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    • 2. 发明申请
    • BATCH PROCESS FOR PREPARING POLYAMIDES
    • 批量制备聚氨酯的方法
    • US20110144300A1
    • 2011-06-16
    • US13058779
    • 2009-08-14
    • Philippe DesboisFaissal-Ali El-ToufailiMichael GallAndreas Wollny
    • Philippe DesboisFaissal-Ali El-ToufailiMichael GallAndreas Wollny
    • C08G69/28
    • C08G69/28B29C47/0014B29C47/0021B29C47/762C08G69/26C08G69/265C08G69/30C08G69/36C08G69/46
    • Polyamides based on dicarboxylic acids and on diamines are produced in a batch process by 1) feeding the entire amount of monomer composed of dicarboxylic acids, of diamines, and, if appropriate, of further polyamide-forming monomers, in the desired stoichiometry, in a closed stirred-tank reactor, 2) heating the monomer mixture in the stirred-tank reactor, with stirring, and with setting of a certain pressure, to a desired reaction temperature for the production of a prepolymer, 3) if appropriate, completely or partially depressurizing the reaction mixture from stage 2), 4) if appropriate, carrying out further thermal treatment of the reaction mixture from stage 2) or 3), and 5) reacting the reaction mixture from stage 2), 3), or 4) in the melt in a vented extruder for further increase of the molecular weight, with discharge of water vapor, and without use of additional polyamide-forming monomers or of polyamides.
    • 以分批方法制备基于二羧酸和二胺的聚酰胺,其通过以下方式制备:以所需的化学计量,在所需的化学计量中,将全部量的由二羧酸,二胺组成的单体,以及如果合适的话,将其加入到另外的聚酰胺形成单体中 2)在搅拌下将搅拌釜中的单体混合物加热至设定一定压力至预期的反应温度,3)如果合适的话,完全或部分地 使反应混合物从阶段2)减压),4)如果合适,进行反应混合物从阶段2)或3)的进一步热处理,和5)使反应混合物从步骤2),3)或4)在 在排气挤出机中的熔体进一步增加分子量,排出水蒸气,并且不使用额外的聚酰胺形成单体或聚酰胺。
    • 4. 发明授权
    • Copolyamides
    • 共聚酰胺
    • US08658724B2
    • 2014-02-25
    • US13378980
    • 2010-06-15
    • Christian SchmidtFaissal-Ali El-ToufailiPhilippe DesboisRaquel Fernandez Rodiles
    • Christian SchmidtFaissal-Ali El-ToufailiPhilippe DesboisRaquel Fernandez Rodiles
    • C08K5/05
    • C08G69/265C08G69/14C08G69/36C08L77/02C08L77/06C09D177/02C09D177/06
    • What are described are a solution comprising a terpolymer formed from the monomers of components A, B and C, the total amount of which adds up to 100% by weight, a) 5 to 60% by weight of lactams as component A, b) 5 to 60% by weight of equimolar amounts of adipic acid and one or more aliphatic diamines as component B, c) 10 to 70% by weight of equimolar amounts of adipic acid and 4,4′-diaminodicyclohexylmethane (dicycan) as component C, in an aromatics-free solvent system comprising 50 to 100% by weight of C1-4-alkanol, 0 to 50% by weight of water and not more than 10% by weight of further aromatics-free solvents, where the total amount of the solvent system adds up to 100% by weight, and a terpolymer formed from the monomers of components A, B and C, the total amount of which adds up to 100% by weight, a) 15 to 40% by weight of lactams as component A, b) 20 to 45% by weight of equimolar amounts of adipic acid and one or more aliphatic diamines as component B, c) 25 to 60% by weight of equimolar amounts of adipic acid and 4,4′-diaminodicyclohexylmethane (dicycan) as component C, excluding terpolymers formed from 30 to 40% by weight of component A, 30 to 40% by weight of component B and 30 to 40% by weight of component C.
    • 描述的是包含由组分A,B和C的单体形成的三元共聚物的溶液,其总量加至100重量%,a)5至60重量%的作为组分A的内酰胺,b) 5至60重量%的等摩尔量的己二酸和一种或多种脂族二胺作为组分B,c)10至70重量%的等摩尔量的己二酸和作为组分C的4,4'-二氨基二环己基甲烷(二环己烷) 在不含芳族化合物的溶剂体系中,其包含50至100重量%的C 1-4链烷醇,0至50重量%的水和不超过10重量%的其它不含芳族化合物的溶剂,其中 溶剂系统加入到100重量%,和由组分A,B和C的单体形成的三元共聚物,其总量加至100重量%,a)15至40重量%的作为组分的内酰胺 A,b)20〜45重量%的等摩尔量的己二酸和一种或多种脂族二胺作为组分B,c)25〜60重量% 等摩尔量的己二酸和作为组分C的4,4'-二氨基二环己基甲烷(二环己烷),不包括由30至40重量%的组分A,30至40重量%的组分B和30至40重量%的组分B形成的三元共聚物, 组分C.
    • 7. 发明申请
    • PROCESS FOR PREPARING POLYAMIDES
    • 制备聚氨酯的方法
    • US20120245308A1
    • 2012-09-27
    • US13514364
    • 2010-12-03
    • Faissal-Ali El-ToufailiPhilippe DesboisAndreas WollnySven LawrenzChristian Schmidt
    • Faissal-Ali El-ToufailiPhilippe DesboisAndreas WollnySven LawrenzChristian Schmidt
    • C08G69/28C08G69/26
    • C08G69/265C08G69/28
    • The present invention relates to a process for preparing a polyamide based on dicarboxylic acids and diamines, comprising the following stages: A) providing an aqueous monomer mixture composed of dicarboxylic acids and diamines, where the molar ratio of dicarboxylic acids to diamines is adjusted such that, at the outlet of stage C), there is a molar deficiency of dicarboxylic acids or diamines of 1 to 10 mol%, based on the respective other component, B) transferring the aqueous mixture from stage A) into a continuous evaporator reactor in which diamines and dicarboxylic acids are converted at a temperature in the range from 100 to 370° C. and a pressure in the range from 1 to 50 bar, C) transferring the mixture from stage B) into a separator which is operated at a temperature in the range from 100 to 370° C. and a pressure in the range from 1 to 50 bar with removal of gaseous components, D) transferring the mixture from stage C) together with diamine or dicarboxylic acid in an amount suitable for compensation for the molar deficiency into a tubular reactor which is operated at a temperature in the range from 100 to 370° C. and a pressure in the range from 1 to 50 bar, for a residence time in the range from 10 seconds to 30 minutes, E) transferring the mixture from stage D) into an extruder which is operated at a temperature in the range from 150 to 400° C. for a residence time in the range from 10 seconds to 30 minutes with removal of gaseous components through venting orifices.
    • 本发明涉及一种制备基于二羧酸和二胺的聚酰胺的方法,包括以下步骤:A)提供由二羧酸和二胺组成的含水单体混合物,其中二羧酸与二胺的摩尔比被调整为使得 ,在阶段C)的出口处,基于各自的其它组分,存在摩尔不足的二羧酸或二胺的1至10摩尔%,B)将水性混合物从阶段A)转移到连续的蒸发器反应器中,其中 二胺和二羧酸在100至370℃的温度和1至50巴的压力范围内转化,C)将混合物从阶段B)转移到分离器中,该分离器在 范围为100至370℃,压力为1至50巴,除去气态组分,D)将混合物与阶段C)一起转移至二胺或二羧酸的量 适合于将摩尔不足补偿到在100至370℃的温度和1至50巴的压力范围内操作的管式反应器中,停留时间在10秒至 30分钟,E)将混合物从阶段D)转移到挤出机中,该挤出机在150-400℃的温度下操作,停留时间在10秒至30分钟之间,同时除去气体成分 通风孔。
    • 10. 发明申请
    • COPOLYAMIDES
    • 共聚酰胺
    • US20120157594A1
    • 2012-06-21
    • US13378980
    • 2010-06-15
    • Christian SchmidtFaissal-Ali El-ToufailiPhilippe DesboisRacquel Fernandez Rodiles
    • Christian SchmidtFaissal-Ali El-ToufailiPhilippe DesboisRacquel Fernandez Rodiles
    • C08K5/05
    • C08G69/265C08G69/14C08G69/36C08L77/02C08L77/06C09D177/02C09D177/06
    • What are described are a solution comprising a terpolymer formed from the monomers of components A, B and C, the total amount of which adds up to 100% by weight,a) 5 to 60% by weight of lactams as component A,b) 5 to 60% by weight of equimolar amounts of adipic acid and one or more aliphatic diamines as component B,c) 10 to 70% by weight of equimolar amounts of adipic acid and 4,4′-diaminodicyclohexylmethane (dicycan) as component C,in an aromatics-free solvent system comprising50 to 100% by weight of C1-4-alkanol,0 to 50% by weight of water andnot more than 10% by weight of further aromatics-free solvents,where the total amount of the solvent system adds up to 100% by weight, and a terpolymer formed from the monomers of components A, B and C, the total amount of which adds up to 100% by weight,a) 15 to 40% by weight of lactams as component A,b) 20 to 45% by weight of equimolar amounts of adipic acid and one or more aliphatic diamines as component B,c) 25 to 60% by weight of equimolar amounts of adipic acid and 4,4′-diaminodicyclohexylmethane (dicycan) as component C,excluding terpolymers formed from 30 to 40% by weight of component A, 30 to 40% by weight of component B and 30 to 40% by weight of component C.
    • 描述的是包含由组分A,B和C的单体形成的三元共聚物的溶液,其总量加至100重量%,a)5至60重量%的作为组分A的内酰胺,b) 5至60重量%的等摩尔量的己二酸和一种或多种脂族二胺作为组分B,c)10至70重量%的等摩尔量的己二酸和作为组分C的4,4'-二氨基二环己基甲烷(二环己烷) 在不含芳族化合物的溶剂体系中,其包含50至100重量%的C 1-4链烷醇,0至50重量%的水和不超过10重量%的其它不含芳族化合物的溶剂,其中 溶剂系统加入到100重量%,和由组分A,B和C的单体形成的三元共聚物,其总量加至100重量%,a)15至40重量%的作为组分的内酰胺 A,b)20〜45重量%的等摩尔量的己二酸和一种或多种作为组分B的脂族二胺,c)25至60重量% 的等摩尔量的己二酸和4,4'-二氨基二环己基甲烷(二环己烷)作为组分C,不包括由30至40重量%的组分A形成的三元共聚物,30至40重量%的组分B和30至40重量% 的组分C.