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    • 1. 发明授权
    • Reaction of a solution comprising a mixture
    • 包含混合物的溶液的反应
    • US06610888B1
    • 2003-08-26
    • US09583290
    • 2000-05-31
    • Eckhard StröferStephan SchollHans Hasse
    • Eckhard StröferStephan SchollHans Hasse
    • C07C21100
    • C07C45/82C07B63/00C07C29/80C07C47/04C07C31/22C07C31/20
    • A method of reacting a solution comprising a mixture of chemical compounds which are in chemical equilibrium with one another with at least one further chemical compound (9) is provided. The method comprises the following steps: fractionation of the solution by means of a separation method to give at least two fractions (5, 6) which are enriched in different chemical compounds of the mixture; and reaction of a fraction (5) with the further chemical compound or compounds (9). The fractionation is advantageously carried out using a film evaporator (1). Unreacted fractions (6) can be recirculated via a residence time vessel (3) back to the fractionation step. The method is particularly suitable for reactions of an aqueous formaldehyde solution in which various components of the solution (formaldehyde, methylene glycol, polyoxymethylene glycols) react in different ways.
    • 提供了使包含与化学平衡化学平衡的化合物的混合物的溶液与至少一种其它化合物(9)反应的方法。 该方法包括以下步骤:通过分离方法对溶液进行分级,得到富含混合物不同化合物的至少两个级分(5,6); 以及级分(5)与其它化合物或化合物(9)的反应。 有利的是使用薄膜蒸发器(1)进行分馏。 未反应的馏分(6)可以通过停留时间容器(3)再循环回分馏步骤。 该方法特别适合甲醛水溶液的反应,其中溶液的各种组分(甲醛,亚甲基二醇,聚氧化亚甲基二醇)以不同的方式反应。
    • 3. 发明授权
    • Method for separating trioxane from a trioxane/formaldehyde/water mixture by means of pressure change rectification
    • 通过压力变换精馏从三恶烷/甲醛/水混合物中分离三恶烷的方法
    • US07713387B2
    • 2010-05-11
    • US10583698
    • 2004-12-21
    • Markus SiegertNeven LangEckhard StröferAchim StammerThorsten FrieseHans Hasse
    • Markus SiegertNeven LangEckhard StröferAchim StammerThorsten FrieseHans Hasse
    • B01D3/00C07D323/06C07C45/78
    • C07D323/06
    • A process for removing trioxane from a use stream I of formaldehyde, trioxane and water, by a) providing a use stream I of formaldehyde as the main component and trioxane and water as the secondary components, b) mixing the use stream I with a recycle stream VII to obtain a feed stream Ia, c) distilling the use stream Ia in a first distillation stage to obtain a stream II of formaldehyde as the main component and water as the secondary component, and a stream III of trioxane as the main component and water and formaldehyde as the secondary components, d) distilling the stream III in a second distillation stage having a pressure higher than in the first distillation stage, to obtain a stream IV of trioxane and a stream V of trioxane as the main component and water and formaldehyde as the secondary components, e) distilling the stream V in a third distillation stage to obtain a stream VI of water and the recycle stream VII of trioxane as the main component and water and formaldehyde as the secondary components.
    • 一种从甲醛,三恶烷和水的使用流I中除去三恶烷的方法,通过以下步骤:a)提供以甲醛为主要成分的使用流I和作为第二组分的三恶烷和水,b)将使用流I与再循环 流VII以获得进料流Ia,c)在第一蒸馏阶段中蒸馏出使用流Ia以获得作为主要组分的甲醛的流II和作为第二组分的水,以及作为主要组分的三恶烷的流III和 水和甲醛作为次要组分,d)在具有高于第一蒸馏阶段的压力的第二蒸馏阶段中蒸馏料流III,得到三恶烷的流IV和三恶烷的流V作为主要成分, 甲醛作为次要组分,e)在第三蒸馏阶段中蒸馏物流V以获得水的流VI和三恶烷的再循环流VII作为主要成分,水和甲醛为t 他的次要成分。
    • 5. 发明授权
    • Method for producing polyoxymethylene dimethyl ethers from methanol and formaldehyde
    • 从甲醇和甲醛生产聚甲醛二甲醚的方法
    • US07671240B2
    • 2010-03-02
    • US11917528
    • 2006-06-12
    • Eckhard StroeferHans HasseSergej Blagov
    • Eckhard StroeferHans HasseSergej Blagov
    • C07C41/56C08G2/08
    • C07C41/48C07C41/56C07C41/58C08G2/08C07C43/30
    • Processes for preparing tri- and tetraoxymethylene glycol dimethyl ether (POMDMEn=3,4) include feeding a reaction mixture of an aqueous formaldehyde solution and methanol into a reactive evaporator and separating into a first low boiler fraction and a first high boiler fraction, recycling the first high boiler fraction into the reactor, feeding the first low boiler fraction into a first distillation column and separating into a second low boiler fraction and a second high boiler fraction, recycling the second high boiler fraction into the reactive evaporator, feeding the second low boiler fraction into a second distillation column and separating into a third low boiler fraction and a third high boiler fraction, feeding the third high boiler fraction into a phase separation apparatus and separating into an aqueous phase and an organic phase, and feeding the organic phase into a third distillation column and separating into a low and high boiler fractions.
    • 制备三 - 和四甲基二醇二甲醚(POMDMEn = 3,4)的方法包括将甲醛水溶液和甲醇的反应混合物进料到反应蒸发器中,并分离成第一低沸点馏分和第一高沸点馏分,循环利用 将第一高锅炉馏分进入反应器,将第一低沸点馏分进料到第一蒸馏塔中并分离成第二低沸点馏分和第二高沸点馏分,将第二高沸点馏分再循环到反应蒸发器中,将第二低沸点馏分 将馏分分馏成第二蒸馏塔并分离成第三低沸点馏分和第三高沸点馏分,将第三高沸点馏分进料到相分离装置中并分离成水相和有机相,并将有机相进料至 第三蒸馏塔并分离成低和高沸点馏分。
    • 7. 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。
    • 9. 发明申请
    • Method for separating trioxane from a mixture containing trioxane, formaldehyde and water
    • 从含有三恶烷,甲醛和水的混合物中分离三恶烷的方法
    • US20070155972A1
    • 2007-07-05
    • US10583696
    • 2004-12-21
    • Neven LangEckhard StroeferAchim StammerThorsten FrieseMarkus SiegertMichael OttHans HasseThomas GrutznerSergej Blagov
    • Neven LangEckhard StroeferAchim StammerThorsten FrieseMarkus SiegertMichael OttHans HasseThomas GrutznerSergej Blagov
    • C07D305/12C07C41/03
    • C07D323/06B01D3/146B01D3/36Y02P20/127
    • A process for removing trioxane from a mixture I of formaldehyde, trioxane and water, by a) distilling the mixture I in a first distillation stage at a pressure of from 0.1 to 2 bar to obtain a stream II which comprises formaldehyde and a stream III which comprises predominantly trioxane and additionally water and formaldehyde, b) mixing the stream III with a recycle stream VII which comprises predominantly trioxane and additionally water and formaldehyde to obtain a stream IIIa which comprises predominantly trioxane and additionally water and formaldehyde, c) distilling the stream IIIa, if appropriate after removing low boilers from the stream III or IIIa in a further distillation stage, in a second distillation stage at a pressure of from 0.2 to 10 bar, the pressure in the second distillation stage being at least 0.1 bar higher than the pressure in the first distillation stage, to obtain a stream IV of trioxane and a stream V which comprises predominantly trioxane and additionally water and formaldehyde, d) distilling the stream V in a third distillation stage at a pressure of from 0.1 to 4 bar to obtain a stream VI which comprises predominantly water and additionally formaldehyde, and the recycle stream VII which comprises predominantly trioxane and additionally water and formaldehyde, e) if appropriate, distilling the stream VI in a fourth distillation stage to obtain a stream VIII which comprises predominantly water, and a stream IX which comprises predominantly formaldehyde.
    • 一种从甲醛,三恶烷和水的混合物I中除去三恶烷的方法,通过以下步骤a)在0.1至2巴的压力下在第一蒸馏阶段中蒸馏混合物I以获得包含甲醛和流III的流II 主要包含三恶烷,另外还含有水和甲醛,b)将流III与主要包含三恶烷,另外含有水和甲醛的再循环流VII混合,得到主要含有三恶烷,另外含有水和甲醛的流IIIa,c)蒸馏流IIIa 如果适当,则在进一步蒸馏阶段从流III或IIIa除去低锅炉后,在0.2至10巴的压力的第二蒸馏阶段中,第二蒸馏阶段中的压力比压力高至少0.1巴 在第一蒸馏阶段,获得三恶烷的流IV和主要包含三恶烷并另外包含的流V 和d)在0.1至4巴的压力下在第三蒸馏阶段中蒸馏物流V以获得主要包含水和另外甲醛的物流VI,以及主要包含三恶烷和另外的水的再循环流VII,以及 甲醛,e)如果合适,在第四蒸馏阶段中蒸馏物流VI以获得主要包含水的物流VIII和主要包含甲醛的物流IX。