참여 물질
| 역할 | 이름 | HCID | 투입량 |
|---|
| 반응물 | Sulfuric Acid | HCID 1118 | — |
| 반응물 | 9,9-Bis[4-(2-hydroxyethoxy)phenyl]fluorene | HCID 3764404 | — |
| 반응물 | 1-Phenoxyethan-1-ol | HCID 17848643 | — |
| 반응물 | Fluoreneone | HCID 22281833 | — |
| 생성물 | Phenoxyethanol | HCID 31236 | — |
| 생성물 | 9,9-Bis[4-(2-hydroxyethoxy)phenyl]fluorene | HCID 3764404 | — |
| 생성물 | Fluoreneone | HCID 22281833 | — |
반응 단계
Further, the inventors of the present invention disclose, as a method using no sulfuric acid, a method of obtaining 9,9-bis(4-(2-hydroxyethoxy)phenyl)fluorene by reacting fluorenone with phenoxyethanol in the presence of a heteropoly acid serving as a catalyst, which method includes (a) partitioning a target substance into an organic phase by adding an extract agent constituted by water and an organic solvent to a reaction liquid and (b) recovering the target substance (refer to Patent Literature 8). Further, the inventors of the present invention propose: a method for producing 9,9-bis(4-(2-hydroxyethoxy)phenyl)fluorene from fluorenone and 2-phenoxyethanol in the presence of a heteropoly acid catalyst (Patent Literature 9); and a method for producing 9,9-bis(4-(2-hydroxyethoxy)phenyl)fluorene whose melting point is 160° C. to 166° C. (Patent Literature 10). Moreover, there is disclosed a method of obtaining a fluorene derivative by reacting fluorenone with a phenol by using hydrochloric acid and a thiol serving as catalysts, which method includes partitioning a target substance into an organic phase by using an extract agent and recovering the target substance (refer to Patent Literature 11). However, according to these methods, a reaction liquid contains a large amount of unreacted phenol or phenoxyalcohol, which is highly soluble in water. This may cause a reduction in liquid separability, and thus cause a deterioration in hue or purity. Further, these methods place a large burden on the environment, because a large amount of organic compounds such as phenols or phenoxyalcohols are mixed in an aqueous phase, and/or it is necessary to use a large amount of organic solvent for liquid separation. Therefore, these methods are not industrially advantageous.
출처 및 근거
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| 특허 번호 | US08841491B2 |
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| 출처 데이터셋 | uspto-grants-2014_09 |
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| ORD ID | ord-7770224673d74d02952ff7d797f0d730 |
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| 출처 메모 | uspto-grants-2014_09 |
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