Method of using higher concentration sulfuric acid for stripping and precipitation of adsorbed magnesium

Claim 2

In a folded bed ion exchange system for removing magnesium ions from aqueous phosphoric acid prepared by the wet process from phosphate rock, the method of regenerating a cation exchange resin loaded with adsorbed magnesium ions and precipitating the stripped magnesium ions, comprising: (a) sequentially introducing increments of said loaded resin into the bottom portion of a regeneration column while sequentially removing regenerated increments of said resin from the top portion of said column, said increments sequentially moving upwardly in said column from the bottom to the top thereof; (b) introducing an aqueous sulfuric acid (H 2 SO 4 ) regenerating solution into the top portion of said column at a concentration of 40% or higher H 2 SO 4 by weight and passing said regenerating solution downwardly within said column, the H 2 SO 4 concentration of said regenerating solution progressively decreasing as said solution flows downwardly through the upwardly moving resin increments, whereby the most recently introduced increment in the column bottom portion is in contact with an H 2 SO 4 solution of relatively low concentration while the increment in the top portion prior to its removal is in contact with an H 2 SO 4 solution of relatively high concentration; (c) removing a magnesium ion-containing sulfuric acid solution of reduced H 2 SO 4 concentration from the lower portion of said column, said removal acid concentration being at least 10 to 20% lower than the introduction concentration and below a concentration at which the magnesium ions precipitate; and (d) precipitating magnesium sulfate from said removed solution by increasing the H 2 SO 4 concentration of said solution to a sufficiently high H 2 SO 4 concentration to cause the magnesium sulfate to form a solid crystalline compound.

Claim 3

The method of claim 1 in which said regenerating solution as introduced into said column has a concentration of 40 to 70% H 2 SO 4 by weight.

Claim 4

The method of claim 1 in which said H 2 SO 4 solution as introduced in step (b) has a concentration of at least 50%, and in step (d) aqueous H 2 SO 4 is added which has a concentration of at least 80%.

Claim 5

The method of claim 1 in which said magnesium sulfate is precipitated at a concentration of at least 70% H 2 SO 4 by weight, and a supernatant solution of at least 70% H 2 SO 4 by weight is separated from the said precipitate.

Claim 6

The method of claim 1 in which said resin for regeneration contains adsorbed calcium ions together with the magnesium ions but not over one mole of calcium being present per each 9 moles of magnesium.

Claim 7

The method of claim 1 in which said resin for regeneration contains organic matter from the phosphate rock used to prepare the wet process phosphoric acid.

Claim 8

The method of claim 1 in which said resin for regeneration contains adsorbed calcium ions together with the adsorbed magnesium ions but not over one mole of calcium being present per each 9 moles of magnesium, and in which said resin contains organic matter from the phosphate rock used to prepare the wet process phosphoric acid.

Claim 9

The method of claim 1 in which the resin increments removed from the top of said column contain sulfuric acid at the high concentration of the regenerating solution as introduced, and in which the removed increments are first washed with aqueous sulfuric acid of an intermediate concentration with respect to the regenerating solution and water and thereafter washed with water.

Claim 12

The method of claim 9 in which said resin for regeneration contains adsorbed calcium ions together with the adsorbed magnesium ions but not over one mole of calcium being present per each 9 moles of magnesium, said resin also containing organic matter from the phosphate rock used to prepare the wet process phosphoric acid.

Claim 13

The method of claim 9 in which said precipitation is carried out at an H 2 SO 4 concentration of from 70 to 80% by weight, and by-product sulfuric acid is obtained at a corresponding concentration.

Claim 14

In a folded bed ion exchange system for removing magnesium ions from aqueous phosphoric acid prepared by the wet process from phosphate rock, the method of regenerating a cation exchange resin loaded with adsorbed magnesium ions and precipitating the stripped magnesium ions, comprising: (a) sequentially introducing increments of said loaded resin into the bottom portion of a regeneration column while sequentially removing regenerated increments of said resin from the top portion of said column, said increments sequentially moving upwardly in said column from the bottom to the top thereof, said resin as introduced into said column containing adsorbed calcium ions together with the adsorbed magnesium ions but not over one mole of calcium being present per each 9 moles of magnesium, and also containing organic matter from the phosphate rock used to prepare the wet process phosphoric acid; (b) introducing an aqueous sulfuric acid (H 2 SO 4 ) regenerating solution into the top portion of said column at a concentration of at least 50% H 2 SO 4 by weight and passing said regenerating solution downwardly within said column, the H 2 SO 4 concentration of said regenerating solution progressively decreasing as said solution flows downwardly through the upwardly moving resin increments, whereby the most recently introduced increment in the column bottom portion is in contact with an H 2 SO 4 solution of relatively low concentration while the increment in the top portion prior to its removal is in contact with an H 2 SO 4 solution of relatively high concentration; (c) removing a magnesium ion-containing sulfuric acid solution of reduced H 2 SO 4 concentration from the lower portion of said column, said removal acid concentration being at least 10 to 20% lower than the introduction concentration and below a concentration at which the magnesium ions precipitate; (d) precipitating magnesium sulfate from said removed solution by adding concentrated sulfuric acid thereto having an H 2 SO 4 concentration of at least 70% by weight to cause the magnesium sulfate to form a solid crystalline compound; and (e) separating the crystalline precipitate and also recovering an H 2 SO 4 solution of at least 70% by weight concentration.

Claim 15

In a folded bed ion exchange system for removing magnesium ions from aqueous phosphoric acid prepared by the wet process from phosphate rock, the method of regenerating a cation exchange resin loaded with adsorbed magnesium ions and precipitating the stripped magnesium ions, comprising: (a) sequentially introducing increments of said loaded resin into the bottom portion of a regeneration column while sequentially removing regenerated increments of said resin from the top portion of said column, said increments sequentially moving upwardly in said column from the bottom to the top thereof, said resin as introduced into said column containing adsorbed calcium ions together with the adsorbed magnesium ions but not over one mole of calcium being present per each 9 moles of magnesium, and also containing organic matter from the phosphate rock used to prepare the wet process phosphoric acid; (b) introducing an aqueous sulfuric acid (H 2 SO 4 ) regenerating solution into the top portion of said column at a concentration of at least 50% H 2 SO 4 by weight and passing said regenerating solution downwardly within said column, the H 2 SO 4 concentration of said regenerating solution progressively decreasing as said solution flows downwardly through the upwardly moving resin increments, whereby the most recently introduced increment in the column bottom portion is in contact with an H 2 SO 4 solution of relatively low concentration while the increment in the top portion prior to its removal is in contact with an H 2 SO 4 solution of relatively high concentration; (c) removing a magnesium ion-containing sulfuric acid solution of reduced H 2 SO 4 concentration from the lower portion of said column, said removal acid concentration being at least 10 to 20% lower than the introduction concentration and below a concentration at which the magnesium ions precipitate; (d) precipitating magnesium sulfate from said removed solution by adding concentrated sulfuric acid thereto having an H 2 SO 4 concentration of at least 70% by weight to cause the magnesium sulfate to form a solid crystalline compound; and (e) separating the crystalline precipitate and also recovering an H 2 SO 4 solution of at least 70% by weight concentration.