会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 11. 发明申请
    • Method for Producing Polyoxymethylene Dimethyl Ethers From Methanol and Formaldehyde
    • US20080207954A1
    • 2008-08-28
    • US11917528
    • 2006-06-12
    • Eckhard StroeferHans HasseSergej Blagov
    • Eckhard StroeferHans HasseSergej Blagov
    • C07C41/09
    • C07C41/48C07C41/56C07C41/58C08G2/08C07C43/30
    • A process for preparing tri- and tetraoxymethylene glycol dimethyl ether (POMDMEn=3,4) by reacting formaldehyde with methanol and subsequently working up the reaction mixture by distillation, comprising the steps of: a) feeding aqueous formaldehyde solution and methanol into a reactor and reacting; b) feeding the reaction mixture a into a reactive evaporator and separating into a low boiler fraction b1 comprising formaldehyde, water, methanol, methylene glycol, polyoxymethylene glycols, hemiformals, methylal and polyoxymethylene glycol dimethyl ethers (POMDMEn>1), and a high boiler fraction b2, and recycling the high boiler fraction b2 into the reactor (step a)); c) feeding the low boiler fraction b1 into a first distillation column and separating into a low boiler fraction c1 comprising formaldehyde, water, methylene glycol, methanol, hemiformals, methylal, di-, tri- and tetraoxymethylene glycol dimethyl ether (POMDMEn=2,3,4), and a high boiler fraction c2, and recycling the high boiler fraction c2 into the reactive evaporator (step b)); d) feeding the low boiler fraction c1 into a second distillation column and separating into a low boiler fraction d1 and a high boiler fraction d2 consisting of formaldehyde, water, methylene glycol, polyoxymethylene glycols, tri- and tetraoxymethylene glycol dimethyl ether (POMDMEn=3,4); e) feeding the high boiler fraction d2 into a phase separation apparatus and separating into an aqueous phase e1 consisting of formaldehyde, water, methylene glycol and polyoxymethylene glycols, and an organic phase e2 comprising tri- and tetraoxymethylene glycol dimethyl ether (POMDMEn=3,4); f) feeding the organic phase e2 into a third distillation column and separating into a low boiler fraction f1 consisting of formaldehyde, water, methylene glycol and polyoxymethylene glycols, and a high boiler fraction f2 consisting of tri- and tetraoxymethylene glycol dimethyl ether (POMDMEn=3,4).
    • 13. 发明授权
    • Production of high-concentration formaldehyde solutions
    • 生产高浓度甲醛溶液
    • US07345207B2
    • 2008-03-18
    • US10547732
    • 2004-03-04
    • Eckhard StroeferNeven LangHans HasseThomas GrütznerMichael Ott
    • Eckhard StroeferNeven LangHans HasseThomas GrütznerMichael Ott
    • G07C45/78C08G8/04
    • C07C45/002C07C45/82C07C47/04
    • Process for preparing high-concentration formaldehyde solutions having a CH2O content of ≧50% by weight from an aqueous formaldehyde solution having a lower CH2O content by evaporation of part of this solution (partial evaporation), in which the aqueous formaldehyde solution is heated to an evaporation temperature T at which the gas phase becomes enriched in water relative to the liquid phase and the gas phase formed is taken off continuously or discontinuously, wherein the evaporation temperature T obeys the relationship: T[° C.]
    • 通过蒸发具有较低CH 2 O 2含量的甲醛水溶液制备CH 2 O 2含量> 50重量%的高浓度甲醛溶液的方法 该部分溶液(部分蒸发),其中甲醛水溶液被加热到气相相对于液相富集水的蒸发温度T,形成的气相连续或不连续地取出,其中 蒸发温度T遵循以下关系:<?in-line-formula description =“In-line Formulas”end =“lead”?> T [°C。] <°C] <?in-line-formula description =“In-line Formulas”end =“tail”?> <?in-line-formula description =“In-line Formulas”end =“lead”?>其中T < (c)= A + Bx(c / 100)+ Cx(c / 100)2 + Dx(c / 100)3 < line-formula description =“In-line Formulas”end =“tail”?> A = + 68.759,B = + 124.77,C = -12.851,D = -10.095,其中c是瞬时CH 2, / 在蒸发期间甲醛水溶液的重量百分比为20〜99重量%。
    • 15. 发明申请
    • METHOD FOR PRODUCING TRIOXANE FROM TRIOXYMETHYLENE GLYCOL DIMETHYL ETHER
    • 从三甲基乙二醇二甲基醚生产三氧化硅的方法
    • US20100130756A1
    • 2010-05-27
    • US12593964
    • 2008-03-27
    • Eckhard StroeferNeven LangMarkus SiegertHans Hasse
    • Eckhard StroeferNeven LangMarkus SiegertHans Hasse
    • C07D323/06
    • C07D323/06
    • A process for preparing trioxane from trioxymethylene glycol dimethyl ether (POMDMEn=3) by converting trioxymethylene glycol dimethyl ether in the presence of an acidic catalyst and subsequent distillative workup of the reaction mixture, comprising the steps of: a) feeding trioxymethylene glycol dimethyl ether (POMDMEn=3) or a mixture comprising trioxymethylene glycol dimethyl ether into a reactor and converting it in the presence of an acidic catalyst to a mixture a comprising trioxane, formaldehyde, water, methylene glycol (MG), polyoxymethylene glycols (MGn>1), methanol, hemiformals (HF), methylal (POMDMEn=1) and polyoxymethylene glycol dimethyl ethers (POMDMEn>1); b) distillatively separating the reaction mixture a into a low boiler fraction b1 comprising trioxane, formaldehyde, water, methylene glycol, methanol, hemiformal (HFn=1), methylal and dioxymethylene glycol dimethyl ether (POMDMEn=2), and a high boiler fraction b2 comprising polyoxymethylene glycols (MGn>1), hemiformals (HFn>1) and polyoxymethylene glycol dimethyl ethers (POMDMEn>2); c) distillatively separating the low boiler fraction b1 into a low boiler fraction c1 comprising formaldehyde, water, methylene glycol, methanol, hemiformal (HFn=1), methylal and dioxymethylene glycol dimethyl ether (POMDMEn=2), and a high boiler fraction c2 comprising trioxane.
    • 一种通过在酸性催化剂存在下转化三甘醇二甲醚和随后的反应混合物的蒸馏后处理由三甘醇二甲醚(POMDMEn = 3)制备三恶烷的方法,包括以下步骤:a)将三亚甲基二醇二甲醚 POMDMEn = 3)或包含三亚甲基二醇二甲醚的混合物加入到反应器中并在酸性催化剂存在下将其转化为包含三恶烷,甲醛,水,亚甲基二醇(MG),聚氧化亚甲基二醇(MGn1), 甲醇,半缩甲醛(HF),甲缩醛(POMDMEn = 1)和聚氧化亚甲基二醇二甲醚(POMDMEn> 1); b)将反应混合物a蒸馏分离成包含三恶烷,甲醛,水,亚甲基二醇,甲醇,半缩甲醛(HFn = 1),甲缩醛和二甲亚甲基二醇二甲醚(POMDMEn = 2)的低沸点馏分b1和高沸点馏分 b2包含聚甲醛二醇(MGn> 1),半缩甲醛(HFn1)和聚甲醛二醇二甲醚(POMDMEn> 2); c)将低沸点馏分b1蒸馏分离成包含甲醛,水,亚甲基二醇,甲醇,半缩甲醛(HFn = 1),甲缩醛和二羟甲基二醇二甲醚(POMDMEn = 2)的低沸点馏分c1,以及高锅炉馏分c2 包括三恶烷。
    • 16. 发明申请
    • Method for separating trioxane from a trioxane/formaldehyde/water mixture by means of pressure change rectification
    • US20070272540A1
    • 2007-11-29
    • US10583698
    • 2004-12-21
    • Markus SiegertNeven LangEckhard StroeferAchim StammerThorsten FrieseHans Hasse
    • Markus SiegertNeven LangEckhard StroeferAchim StammerThorsten FrieseHans Hasse
    • B01D3/00C07D323/06
    • C07D323/06
    • 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) mixing the use stream I with a recycle stream VII which comprises trioxane as the main component and formaldehyde and water as the secondary components to obtain a feed stream Ia which comprises formaldehyde as the main component and trioxane and water as the secondary components, c) distilling the use stream Ia in a first distillation stage 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, d) 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 a stream V which comprises trioxane as the main component and water and formaldehyde as the secondary components, e) optionally mixing the stream V with a stream IX which comprises water as the main component to obtain a stream Va having a higher water content than the stream V, the stream Va comprising trioxane as the main component and water and formaldehyde as the secondary components, f) distilling the stream V or Va in a third distillation stage at a pressure of from 1 to 10 bar to obtain a stream VI which consists substantially of water and the recycle stream VII which comprises trioxane as the main component and water and formaldehyde as the secondary components
    • 17. 发明申请
    • METHOD FOR PRODUCING CYCLIC FORMALDEHYDE DERIVATIVES FROM POLYOXY DIALKYL ETHERS
    • 从多羟基二烷基醚生产环状甲醛衍生物的方法
    • US20100145079A1
    • 2010-06-10
    • US12532430
    • 2008-03-27
    • Eckhard StroeferNeven LangMarkus SiegertHans Hasse
    • Eckhard StroeferNeven LangMarkus SiegertHans Hasse
    • C07D323/06
    • C07D323/06
    • A process for preparing trioxane from trioxymethylene glycol dimethyl ether (POMDMEn=3) by converting trioxymethylene glycol dimethyl ether in the presence of an acidic catalyst and subsequent distillative workup of the reaction mixture, comprising the steps of: a) feeding trioxymethylene glycol dimethyl ether (POMDMEn=3) or a mixture comprising trioxymethylene glycol dimethyl ether into a reactor and converting it in the presence of an acidic catalyst to a mixture a comprising trioxane, formaldehyde, water, methylene glycol (MG), polyoxymethylene glycols (MGn>1), methanol, hemiformals (HF), methylal (POMDMEn=1) and polyoxymethylene glycol dimethyl ethers (POMDMEn>1); b) distillatively separating the reaction mixture a into a low boiler fraction b1 comprising formaldehyde, water, methylene glycol, methanol, hemiformal (HFn=1), methylal and dioxymethylene glycol dimethyl ether (POMDMEn=2), and a high boiler fraction b2 comprising trioxane, polyoxymethylene glycols (MGn>1), hemiformals (HFn>1) and polyoxymethylene glycol dimethyl ethers (POMDMEn>2); c) distillatively separating the high boiler fraction b2 into a low boiler fraction c1 comprising trioxane, and a high boiler fraction c2 comprising polyoxymethylene glycols (MGn>1), hemiformals (HFn>1) and polyoxymethylene glycol dimethyl ethers (POMDMEn>2).
    • 一种通过在酸性催化剂存在下转化三甘醇二甲醚和随后的反应混合物的蒸馏后处理由三甘醇二甲醚(POMDMEn = 3)制备三恶烷的方法,包括以下步骤:a)将三亚甲基二醇二甲醚 POMDMEn = 3)或包含三亚甲基二醇二甲醚的混合物加入到反应器中并在酸性催化剂存在下将其转化为包含三恶烷,甲醛,水,亚甲基二醇(MG),聚氧化亚甲基二醇(MGn1), 甲醇,半缩甲醛(HF),甲缩醛(POMDMEn = 1)和聚氧化亚甲基二醇二甲醚(POMDMEn> 1); b)将反应混合物a蒸馏分离成包含甲醛,水,亚甲基二醇,甲醇,半缩甲醛(HFn = 1),甲缩醛和二甲亚甲基二醇二甲醚(POMDMEn = 2)的低沸点馏分b1,以及高沸点馏分b2, 三氧杂环己烷,聚甲醛(MGn> 1),半缩甲醛(HFn1)和聚甲醛二醇二甲醚(POMDMEn> 2); c)将高沸点馏分b2蒸馏成包含三恶烷的低沸点馏分c1和包含聚甲醛二醇(MGn> 1),半缩甲醛(HFn1)和聚甲醛二醇二甲醚(POMDMEn2)的高沸点馏分c2。