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    • 5. 发明申请
    • DIVISION OF A POLYARYLENE ETHER SOLUTION
    • 聚亚烷基醚解决方案
    • US20160208056A1
    • 2016-07-21
    • US14904491
    • 2014-07-16
    • BASF SE
    • Joerg ERBESGerhard LANGETobias KORTEKAMPCecile SCHNEIDER
    • C08J3/14C08G75/23
    • C08J3/14C08G65/46C08G75/23C08J3/12C08J2381/06
    • Process for producing polyarylene ether beads from a polyarylene ether solution, comprising the steps of i) dividing the polyarylene ether solution into droplets, ii) transferring the droplets into a precipitation bath to form polyarylene ether beads in the precipitation bath which (A) comprises at least one aprotic solvent (component (1)) and at least one protic solvent (component (2)), (B) has a temperature of 0° C. to Tc, where the critical temperature Tc in [° C.] can be determined by the numerical equation Tc=(77−c)/0.58 in which c is the concentration of component (1) in the precipitation bath in [% by weight] and (C) has component (1) in concentrations of 5% by weight to cc, where the critical concentration cc in [% by weight] can be determined by the numerical equation cc=77−0.58*T in which T is the temperature in the precipitation bath in [° C.], where the percentages by weight are each based on the sum of the percentages by weight of component (1) and of component (2) in the precipitation bath.
    • 用于从聚亚芳基醚溶液制备聚亚芳基醚珠粒的方法,包括以下步骤:i)将聚亚芳基醚溶液分成液滴,ii)将沉淀液转移到沉淀浴中,以在沉淀槽中形成聚亚芳基醚珠粒,其中(A) 至少一种非质子溶剂(组分(1))和至少一种质子溶剂(组分(2)),(B)具有0℃至Tc的温度,其中[℃]中的临界温度Tc可以 通过数值方程Tc =(77-c)/0.58确定,其中c是沉淀浴中组分(1)的浓度[重量%],(C)中组分(1)的浓度为5% 重量至cc,其中[重量%]的临界浓度cc可以通过数值方程式cc = 77-0.58 * T确定,其中T是沉淀浴中的温度[℃],其中百分比由 重量分别基于组分(1)和组分(2)的重量百分比的总和, 在沉淀浴中。
    • 6. 发明申请
    • DIVISION OF A POLYARYLENE ETHER SOLUTION
    • 聚亚烷基醚解决方案
    • US20160159990A1
    • 2016-06-09
    • US14904614
    • 2014-07-16
    • BASF SE
    • Joerg ERBESStefan MUESSIGTobias KORTEKAMPMarco KRUEGERMarkus STEFFENAngela ULZHOEFERCecile SCHNEIDERAlexandra WIEDEMANNSimon GRAMLICH
    • C08J3/14B29C47/00C08G75/23
    • C08J3/14B29C47/0011B29K2081/06C08G65/46C08G75/23C08J3/12C08J2381/06C08J2381/08
    • The invention relates to a process for producing polyarylene ether beads from a polyarylene ether solution, comprising the steps of i) dividing the polyarylene ether solution in a division apparatus which is made to vibrate with a frequency of 10 to 1400 Hz to obtain droplets, ii) transferring the droplets into a precipitation bath to form polyarylene ether beads in the precipitation bath which (A) comprises at least one aprotic solvent (component (1)) and at least one protic solvent (component (2)), (B) has a temperature of 0° C. to Tc, where the critical temperature Tc in [° C.] can be determined by the numerical equation Tc=(77−c)/0.58 in which c is the concentration of component (1) in the precipitation bath in [% by weight] and (C) has component (1) in concentrations of 5% by weight to cc, where the critical concentration cc in [% by weight] can be determined by the numerical equation cc=77−0.58*T in which T is the temperature in the precipitation bath in [° C.], where the percentages by weight are each based on the sum of the percentages by weight of component (1) and of component (2) in the precipitation bath.
    • 本发明涉及一种由聚亚芳基醚溶液制备聚亚芳基醚珠粒的方法,包括以下步骤:i)将分散装置中的聚亚芳基醚溶液除以10-1400Hz的频率振动得到液滴,ii (A)包含至少一种非质子溶剂(组分(1))和至少一种质子溶剂(组分(2)),(B)具有至少一种质子溶剂 0℃至Tc的温度,其中[℃]中的临界温度Tc可以通过数值方程Tc =(77-c)/0.58确定,其中c是组分(1)中的浓度 沉淀浴中的[重量%]和(C)的组分(1)的浓度为5重量%〜cc,其中临界浓度cc [重量%]可以通过数学式cc = 77-0.58 * T,其中T是沉淀浴中的温度[℃],其中 重量百分比分别基于沉淀浴中组分(1)和组分(2)的重量百分比之和。
    • 10. 发明申请
    • PROCESS FOR THE TREATMENT OF A RECYCLING STREAM FROM A PLANT FOR THE PRODUCTION OF POLYARYLENE ETHER
    • 用于处理来自用于生产聚亚烷基醚的植物的回收流的方法
    • US20140183032A1
    • 2014-07-03
    • US14140947
    • 2013-12-26
    • BASF SE
    • Christoph SigwartCornelis Hendricus De RuiterJutta VonendJörg Erbes
    • B01D3/14
    • B01D3/141B01D3/143C08G65/46C08G65/48
    • A process is proposed for the treatment of a recycling stream (1) from a plant for the production of polyarylene ether sulfones via polycondensation of aromatic bishalogen compounds and of aromatic bisphenols or their salts in the presence of at least one alkali metal carbonate or ammonium carbonate or alkali metal hydrogencarbonate or ammonium hydrogencarbonate in an N-alkyl-2-pyrrolidone as solvent, comprising from 60 to 90% by weight of water, from 10 to 40% by weight of N-alkyl-2-pyrrolidone and, as contaminant detrimental to specification, up to 5000 ppm by weight of the alkylsuccinimide corresponding to the N-alkyl-2-pyrrolidone and, alongside this, up to 1000 ppm by weight of other substances with higher boiling point than N-alkyl-2-pyrrolidone, in particular inorganic salts, based in each case on the total weight of the recycling stream (1), where the entirety of the components gives 100% by weight, giving a pure N-alkyl-2-pyrrolidone stream (2) which can be returned to the plant for the production of polyarylene ether sulfones, via a final distillation, which comprises carrying out the final distillation process in a partitioned column (TK), with a partition (T) arranged in the longitudinal direction of the column and dividing the space within the partitioned column (TK) into an input region (A), an output region (B), an upper undivided region (C) of the column, and a lower undivided region (D) of the column, the recycling stream (1) being introduced into the column in the input section (A) of the same, and being separated, in the partitioned column (TK), into a bottom stream (7) comprising N-methylsuccinimide, an overhead stream (8) comprising water, and a pure NMP stream, as side stream (2) from the output section (B).
    • 提出了一种方法,用于在至少一种碱金属碳酸盐或碳酸铵存在下,通过芳族双酚类化合物和芳族双酚或其盐的缩聚来处理来自植物的生产聚亚芳基醚砜的再循环料流(1) 或N-烷基-2-吡咯烷酮作为溶剂的碱金属碳酸氢盐或碳酸氢铵,包含60至90重量%的水,10至40重量%的N-烷基-2-吡咯烷酮和作为污染物的有害物质 相对于N-烷基-2-吡咯烷酮至多5000重量ppm的烷基琥珀酰亚胺,并且除此之外,高达1000重量ppm的沸点高于N-烷基-2-吡咯烷酮的其它物质,在 特定的无机盐,基于每种情况下的循环流(1)的总重量,其中全部组分给出100重量%,得到纯N-烷基-2-吡咯烷酮流(2),其可以返回 到pla nt用于生产聚亚芳基醚砜,通过最终蒸馏,其包括在分隔塔(TK)中进行最终蒸馏过程,其中分隔壁(T)沿塔的纵向方向排列,并将空间分成 分隔柱(TK)分为输入区域(A),输出区域(B),塔的上部未分割区域(C)和塔的下部不分割区域(D),再循环流 引入其输入部分(A)中的列并在分隔柱(TK)中分离成包含N-甲基琥珀酰亚胺的底部流(7),包含水的塔顶物流(8)和 纯NMP流,作为来自输出部分(B)的侧流(2)。