Process for removing solid organic material from wet-process phosphoric acid

Claim 2

A process for removing solid organic material from wet-process phosphoric acid derived from the acidulation of uncalcined phosphate rock without otherwise altering the chemical composition of aqueous solution comprising: a. mixing the wet-process phosphoric acid with a liquid consisting essentially of one or more hydrocarbons at a temperature of not less than about 55° C nor more than about 70° C and at a volume ratio of aqueous to organic up to about 30:1 so that the aqueous phase is continuous to emulsify substantially all of said organic material in said liquid hydrocarbon; b. allowing the mixture to separate into an aqueous phase containing substantially all of the phosphoric acid and an organic phase containing substantially all of said solid organic material; and c. separating the phosphoric acid aqueous phase from the organic phase.

Claim 3

A process according to claim 1 wherein the volume ratio of the aqueous phase to the organic phase is at least 1:1.

Claim 4

A process according to claim 2 wherein said volume ratio is between 1:1 and 2:1.

Claim 5

A process according to claim 1 wherein said liquid hydrocarbon is hexane, kerosene, gasoline, benzene, toluene or naphthene solvents.

Claim 6

A process according to claim 1 wherein said liquid hydrocarbon is a refined high-boiling, high-flash point solvent.

Claim 7

A process according to claim 1 wherein the organic phase containing the solid organic material of steps (b) and (c) is treated to remove the solid organic material contained therein and thereafter recycled for contacting with fresh wet-process phosphoric acid.

Claim 8

A process according to claim 1 wherein said wet-process phosphoric acid has a concentration of about 28 to 31% P 2 O 5 .

Claim 9

A process according to claim 1 wherein said liquid hydrocarbon has a boiling point above about 70° C under atmospheric pressure.

Claim 10

A process according to claim 1 wherein said liquid hydrocarbon has a boiling point above about 125° C under atmospheric pressure.

Claim 11

A process according to claim 1 wherein said liquid hydrocarbon is essentially immiscible with said wet-process phosphoric acid and has a substantially zero extraction coefficient for said wet-process phosphoric acid.

Claim 12

A process for removing solid organic material from wet-process phosphoric acid containing uranium which is derived from the sulfuric acid acidulation of uncalcined phosphate rock comprising: a. intimately contacting said wet-process phosphoric acid with a liquid having a substantially zero extraction coefficient for uranium, said liquid comprising a liquid hydrocarbon, at a temperature of not less than about 55° C nor more than about 70° C so that the aqueous phase is continuous and the solid organic material is emulsified within said liquid hydrocarbon; b. allowing the mixture thus formed to settle in a first zone into a purified acid phase containing substantially all of the phosphoric acid and a liquid hydrocarbon phase containing substantially all of the solid organic material suspended therein; c. withdrawing purified wet-process phosphoric acid from the purified acid phase of the first zone; d. transferring a portion of the liquid hydrocarbon phase from said first zone to a second zone; allowing the portion of the liquid hydrocarbon phase in said second zone to separate into an emulsion, a purified hydrocarbon phase and a phosphoric acid phase; f. filtering said emulsion to obtain solid organic material and a filtrate; and g. recycling said filtrate, a portion of said purified hydrocarbon phase, and a portion of said phosphoric acid phase for contacting an additional amount of wet-process phosphoric acid containing solid organic material.

Claim 13

A process for removing solid organic material from wet-process phosphoric acid containing uranium which is derived from the sulfuric acid acidulation of uncalcined phosphate rock comprising: a. intimately contacting said wet-process phosphoric acid with a liquid having a substantially zero extraction coefficient for uranium, said liquid comprising a liquid hydrocarbon, at a temperature of not less than about 55° C nor more than about 70° C so that the aqueous phase is continuous and the solid organic material is emulsified within said liquid hydrocarbon; b. allowing the mixture thus formed to settle in a first zone into a purified acid phase containing substantially all of the phosphoric acid and a liquid hydrocarbon phase containing substantially all of the solid organic material suspended therein; c. withdrawing purified wet-process phosphoric acid from the purified acid phase of the first zone; d. transferring a portion of the liquid hydrocarbon phase from said first zone to a second zone; allowing the portion of the liquid hydrocarbon phase in said second zone to separate into an emulsion, a purified hydrocarbon phase and a phosphoric acid phase; f. filtering said emulsion to obtain solid organic material and a filtrate; and g. recycling said filtrate, a portion of said purified hydrocarbon phase, and a portion of said phosphoric acid phase for contacting an additional amount of wet-process phosphoric acid containing solid organic material.

Claim 14

A process according to claim 11 wherein the recycle ratio of the recycle step is sufficient so that when said hydrocarbon is contacted with said wet-process phosphoric acid, the volume ratio of the wet-process phosphoric acid to the hydrocarbon is at least 1:1.

Claim 15

A process according to claim 12 wherein said volume ratio is about 1:1 to 2:1.

Claim 16

A process according to claim 12 wherein said hydrocarbon is a refined high-boiling, high-flash point solvent.

Claim 17

A process according to claim 11 wherein the material recycled in step (g) is mixed with the purified, wet-process phosphoric acid of step (c), the mixture thereby formed is allowed to separate into a second aqueous phase and a second organic phase, the second aqueous phase is withdrawn from the second organic phase, and the second organic phase is contacted with the wet-process phosphoric acid feed.

Claim 18

A process for removing organic solids from freshly produced wet-process phosphoric acid having a concentration of about 28 to 31% P 2 O 5 and containing uranium, inorganic solids including calcium sulfate and organic solids including humic acid solids comprising intimately mixing the phosphoric acid with a liquid having a substantially zero extraction coefficient for uranium, said liquid comprising a liquid hydrocarbon, at a temperature of not less than about 55° C nor more than about 70° C in a manner such that the aqueous phase is continuous, permitting the two phases to separate in a separator tank having a conical bottom which has an angle with the horizontal of not less than 45° and an aqueous outlet near the apex of the cone, removing the liquid hydrocarbon along with the emulsified organic solids and any entrained phosphoric acid overhead from the separator tank to a settling tank, permitting the organic solids to consolidate, recycling the liquid hydrocarbon, separating the organic solids from entrained phosphoric acid and liquid hydrocarbon by filtration and returning the filtrate to the process.

Claim 19

A process for removing organic solids from freshly produced wet-process phosphoric acid having a concentration of about 28 to 31% P 2 O 5 and containing uranium, inorganic solids including calcium sulfate and organic solids including humic acid solids comprising intimately mixing the phosphoric acid with a liquid having a substantially zero extraction coefficient for uranium, said liquid comprising a liquid hydrocarbon, at a temperature of not less than about 55° C nor more than about 70° C in a manner such that the aqueous phase is continuous, permitting the two phases to separate in a separator tank having a conical bottom which has an angle with the horizontal of not less than 45° and an aqueous outlet near the apex of the cone, removing the liquid hydrocarbon along with the emulsified organic solids and any entrained phosphoric acid overhead from the separator tank to a settling tank, permitting the organic solids to consolidate, recycling the liquid hydrocarbon, separating the organic solids from entrained phosphoric acid and liquid hydrocarbon by filtration and returning the filtrate to the process.

Claim 20

A process for removing solid organic material from freshly produced wet-process phosphoric acid having a concentration of about 28 to 31% P 2 O 5 derived from the acidulation of uncalcined phosphate rock and containing uranium without otherwise altering the chemical composition of the aqueous solution comprising: a. mixing the wet-process phosphoric acid with a liquid consisting essentially of one or more hydrocarbons at a temperature of not less than about 55° C nor more than about 70° C and at a volume ratio of aqueous to organic of about 1:1 to about 5:1 so that the aqueous phase is continuous to emulsify substantially all of said organic material in said liquid hydrocarbon, said liquid hydrocarbon having a boiling point above about 125° C under atmospheric pressure, said liquid hydrocarbon being essentially immiscible with said wet-process phosphoric acid and having a substantially zero extraction coefficient for said wet-process phosphoric acid and said uranium; b. allowing the mixture to separate into an aqueous phase containing substantially all of the phosphoric acid and an organic phase containing substantially all of said solid organic material, said separation occurring within about 10 minutes after said mixing; and c. separating the phosphoric acid aqueous phase from the organic phase.

Claim 21

A process for removing solid organic material from freshly produced wet-process phosphoric acid having a concentration of about 28 to 31% P 2 O 5 derived from the acidulation of uncalcined phosphate rock and containing uranium without otherwise altering the chemical composition of the aqueous solution comprising: a. mixing the wet-process phosphoric acid with a liquid consisting essentially of one or more hydrocarbons at a temperature of not less than about 55° C nor more than about 70° C and at a volume ratio of aqueous to organic of about 1:1 to about 5:1 so that the aqueous phase is continuous to emulsify substantially all of said organic material in said liquid hydrocarbon, said liquid hydrocarbon having a boiling point above about 125° C under atmospheric pressure, said liquid hydrocarbon being essentially immiscible with said wet-process phosphoric acid and having a substantially zero extraction coefficient for said wet-process phosphoric acid and said uranium; b. allowing the mixture to separate into an aqueous phase containing substantially all of the phosphoric acid and an organic phase containing substantially all of said solid organic material, said separation occurring within about 10 minutes after said mixing; and c. separating the phosphoric acid aqueous phase from the organic phase.

Claim 22

A process for removing solid organic material from freshly produced wet-process phosphoric acid having a concentration of about 28 to 31% P 2 O 5 derived from the acidulation of uncalcined phosphate rock and containing uranium without otherwise altering the chemical composition of the aqueous solution comprising: a. mixing the wet-process phosphoric acid with a liquid consisting essentially of one or more hydrocarbons at a temperature of not less than about 55° C nor more than about 70° C and at a volume ratio of aqueous to organic of about 1:1 to about 5:1 to emulsify said organic material in said liquid hydrocarbon, said liquid hydrocarbon being essentially immiscible with said wet-process phosphoric acid and having a substantially zero extraction coefficient for said wet-process phosphoric acid and said uranium; b. allowing the mixture to separate into an aqueous phase containing substantially all of the phosphoric acid and an organic phase containing substantially all of said emulsified solid organic material; and c. separting the phosphoric acid aqueous phase from the organic phase.

Claim 23

A process for removing solid organic material from freshly produced wet-process phosphoric acid having a concentration of about 28 to 31% P 2 O 5 derived from the acidulation of uncalcined phosphate rock and containing uranium without otherwise altering the chemical composition of the aqueous solution comprising: a. mixing the wet-process phosphoric acid with a liquid consisting essentially of one or more hydrocarbons at a temperature of not less than about 55° C nor more than about 70° C and at a volume ratio of aqueous to organic of about 1:1 to about 5:1 to emulsify said organic material in said liquid hydrocarbon, said liquid hydrocarbon being essentially immiscible with said wet-process phosphoric acid and having a substantially zero extraction coefficient for said wet-process phosphoric acid and said uranium; b. allowing the mixture to separate into an aqueous phase containing substantially all of the phosphoric acid and an organic phase containing substantially all of said emulsified solid organic material; and c. separting the phosphoric acid aqueous phase from the organic phase.