참여 물질
| 역할 | 이름 | HCID | 투입량 |
|---|
| 반응물 | Thiocyanic Acid | HCID 781 | — |
| 반응물 | Sulfuric Acid | HCID 1118 | — |
| 반응물 | Hafnium | HCID 23986 | — |
| 반응물 | Ammonium Sulfate | HCID 6097028 | — |
| 반응물 | Hafnium thiocyanate | HCID 14619944 | — |
| 생성물 | Ammonium thiocyanate | HCID 15666 | — |
| 생성물 | Hafnium(4+) tetrahydroxide | HCID 9881356 | — |
반응 단계
This process was allegedly further improved by stripping the loaded solvent with a saturated aqueous solution of ammonium sulfate containing some sulfuric acid, the extract phase containing thiocyanic acid, ammonium sulfate, and the hafnium values in the form of hafnium thiocyanate. Such extract phase is then treated with gaseous ammonia, which reacts with the thiocyanic acid and hafnium thiocyanate to simultaneously form ammonium thiocyanate and hafnium hydroxide. This is said to be of the utmost importance in coprecipitating ammonium sulfate with the hafnium hydroxide to make the hafnium hydroxide easily filterable, see the aforementioned Greenberg et al., U.S. Pat. No. 3,069,232 of Dec. 18, 1962 entitled "Recovery of Hafnium Values." However, not only is the sulfate ion present, but the sulfuric acid introduced into the ammonium sulfate extractant to ensure recovery of the major portion of the thiocyanic acid in the extract phase, contaminates the extract phase and requires additional purification steps.
출처 및 근거
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| 특허 번호 | US04873072 |
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| 출처 데이터셋 | uspto-grants-1989_10 |
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| ORD ID | ord-11d10964131845d5a33f8f27299eca0c |
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| 출처 메모 | uspto-grants-1989_10 |
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