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    • 71. 发明申请
    • Method For Producing 3-Pentenenitrile
    • 生产3-戊烯腈的方法
    • US20080227998A1
    • 2008-09-18
    • US10586007
    • 2005-01-27
    • Jens ScheidelTim JungkampMichael BartschGerd HaderleinRobert BaumannHermann Luyken
    • Jens ScheidelTim JungkampMichael BartschGerd HaderleinRobert BaumannHermann Luyken
    • C07C255/01
    • C07C253/10C07C253/34C07C255/07
    • A process is described for preparing 3-pentenenitrile, characterized by the following process steps: (a) reacting 1,3-butadiene with hydrogen cyanide over at least one catalyst to obtain a stream 1 which comprises 3-pentenenitrile, 2-methyl-3-butenenitrile, the at least one catalyst and 1,3-butadiene, (b) distilling stream 1 in a column to obtain a high-1,3-butadiene stream 2 as the top product and a low-1,3-butadiene stream 3 as the bottom product which comprises 3-pentenenitrile, the at least one catalyst and 2-methyl-3-butenenitrile, (c) distilling stream 3 in a column to obtain a stream 4 as the top product which comprises 1,3-butadiene, a stream 5 which comprises 3-pentenenitrile and 2-methyl-3-butenenitrile at a side draw of the column, and a stream 6 as the bottom product which comprises the at least one catalyst, (d) distilling stream 5 to obtain a stream 7 as the top product which comprises 2-methyl-3-butenenitrile, and a stream 8 as the bottom product which comprises 3-pentenenitrile.
    • 描述了一种制备3-戊烯腈的方法,其特征在于以下工艺步骤:(a)使1,3-丁二烯与氰化氢在至少一种催化剂上反应,得到流1,其包含3-戊烯腈,2-甲基-3 丁烯腈,至少一种催化剂和1,3-丁二烯,(b)在塔中蒸馏物流1,得到作为顶部产物的高-1,3-丁二烯流2和低-1,3-丁二烯流 3作为底部产物,其包含3-戊烯腈,至少一种催化剂和2-甲基-3-丁烯腈,(c)在塔中蒸馏流3以获得作为顶部产物的料流4,其包含1,3-丁二烯 ,在塔的侧馏分中包含3-戊烯腈和2-甲基-3-丁烯腈的料流5和作为底部产物的料流6,其包含至少一种催化剂,(d)蒸馏流5以获得 流7作为顶部产物,其包含2-甲基-3-丁烯腈,以及作为底部产物的料流8,其包含3-戊烯 腈
    • 77. 发明授权
    • Method for producing dinitriles
    • 生产二腈的方法
    • US07816551B2
    • 2010-10-19
    • US10586500
    • 2005-01-27
    • Tim JungkampRobert BaumannMichael BartschGerd HaderleinHermann LuykenJens Scheidel
    • Tim JungkampRobert BaumannMichael BartschGerd HaderleinHermann LuykenJens Scheidel
    • C07C253/10
    • C07C253/10C07C255/04
    • An adiponitrile/methylglutaronitrile preparation process includes distilling a reaction stream to obtain stream 3 depleted in pentenenitriles (bottom product) and stream 4 enriched in pentenenitriles (top product); extracting stream 3 obtaining stream 6 enriched with extractant (top product) and stream 7 depleted in extractant (bottom product); distilling stream 6 obtaining stream 8 comprising the catalyst (bottom product) and stream 9 comprising the extractant (top product); distilling stream 7 obtaining stream 10 (bottom product) and stream 11 comprising the extractant (top product); distilling stream 10 obtaining stream 12 comprising catalyst degradation products, at least one promotor, adiponitrile and methylglutaronitrile (bottom product) and stream 13 comprising pentenenitriles (top product); distilling stream 12 obtaining stream 14 comprising catalyst degradation products and the promotor(s) (bottom product) and stream 15 comprising adiponitrile and methylglutaronitrile (top product); distilling stream 15 obtaining stream 16 comprising adiponitrile (bottom product) and stream 17 comprising methylglutaronitrile (top product).
    • 己二腈/甲基戊二腈的制备方法包括蒸馏反应物流以获得贫饱和腈(最终产物)的流3和富含戊烯腈的流4(顶部产物); 提取物流3获得富集萃取剂(顶部产物)的流6和耗尽萃取剂(底部产物)的料流7; 蒸馏流6获得包含催化剂(底部产物)的流8和包含萃取剂的流9(顶部产物); 蒸馏流7获得流10(底部产物)和包含萃取剂(顶部产物)的料流11; 蒸馏流10获得包含催化剂降解产物的流12,至少一种促进剂,己二腈和甲基戊二腈(底部产物)和包含戊烯腈(顶部产物)的料流13; 蒸馏流12获得包含催化剂降解产物和促进剂(底部产物)的流14和包含己二腈和甲基戊二腈(顶部产物)的料流15; 蒸馏流15获得包含己二腈(底部产物)的流16和包含甲基戊二腈(顶部产物)的料流17。