发明公开
EP1299359A1 CHEMICAL PROCESS FOR THE EXTRACTION OF 2-HYDROXY PYRIDINE DERIVATIVES, 2-HYDROXYQUINOLINE, AND 2-HYDROXYBENZOTHIAZOLE
有权
2-羟基吡啶衍生物,2-羟基喹啉和2-羟基苯并噻唑CHEMICAL提取工艺
- 专利标题: CHEMICAL PROCESS FOR THE EXTRACTION OF 2-HYDROXY PYRIDINE DERIVATIVES, 2-HYDROXYQUINOLINE, AND 2-HYDROXYBENZOTHIAZOLE
- 专利标题(中): 2-羟基吡啶衍生物,2-羟基喹啉和2-羟基苯并噻唑CHEMICAL提取工艺
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申请号: EP01938443.7申请日: 2001-06-14
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公开(公告)号: EP1299359A1公开(公告)日: 2003-04-09
- 发明人: JONES, Raymond Vincent Heavon , STEWART, Alastair Iain Currie , WHITTON, Alan John , WHITE, Jennifer Ann , FORRESTER, Julie , MURRAY, Joanne Emma , HAMILTON, Susan Thomson
- 申请人: Syngenta Limited
- 申请人地址: European Regional CentrePriestley RoadSurrey Research Park GuildfordSurrey GU2 7YH GB
- 专利权人: Syngenta Limited
- 当前专利权人: Syngenta Limited
- 当前专利权人地址: European Regional CentrePriestley RoadSurrey Research Park GuildfordSurrey GU2 7YH GB
- 代理机构: Houghton, Malcolm John
- 优先权: GB0016338 20000703
- 国际公布: WO02002528 20020110
- 主分类号: C07D213/64
- IPC分类号: C07D213/64 ; C07D215/22 ; C07D277/68
摘要:
A process for extracting from aqueous solution the alkali metal or calcium salt of a halo or haloalkyl substituted 2-hydroxypyridine, or a 2-hydroxyquinoline or 2-hydroxybenzothiazole which comprises contacting an aqueous alkaline or neutral solution of the alkali metal or calcium salt, in which is dissolved an alkali metal fluoride, chloride, bromide, hydroxide, sulphate, sulphite, cyanate, cyanide, thiocyanate, thiosulphate, sulphide, phosphate, hydrogen phosphate, carbonate, bicarbonate, borate, chlorate, hypochlorite, perchlorate, nitrite, chromate, dichromate or permanganate or calcium chloride, bromide, nitrate, nitrite, chlorate, hypochlorite, perchlorate, thiocyanate, thiosulphate, chromate, dichtromate or permanganate, with a partially water-miscible organic solvent so as to transfer aqueous solution of the alkali metal or calcium salt of the 2-hydroxypyridine, 2-hydroxyquinoline or 2-hydroxybenzothiazole into the solvent whilst retaining separate aqueous and solvent phases, and thereafter separating the solvent phase containing the alkali metal or calcium salt and water from the aqueous phase, the ratio of solvent to water in the separated solvent phase being from 0.5:1 to 10:1 w/w.
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