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    • 3. 发明授权
    • Process for the preparation of alkanediol
    • 制备链烷二醇的方法
    • US07342141B2
    • 2008-03-11
    • US11678009
    • 2007-02-22
    • Evert Van Der HeideCornelis Leonardus Maria Vrouwenvelder
    • Evert Van Der HeideCornelis Leonardus Maria Vrouwenvelder
    • C07C29/159C07C29/15
    • C07C29/12C07C68/065C07C31/202C07C31/205C07C69/96
    • The invention provides a process for the preparation of alkanediol comprising the steps: (i) contacting alkylene oxide with carbon dioxide in the presence of a carbonation catalyst to obtain a reaction mixture containing alkylene carbonate at a reaction temperature of from 100 to 200° C.; (ii) contacting the reaction mixture obtained in step (i) with R—OH, in which R is hydrogen or an alkyl group in the presence of a catalyst to obtain a second reaction mixture containing alkanediol and R2CO3; (iii) subjecting the second reaction mixture containing alkanediol and R2CO3 to a separation step to yield a crude alkanediol stream, which is subjected to distillation to yield a purified stream of alkanediol as the bottom stream; (iv) subjecting the purified stream of alkanediol obtained in step (iii) to further distillation to obtain a second bottom stream containing a mixture of alkanediol, heavy components, and optionally carbonation catalyst, and a top stream containing high purity alkanediol; wherein at least part of the reaction mixture obtained in step (i) is used for heat exchange with at least part of the crude alkanediol stream and/or with at least part of the purified alkanediol stream.
    • 本发明提供一种制备链烷二醇的方法,包括以下步骤:(i)在碳酸化催化剂存在下使环氧烷与二氧化碳接触,得到反应温度为100-200℃的含有碳酸亚烷基酯的反应混合物 ; (ii)在催化剂存在下使步骤(i)中获得的反应混合物与R-OH(其中R是氢或烷基)接触,得到含有链烷二醇和R 2的第二反应混合物 > CO 3 3; (iii)将含有链烷二醇和R 2 CO 3的第二反应混合物进行分离步骤以产生粗链烷二醇流,将其进行蒸馏以产生纯化的流 的链烷二醇作为底部流; (iv)使步骤(iii)中获得的纯化的烷烃二醇进一步蒸馏,得到含有链烷二醇,重组分和任选碳酸化催化剂的混合物的第二塔底料流和含有高纯度链烷二醇的顶流; 其中步骤(i)中获得的至少部分反应混合物用于与至少部分粗链烷二醇流和/或至少部分纯化的链烷二醇流进行热交换。
    • 4. 发明申请
    • PROCESS FOR THE PREPARATION OF A 1,2-ALKYLENE DIOL AND A DIALKYLCARBONATE
    • 制备1,2-亚苄基二醇和对二氯甲烷的方法
    • US20090270657A1
    • 2009-10-29
    • US12108299
    • 2008-04-23
    • Evert Van Der HeideCornelis Leonardus Maria Vrouwenvelder
    • Evert Van Der HeideCornelis Leonardus Maria Vrouwenvelder
    • C07C31/18
    • C07C68/065C07C69/96
    • The present invention relates to a process for the preparation of a 1,2-alkylene diol and a dialkylcarbonate, comprising the steps of (i) contacting a 1,2-alkylene oxide with carbon dioxide in the presence of a carbonation catalyst in a downflow jet reactor to obtain a reaction mixture containing a 1,2-alkylene carbonate, wherein the downflow jet reactor further comprises a deflection means situated in between the ejector means and the outlet means in the direction of the flow path of the gas/liquid mixture generated by the ejector means; (ii) contacting at least part of the reaction mixture obtained in step (i) with an alkanol to obtain a reaction mixture containing a 1,2-alkylene diol and a dialkylcarbonate; and (iii) recovering the 1,2-alkylene diol and the dialkylcarbonate from the reaction mixture obtained in step (ii).
    • 本发明涉及一种1,2-亚烷基二醇和碳酸二烷基酯的制备方法,包括以下步骤:(i)在碳酸化催化剂存在下使1,2-环氧烷与二氧化碳在下流 以获得含有1,2-亚烷基碳酸酯的反应混合物,其中所述下流喷射反应器还包括位于所述喷射装置和所述出口装置之间的偏转装置,所述偏转装置沿所述气/液混合物的流动路径的方向产生 通过喷射器装置; (ii)使步骤(i)中获得的反应混合物的至少一部分与链烷醇接触,得到含有1,2-亚烷基二醇和碳酸二烷基酯的反应混合物; 和(iii)从步骤(ii)中获得的反应混合物中回收1,2-亚烷基二醇和碳酸二烷基酯。
    • 7. 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。
    • 9. 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。
    • 10. 发明申请
    • PROCESS FOR THE PREPARATION OF ALKANEDIOL
    • 制备阿尔卡尼醇的方法
    • US20070203373A1
    • 2007-08-30
    • US11678009
    • 2007-02-22
    • Evert Van Der HeideCornelis Vrouwenvelder
    • Evert Van Der HeideCornelis Vrouwenvelder
    • C07C29/10
    • C07C29/12C07C68/065C07C31/202C07C31/205C07C69/96
    • The invention provides a process for the preparation of alkanediol comprising the steps: (i) contacting alkylene oxide with carbon dioxide in the presence of a carbonation catalyst to obtain a reaction mixture containing alkylene carbonate at a reaction temperature of from 100 to 200° C.; (ii) contacting the reaction mixture obtained in step (i) with R—OH, in which R is hydrogen or an alkyl group in the presence of a catalyst to obtain a second reaction mixture containing alkanediol and R2CO3; (iii) subjecting the second reaction mixture containing alkanediol and R2CO3 to a separation step to yield a crude alkanediol stream, which is subjected to distillation to yield a purified stream of alkanediol as the bottom stream; (iv) subjecting the purified stream of alkanediol obtained in step (iii) to further distillation to obtain a second bottom stream containing a mixture of alkanediol, heavy components, and optionally carbonation catalyst, and a top stream containing high purity alkanediol; wherein at least part of the reaction mixture obtained in step (i) is used for heat exchange with at least part of the crude alkanediol stream and/or with at least part of the purified alkanediol stream.
    • 本发明提供一种制备链烷二醇的方法,包括以下步骤:(i)在碳酸化催化剂存在下使环氧烷与二氧化碳接触,得到反应温度为100-200℃的含有碳酸亚烷基酯的反应混合物 ; (ii)在催化剂存在下使步骤(i)中获得的反应混合物与R-OH(其中R是氢或烷基)接触,得到含有链烷二醇和R 2的第二反应混合物 > CO 3 3; (iii)将含有链烷二醇和R 2 CO 3的第二反应混合物进行分离步骤以产生粗链烷二醇流,将其进行蒸馏以产生纯化的流 的链烷二醇作为底部流; (iv)使步骤(iii)中获得的纯化的烷烃二醇进一步蒸馏,得到含有链烷二醇,重组分和任选碳酸化催化剂的混合物的第二塔底料流和含有高纯度链烷二醇的顶流; 其中步骤(i)中获得的至少部分反应混合物用于与至少部分粗链烷二醇流和/或至少部分纯化的链烷二醇流进行热交换。