Molten metaphosphate electrolysis for production of white phosphorus
US-11767597-B2 · Sep 26, 2023 · US
US12559372B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12559372-B2 |
| Application number | US-202017789051-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 9, 2020 |
| Priority date | Dec 27, 2019 |
| Publication date | Feb 24, 2026 |
| Grant date | Feb 24, 2026 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A method for producing phosphorus in which a reaction for forming gaseous phosphorus (g) by bringing phosphorus oxide generated by heating a liquid phosphoric acid compound into contact with a carbon material to reduce the phosphorus oxide and for condensing the gaseous phosphorus (g) to obtain liquid phosphorus (L) is conducted by a flow reaction with a nonoxidizing gas flow, wherein the reduction reaction of the phosphorus oxide is conducted in a carbon material-packed bed, and the condensation of the formed gaseous phosphorus (g) is substantially conducted in a condensation accelerator-packed bed which is disposed downstream of the carbon material-packed bed in contact with the carbon material-packed bed.
Opening claim text (preview).
The invention claimed is: 1 . A method for producing phosphorus, the method comprising: a reduction reaction for forming gaseous phosphorus (g) by bringing phosphorus oxide generated by heating a liquid phosphoric acid compound into contact with a carbon material, and a condensation of the gaseous phosphorus (g) into liquid phosphorus (L), wherein the reduction reaction of the phosphorus oxide and the condensation of the gaseous phosphorus (g) are conducted by a flow reaction with a nonoxidizing gas flow, wherein the reduction reaction of the phosphorus oxide is conducted in a carbon material-packed bed, and the condensation of the gaseous phosphorus (g) is substantially conducted in a condensation accelerator-packed bed which is disposed downstream of the carbon material-packed bed and in contact with the carbon material-packed bed. 2 . The method for producing phosphorus according to claim 1 , wherein the liquid phosphorus (L) is obtained by continuously supplying the liquid phosphoric acid compound. 3 . The method for producing phosphorus according to claim 1 , wherein the liquid phosphoric acid compound is supplied by providing a porous carrier containing the liquid phosphoric acid compound. 4 . The method for producing phosphorus according to claim 1 , wherein the liquid phosphoric acid compound is supplied dropwise. 5 . The method for producing phosphorus according to claim 1 , wherein the liquid phosphoric acid compound is heated to 200 to 1000° C. to generate the phosphorus oxide, and a reduction reaction temperature of the phosphorus oxide is 700 to 1200° C. 6 . The method for producing phosphorus according to claim 1 , wherein a condensation temperature in the condensation accelerator-packed bed is in a temperature range of 44° C. or higher and lower than 280° C. or in a temperature range in which the gaseous phosphorus (g) substantially condenses. 7 . The method for producing phosphorus according to claim 1 , wherein the liquid phosphoric acid compound contains at least one selected from the group consisting of crude phosphoric acid, crude condensed phosphoric acid and crude phosphorous acid. 8 . The method for producing phosphorus according to claim 1 , wherein a heating temperature of the liquid phosphoric acid compound and a reduction reaction temperature of the phosphorus oxide are independently regulated. 9 . The method for producing phosphorus according to claim 1 , wherein the reduction reaction of the phosphorus oxide is conducted in the carbon material-packed bed by regulating at least one of a heating temperature of the liquid phosphoric acid compound and a nonoxidizing gas flow rate based on a total discharged gas flow rate of carbon monoxide gas and hydrogen gas generated through the reduction reaction of the phosphorus oxide. 10 . The method for producing phosphorus according to claim 1 , wherein unreacted phosphorus oxide is recovered in a container holding water disposed downstream of the condensation accelerator-packed bed in the reduction reaction of the phosphorus oxide. 11 . The method for producing phosphorus according to claim 1 , wherein the carbon material is supplied to the carbon material-packed bed depending on an amount of decrease in the carbon material in the carbon material-packed bed due to the reduction reaction of the phosphorus oxide so as to maintain the height of carbon material-packed bed in the range of the height of the carbon material bed at the beginning of the reaction ±10%. 12 . The method for producing phosphorus according to claim 1 , wherein the liquid phosphorus (L) is obtained by discontinuously supplying the liquid phosphoric acid compound.
Beds · CPC title
with stationary packing material in the bed, e.g. bricks, wire rings, baffles · CPC title
Heating or cooling the reactor (for tubular reactors in furnaces B01J8/062) · CPC title
Feeding reactive fluids (for solid material B01J8/0015) · CPC title
Oxides of phosphorus · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.