发明申请
US20100121081A1 METHOD FOR SEPARATING TRIOXANE FROM A TRIOXANE/FORMALDEHYDE/WATER MIXTURE BY MEANS OF PRESSURE CHANGE RECTIFICATION
失效
通过压力变化方法从三氧化硅/甲醛/水混合物中分离三氧化二锑的方法
- 专利标题: METHOD FOR SEPARATING TRIOXANE FROM A TRIOXANE/FORMALDEHYDE/WATER MIXTURE BY MEANS OF PRESSURE CHANGE RECTIFICATION
- 专利标题(中): 通过压力变化方法从三氧化硅/甲醛/水混合物中分离三氧化二锑的方法
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申请号: US12523741申请日: 2008-01-23
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公开(公告)号: US20100121081A1公开(公告)日: 2010-05-13
- 发明人: Neven Lang , Joachim Thiel , Eckhard Stroefer , Julia Kirschbaum , Markus Siegert
- 申请人: Neven Lang , Joachim Thiel , Eckhard Stroefer , Julia Kirschbaum , Markus Siegert
- 申请人地址: DE Ludwigshafen
- 专利权人: BASF SE
- 当前专利权人: BASF SE
- 当前专利权人地址: DE Ludwigshafen
- 优先权: EP07101198.5 20070125
- 国际申请: PCT/EP08/50745 WO 20080123
- 主分类号: C07D323/06
- IPC分类号: C07D323/06
摘要:
A process for removing trioxane from a use stream I of formaldehyde, trioxane and water, by a) providing a use stream I which comprises formaldehyde as the main component and trioxane and water as the secondary components, b) feeding the use stream I, a recycle stream V and a recycle stream VII which comprises formaldehyde as the main component and water and trioxane as the secondary components into a first distillation stage and distilling at a pressure of from 0.1 to 2.5 bar to obtain a stream II which comprises formaldehyde as the main component and water as the secondary component, and a stream III which comprises trioxane as the main component and water and formaldehyde as the secondary components, and a stream X which comprises water, trioxane and formaldehyde, c) distilling the stream III, optionally after removing low boilers from the stream III in a low boiler removal stage, in a second distillation stage at a pressure of from 0.2 to 17.5 bar, the pressure in the second distillation stage being from 0.1 to 15 bar higher than the pressure in the first distillation stage, to obtain a stream IV which consists substantially of trioxane and the recycle stream V which comprises trioxane as the main component and water and formaldehyde as the secondary components, d) feeding the stream X and if appropriate a stream IX which comprises water as the main component into a third distillation stage and distilling at a pressure of from 1 to 10 bar to obtain a stream VI which consists substantially of water and a recycle stream VII which comprises formaldehyde as the main component and water and trioxane as the secondary components.
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