发明申请
US20100270140A1 METHOD FOR SEPARATING TIOXANE 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E /甲醛/水混合物中分离三氧化二锑的方法
- 专利标题: METHOD FOR SEPARATING TIOXANE 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E /甲醛/水混合物中分离三氧化二锑的方法
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申请号: US12682294申请日: 2008-09-22
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公开(公告)号: US20100270140A1公开(公告)日: 2010-10-28
- 发明人: Markus Siegert , Neven Lang , Laszlo Szarvas , Christoph Sigwart , Franz Niklaus Windlin , Eckhard Stroefer
- 申请人: Markus Siegert , Neven Lang , Laszlo Szarvas , Christoph Sigwart , Franz Niklaus Windlin , Eckhard Stroefer
- 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: EP07118103.6 20071009
- 国际申请: PCT/EP08/62620 WO 20080922
- 主分类号: B01D3/10
- IPC分类号: B01D3/10 ; B01D3/36
摘要:
A process for separating trioxane from a feed stream I comprising formaldehyde, trioxane and water, in which a) a feed stream I comprising formaldehyde as main component and trioxane and water as secondary components is provided, b) the feed stream I, a recycle stream V and a recycle stream VII comprising formaldehyde as main component and water and trioxane as secondary components are fed into a first distillation stage and distilled at a pressure of from 0.1 to 2.5 bar to give a stream II comprising formaldehyde as main component and water as secondary component and a stream III comprising trioxane as main component and water and formaldehyde as secondary components and a stream X comprising water, trioxane and formaldehyde, c) the stream III is, if appropriate after removal of low boilers from the stream III in a low boiler removal stage, distilled in a second distillation stage at a pressure of from 0.2 to 17.5 bar, with the pressure in the second distillation stage being from 0.1 to 15 bar higher than the pressure in the first distillation stage, to give a stream IV consisting essentially of trioxane and the recycle stream V comprising trioxane as main component and water and formaldehyde as secondary components, c1) the stream IV is purified in at least one further trioxane distillation stage at a pressure at the top of from 0.5 to 2 bar to give purified trioxane as side offtake stream XII in the enrichment section of the column, d) the stream X and, if appropriate, a stream IX comprising water as main component are fed into a third distillation stage and distilled at a pressure of from 1 to 10 bar to give a stream VI consisting essentially of water and a recycle stream VII comprising formaldehyde as main component and water and trioxane as secondary components, is described.
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