Phosphorus purification

Claim 3

The method according to claim 1 wherein the portion of the mass mixed with water is such as to provide a volume ratio of the mass to water of about 40:1.

Claim 4

The method according to claim 1 wherein the intense agitation is effected by passing the mixture through a restricted passage under conditions to create a turbulent flow of the mixture.

Claim 5

The method according to claim 1 wherein the intense agitation is effected by passing the mixture through a restricted passage under conditions whereby the mixture attains a Reynolds number of at least about 50,000.

Claim 6

The method according to claim 1 wherein the intense agitation is effected by passing the mixture through a pipeline under conditions whereby the mixture attains a Reynolds number of at least about 140,000.

Claim 7

A cyclic method for refining yellow phosphorus existing as a mass of liquid yellow phosphorus in a continuous phase and containing sufficient color-causing impurities to impart to the phosphorus a black color by reflected light which comprises forming an intimate mixture of a portion of the mass and water to provide a volume ratio of the portion of the mass to water of from about 2:1 to about 100:1, agitating intensely the mixture to effect a migration of color-causing impurities from the phosphorus to the phosphorus-water interface, adding the agitated mixture to the remainder of the mass to form a mass of liquid yellow phosphorus containing a lower proportion of color-causing impurities, repeating the cycle until sufficient color-causing impurities have been removed from the mass to impart to the liquid yellow phosphorus a yellow brown cast and separating refined yellow phosphorus from the aqueous phase containing the impurities.

Claim 8

A cyclic method for refining yellow phosphorus existing as a mass of liquid yellow phosphorus in a continuous phase and containing sufficient color-causing impurities to impart to the phosphorus a black color by reflected light which comprises forming an intimate mixture of a portion of the mass and water to provide a volume ratio of the portion of the mass to water of from about 2:1 to about 100:1, agitating intensely the mixture to effect a migration of color-causing impurities from the phosphorus to the phosphorus-water interface, adding the agitated mixture to the remainder of the mass to form a mass of liquid yellow phosphorus containing a lower proportion of color-causing impurities, repeating the cycle until sufficient color-causing impurities have been removed from the mass to impart to the liquid yellow phosphorus a yellow brown cast and separating refined yellow phosphorus from the aqueous phase containing the impurities.

Claim 9

The method according to claim 6 wherein the portion of the mass mixed with water is such so as to provide a volume ratio of phosphorus to water of about 40:1.

Claim 10

The method according to claim 6 wherein the mixture is agitated intensely by passing it through a restricted passage under conditions to create a turbulent flow of the mixture.

Claim 11

The method according to claim 6 wherein the mixture agitated intensely by passing it through a restricted passage under conditions whereby the mixture attains a Reynolds number of at least about 50,000.

Claim 12

The method according to claim 6 wherein the mixture is agitated intensely by passing it through a pipeline under conditions whereby the mixture attains a Reynolds number of at least about 140,000.

Claim 13

The method according to claim 6 wherein the cycles of treatment are repeated until the liquid yellow phosphorus has a color corresponding to Pantone Color 139.

Claim 14

A cyclic method for refining yellow phosphorus existing as a mass of liquid yellow phosphorus in a continuous phase and containing sufficient color-causing impurities to impart to the phosphorus a black color by reflected light which comprises the steps of continuously withdrawing a portion of the mass, mixing intensely the withdrawn portion with water in a volume ratio of liquid yellow phosphorus to water of from about 2:1 to about 100:1, subjecting the mixture to intense agitation so as to effect a migration of color-causing impurities from the phosphorus to the phosphorus-water interface, discharging the agitated mixture into the remainder of the mass, allowing the discharged mixture to stratify whereby the liquid phosphorus of the mixture commingles and coalesces with the remainder of the liquid phosphorus of the mass to form a mass of liquid phosphorus containing a lower proportion of color-causing impurities, continuing the cycle of steps until the withdrawn portion of the phosphorus exhibits a yellow brown cast and separating the refined liquid yellow phosphorus from the aqueous phase containing the impurities.

Claim 15

A cyclic method for refining yellow phosphorus existing as a mass of liquid yellow phosphorus in a continuous phase and containing sufficient color-causing impurities to impart to the phosphorus a black color by reflected light which comprises the steps of continuously withdrawing a portion of the mass, mixing intensely the withdrawn portion with water in a volume ratio of liquid yellow phosphorus to water of from about 2:1 to about 100:1, subjecting the mixture to intense agitation so as to effect a migration of color-causing impurities from the phosphorus to the phosphorus-water interface, discharging the agitated mixture into the remainder of the mass, allowing the discharged mixture to stratify whereby the liquid phosphorus of the mixture commingles and coalesces with the remainder of the liquid phosphorus of the mass to form a mass of liquid phosphorus containing a lower proportion of color-causing impurities, continuing the cycle of steps until the withdrawn portion of the phosphorus exhibits a yellow brown cast and separating the refined liquid yellow phosphorus from the aqueous phase containing the impurities.

Claim 16

The method according to claim 12 wherein intense agitation of the mixture is effected by passing the mixture through a restricted passage under conditions creating a turbulent flow of the mixture.

Claim 17

The method according to claim 12 wherein the conditions under which the mixture is passed through the restricted passage are such that the mixture attains a Reynolds number of at least about 50,000.

Claim 18

The method according to claim 12 wherein the mixture is passed through a pipeline under conditions whereby the mixture attains a Reynolds number of at least 50,000.

Claim 19

The method according to claim 12 wherein a portion of the mass is mixed with water in a volume ratio of about 40:1 and the mixture is passed through a pipeline under conditions whereby the mixture attains a Reynolds number of at least about 140,000.

Claim 20

The method according to claim 12 wherein a portion of the mass is mixed with water in a volume ratio of about 40:1, the mixture is passed through a pipeline under conditions whereby the mixture attains a Reynolds number of at least about 140,000 and the cycles of steps are continued until the phosphorus exhibits a color corresponding to Pantone Color 139.