1947
DOI: 10.1002/jctb.5000661103
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Production of rare earth and thorium compounds from monazite. Part I

Abstract: A process is described for the separation of rare earth clcments in monazite into the following products : (a) cerium group hydroxides containing thorium hydroxide, (b) crude thorium osalate. Quantitative aspects of the various methods used to accomplish the separations have been investigated. The process is suitable for large scale operation.

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Cited by 30 publications
(6 citation statements)
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“…The dissolution of thorium was consistently low in acid bake/leach tests using leach solutions of pH 1 and a liquid to solid ratio of 20:1, even for bake temperatures of 200-300°C where information from the literature predicted high dissolutions of thorium (Eyring, 1964;Pilkington and Wylie, 1947;Takeuchi, 1976). Analysis of the 300°C bake/leach residue by XRF showed that the residue was highly enriched in thorium.…”
Section: Effect Of Leach Aciditymentioning
confidence: 98%
See 1 more Smart Citation
“…The dissolution of thorium was consistently low in acid bake/leach tests using leach solutions of pH 1 and a liquid to solid ratio of 20:1, even for bake temperatures of 200-300°C where information from the literature predicted high dissolutions of thorium (Eyring, 1964;Pilkington and Wylie, 1947;Takeuchi, 1976). Analysis of the 300°C bake/leach residue by XRF showed that the residue was highly enriched in thorium.…”
Section: Effect Of Leach Aciditymentioning
confidence: 98%
“…Sulfuric acid based treatment of monazite has a long history, being first developed in the early-mid 1900's for the recovery of rare earths and thorium from high grade beach sand monazites (Kithil, 1915;Pilkington and Wylie, 1947;Shaw et al, 1954). Early processes involved digestion of monazite in stirred reactors at 200-245°C, using an acid:concentrate weight ratio varying from 1.5:1 to 3:1 (Borrowman and Rosenbaum, 1961;Pilkington and Wylie, 1947;Shaw et al, 1954). Shaw et al (1954) found that a minimum temperature of about 200°C was required for near complete monazite decomposition, while the minimum acid:concentrate ratio required was 1.6:1 for the two samples tested.…”
Section: Accepted Manuscript 1 Introductionmentioning
confidence: 99%
“…Figure 7 Effect of H 2 SO 4 concentration on the solubility of Ce 2 (SO 4 ) 3. Data from Linke and Seidell (1965) For high grade concentrates of both monazite and bastnasite a water to solid ratio of 10:1 has been widely used (see (Pilkington and Wylie, 1947;Shaw, 1959a).…”
Section: Liquid To Solid Ratiomentioning
confidence: 99%
“…Figure 8 shows the effect of temperature on solubility of lanthanum sulfate and thorium sulfate. Because of the inverse relationship of solubility with temperature for the rare earth sulfates, water leaching is generally carried out at ambient or colder temperatures to maximise rare earth solubility (Pilkington and Wylie, 1947). The effect of increasing temperature was investigated by Kul et al (2008) during water leaching of Beylikahır bastnasite preconcentrate.…”
Section: Temperaturementioning
confidence: 99%
“…Recovery of Rare Earths. After extraction of thorium and uranium, rare earths are readily recovered from the liquor by salting out the sodium double sulfate with sodium chloride or sodium sulfate (73,19). The precipitate settles and filters extremely rapidly.…”
Section: Recovery From Monazitementioning
confidence: 99%