Abstract A process is disclosed for making a rare-earth oxysulfide phosphor resistant to hydrolysis, which comprises forming a slurry of the phosphor in water, adding to the slurry, a zinc compound in an amount sufficient to result in a zinc ion concentration in the water of from about 0.01 molar to about 0.05 molar, separating the resulting zinc-treated phosphor from the liquid portion of the slurry, heating the zinc-treated phosphor in air at a temperature of from about 500° C. to about 600° C. for a sufficient time to enhance the brightness of the phosphor, and screening the resulting heated phosphor to remove non-luminescent material therefrom. The phosphor has a resistance to hydrolysis that is at least about 50% greater than phosphors produced without the zinc treatment.
A process for making a rare-earth oxysulfide phosphor resistant to hydrolysis, said process comprising: (a) forming a slurry of said phosphor in water; (b) treating said slurry with a zinc compound, said treating consisting of adding to said slurry, a water-soluble zinc compound in an amount sufficient to result in a zinc ion concentration in said water of from about 0.01 molar to about 0.05 molar, and agitating said slurry; (c) separating the resulting zinc-treated phosphor from the liquid portion of said slurry; (d) heating said zinc-treated phosphor in air at a temperature of from about 500° C. to about 600° C. for a sufficient time to enhance the brightness of said phosphor; and (e) screening the resulting heated phosphor to remove nonluminescent material therefrom, said phosphor having a resistance to hydrolysis that is at least about 50% greater than said rare-earth oxysulfide phosphor absent the zinc treatment.
Claim 2
Dependent Claim
148 words
A process for making a rare-earth oxysulfide phosphor resistant to hydrolysis, said process comprising: (a) forming a slurry of said phosphor in water; (b) treating said slurry with a zinc compound, said treating consisting of adding to said slurry, a water-soluble zinc compound in an amount sufficient to result in a zinc ion concentration in said water of from about 0.01 molar to about 0.05 molar, and agitating said slurry; (c) separating the resulting zinc-treated phosphor from the liquid portion of said slurry; (d) heating said zinc-treated phosphor in air at a temperature of from about 500° C. to about 600° C. for a sufficient time to enhance the brightness of said phosphor; and (e) screening the resulting heated phosphor to remove nonluminescent material therefrom, said phosphor having a resistance to hydrolysis that is at least about 50% greater than said rare-earth oxysulfide phosphor absent the zinc treatment.
Claim 3
Dependent Claim
46 words
A process of claim 1 wherein said phosphor consists essentially of a host selected from the group consisting of gadolinium oxysulfide, yttrium oxysulfide, gadolinium-yttrium oxysulfide, and lanthanum oxysulfide, and from about 0.001 moles to about 0.10 moles of terbium per mole of host as an activator.