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
    • 6. 发明授权
    • Process for the preparation of an alkanediol and a dialkyl carbonate
    • 制备链烷二醇和碳酸二烷基酯的方法
    • US07563919B2
    • 2009-07-21
    • US11677999
    • 2007-02-22
    • Evert Van Der HeideTimothy Michael NisbetGaro Garbis Vaporciyan
    • Evert Van Der HeideTimothy Michael NisbetGaro Garbis Vaporciyan
    • C07C69/96C07C27/00
    • C07C68/065Y02P20/127C07C69/96
    • An alkanediol and a dialkyl carbonate are prepared in a process comprising: (a) contacting an alkylene carbonate with an alkanol feedstock under transesterification conditions in a reactive distillation zone to obtain a top stream comprising dialkyl carbonate and the alkanol and a bottom stream comprising an alkanediol; (b) separating the top stream comprising dialkyl carbonate and the alkanol into an alkanol-rich stream and a dialkyl carbonate-rich stream; (c) recovering the dialkyl carbonate from the dialkyl carbonate-rich stream; and (d) recycling at least part of the alkanol-rich stream to the reactive distillation zone as part of the alkanol feedstock, wherein the alkanol-rich stream is split in at least two portions, and at least one portion is condensed and freed from compounds with a lower boiling point than the alkanol. The process is especially suitable for the production of propylene glycol and dimethyl carbonate from propylene carbonate and methanol.
    • 制备烷基二醇和碳酸二烷基酯的方法包括:(a)在反应蒸馏区中在酯交换反应条件下使烯烃碳酸酯与链烷醇原料接触以获得包含碳酸二烷基酯和链烷醇的底部料流和包含链烷二醇 ; (b)将包含碳酸二烷基酯和链烷醇的顶部料流分离成富链烷醇流和富含碳酸二烷基酯的料流; (c)从富含碳酸二烷基酯的料流中回收碳酸二烷基酯; 和(d)作为链烷醇原料的一部分将至少部分富含链烷醇的料流再循环至反应性蒸馏区,其中富链烷醇流分成至少两部分,并且至少一部分被冷凝并从 沸点低于链烷醇的化合物。 该方法特别适用于从碳酸丙烯酯和甲醇生产丙二醇和碳酸二甲酯。
    • 9. 发明授权
    • Process for the production of dialkyl carbonate and alkanediol
    • 生产碳酸二烷基酯和链烷二醇的方法
    • US07763745B2
    • 2010-07-27
    • US11678008
    • 2007-02-22
    • Evert Van Der HeideTimothy Michael NisbetGaro Garbis Vaporciyan
    • Evert Van Der HeideTimothy Michael NisbetGaro Garbis Vaporciyan
    • C07C69/96
    • C07C68/065C07C29/128C07C68/08Y02P20/127Y02P20/142C07C69/96C07C31/205
    • An alkylene carbonate and an alkanol are subjected to transesterification to yield a dialkyl carbonate and alkanediol in a process comprising (a) introducing the alkylene carbonate and an alkanol feedstock into a reaction zone to react in the presence of a transesterification catalyst to yield an alkanediol-rich stream and a stream comprising dialkyl carbonate and alkanol, which streams are separated; (b) passing the stream comprising dialkyl carbonate and alkanol to an extractive distillation zone in which an extractant is added to the stream; (c) obtaining from the extractive distillation zone an alkanol-rich vapor stream and a bottom stream containing the extractant and the dialkyl carbonate; (d) separating the bottom stream from step (c) in a second non-extractive distillation zone to yield a dialkyl carbonate-rich top stream and a extractant-rich bottom stream; and (e) at least partly recycling the extractant-rich bottom stream to the extractive distillation zone, wherein the extractant-rich bottom stream is used as heat source for the alkanol feedstock.
    • 碳酸亚烷基酯和链烷醇进行酯交换反应,得到碳酸二烷基酯和链烷二醇,该方法包括(a)将碳酸亚烷基酯和链烷醇原料引入反应区,在酯交换催化剂的存在下进行反应,得到链烷二醇 - 富含物流和包含碳酸二烷基酯和链烷醇的物流,所述物流被分离; (b)将包含碳酸二烷基酯和链烷醇的料流送入萃取蒸馏区,其中将萃取剂加入料流中; (c)从萃取蒸馏区获得富链烷醇蒸气流和含有萃取剂和碳酸二烷基酯的底部料流; (d)在第二非萃取蒸馏区中将步骤(c)的塔底物流分离,得到富含二烷基碳酸盐的顶部物流和富含萃取剂的塔底物流; 和(e)至少部分地将萃取剂富集底部物流再循环到萃取蒸馏区,其中富萃取剂底部料流用作链烷醇原料的热源。
    • 10. 发明授权
    • Process for the preparation of an alkanediol and a dialkyl carbonate
    • 制备链烷二醇和碳酸二烷基酯的方法
    • US07732630B2
    • 2010-06-08
    • US12017296
    • 2008-01-21
    • Timothy Michael NisbetGaro Garbis VaporciyanCornelis Leonardus Maria VrouwenvelderPaul Wood
    • Timothy Michael NisbetGaro Garbis VaporciyanCornelis Leonardus Maria VrouwenvelderPaul Wood
    • C07C69/96
    • C07C68/065Y02P20/127C07C69/96
    • An alkanediol and a dialkyl carbonate are prepared in a process comprising: (a) reacting an alkylene carbonate and an alkanol feedstock in a reaction zone under transesterification conditions to obtain a product mixture of dialkyl carbonate, unconverted alkanol, the alkanediol, and unconverted alkylene carbonate; (b) separating dialkyl carbonate and unconverted alkanol from the product mixture to obtain a bottom product stream containing alkanediol and unconverted alkylene carbonate; (c) recovering the dialkyl carbonate; and (d) separating alkanediol from the bottom product stream to leave a recycle stream comprising unconverted alkylene carbonate, wherein the recycle stream comprising unconverted alkylene carbonate is split in at least two portions, and at least one portion is recycled to the reaction zone and another portion is subjected to hydrolysis to yield alkanediol and carbon dioxide.
    • 制备烷基二醇和碳酸二烷基酯的方法包括:(a)在酯交换条件下使反应区中的碳酸亚烷基酯和链烷醇原料反应,得到碳酸二烷基酯,未转化的链烷醇,链烷二醇和未转化的碳酸亚烃酯的产物混合物 ; (b)从产物混合物中分离出碳酸二烷基酯和未转化的链烷醇,得到含有链烷二醇和未转化的碳酸亚烃酯的底部产物流; (c)回收碳酸二烷基酯; 和(d)从底部产物流分离链烷二醇以留下包含未转化的碳酸亚烃酯的再循环料流,其中包含未转化的碳酸亚烃酯的再循环料流至少分成两部分,并且至少一部分再循环至反应区,另一部分再循环至反应区 部分水解,得到链烷二醇和二氧化碳。