MgO:P 2 O 5 , soluble, of less than about Y.

Claim 54

A process as claimed in claim 43 in which the solid precipitant comprises calcium fluoride.

Claim 55

A three-stage continuous-stirred tank process for reducing the magnesium content of phosphoric acid produced by a di-hydrate process and containing from about 46% to about 54% by weight P 2 O 5 , so that the weight ratio of MgO to P 2 O 5 , soluble, is no greater than a selected value which comprises the steps of: (a) adding to the phosphoric acid solid precipitant containing at least 50% by weight calcium and F prepared by treament of wet process phosphoric acid plant pond water with a calcium-containing compound, the amount of precipitant added being sufficient to substantially satisfy the equation: ##EQU8## where, [SNS]=the amount of precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated and in the range of 0%≦[SNS]≦10%; Y=the final ratio of MgO to P 2 O 5 soluble expressed as 100 [MgO]/[P 2 O 5 ); and X=the initial ratio of MgO to P 2 O 5 , initial total expressed as 100 [MgO]/[P 2 O 5 ); (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a weight ratio of MgO:P 2 O 5 , soluble, of less than about Y.

Claim 56

A three-stage continuous-stirred tank process for reducing the magnesium content of phosphoric acid produced by a di-hydrate process and containing from about 46% to about 54% by weight P 2 O 5 , so that the weight ratio of MgO to P 2 O 5 , soluble, is no greater than a selected value which comprises the steps of: (a) adding to the phosphoric acid solid precipitant containing at least 50% by weight calcium and F prepared by treament of wet process phosphoric acid plant pond water with a calcium-containing compound, the amount of precipitant added being sufficient to substantially satisfy the equation: ##EQU8## where, [SNS]=the amount of precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated and in the range of 0%≦[SNS]≦10%; Y=the final ratio of MgO to P 2 O 5 soluble expressed as 100 [MgO]/[P 2 O 5 ); and X=the initial ratio of MgO to P 2 O 5 , initial total expressed as 100 [MgO]/[P 2 O 5 ); (b) maintaining the soluble sulfate content of the phosphoric acid at at least about 2% by weight; (c) thereafter, aging the phosphoric acid at a temperature from about 135° F. to about 160° F. for up to about four days to allow the formation of a precipitate containing magnesium; and (d) separating formed precipitate from the phosphoric acid to produce a phosphoric acid having a weight ratio of MgO:P 2 O 5 , soluble, of less than about Y.

Claim 57

A process as claimed in claim 45 in which the amount of precipitant added is from about 106% to about 110% of the amount determined to satisfy the equation.

Claim 58

The process of claims 28, 41, 43, 45 or 46 in which the step of maintaining the soluble sulfate content comprises adding to the phosphoric acid at least a quantity of sulfuric acid which substantially satisfies the equation: ##EQU9## where, [H 2 SO 4 ]=the amount of H 2 SO 4 to be added to the phosphoric acid expressed as weight percent of the phosphoric acid to be treated; [H 2 SO 4 ] 0 =the initial soluble H 2 SO 4 as percent by weight of the phosphoric acid to be treated. [SNS]=the amount of the precipitant to be added on a dry basis as a percent by weight of the phosphoric acid to be treated. [F] SNS =weight percent of fluorine in the precipitant on a dry basis.

Claim 59

A process as claimed in claim 45 in which the solid precipitant comprises calcium fluoride.