David A. Crea - Pocatello ID Jerry A. Keely - Pocatello ID
Assignee:
FMC Corporation - Philadelphia PA
International Classification:
C01B 2501 C01B 2502 C01B 2504
US Classification:
423322
Abstract:
Liquid phosphorus as produced by the reduction of a phosphate ore in an electric arc furnace while of high purity contains color-causing impurities that impart to the phosphorus a black color by reflected light. Such liquid phosphorus is polished or refined to exhibit a yellow or yellow brown cast by mixing it with hot water and subjecting the mixture to intense agitation. The refined phosphorus is separated from the water phase which retains the impurities.
Process For Treatment Of Phossy Water For Recycling
Gordon H. Scherbel - Pocatello ID David A. Crea - Pocatello ID Jerry A. Keely - Pocatello ID Ronald L. Andersen - Pocatello ID Byron L. Nichols - Federal Way WA
Assignee:
FMC Corporation - Philadelphia PA
International Classification:
C01B 2501
US Classification:
423323
Abstract:
In the electric arc furnace production of elemental phosphorus, cold phossy water is segregated from hot phossy water. The cold phossy water is discharged to a lined pond wherein solids settle to form a clarified cold water which is recycled for cooling and washing purposes. The hot phossy water is passed through a lamellar settler wherein phosphorus and solids are separated as a sludge to form a clarified hot water. The clarified hot water, without requiring additional heat, is recycled for process use. Phosphorus is recovered from the sludge to reduce to a minimum the amount of phosphorus discharged with dirt from the hot phossy water to the pond.
David A. Crea - Pocatello ID James A. Robertson - Levittown PA Jerry A. Keely - Pocatello ID
Assignee:
FMC Corporation - Philadelphia PA
International Classification:
B01D 4300
US Classification:
209 2
Abstract:
Process for recovery of elemental phosphorus from phosphorus sludge produced in a phosphorus furnace by treating the sludge in a centrifugal separator and separating a fine dirt slimes fraction from a recovered heavy fraction containing the major portion of phosphorus; treating the slimes fraction in hydrocyclones not over one inch (24. 4 mm) in diameter to separate two streams, a first phosphorus-poor stream containing particles smaller than 8-15 micrometers, and a second phosphorus-rich stream containing particles larger than 8-15 micrometers; recycling the second, phosphorus-rich stream to the centrifugal separator for phosphorus recovery, and discarding the first, phosphorus-poor stream.