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    • 5. 发明公开
    • 1,3-부타디엔의 하이드로시안화를 통한 3-펜텐니트릴의 제조 방법
    • 通过1,3-丁二烯的水解制备3-苯并噻唑的方法
    • KR1020090037973A
    • 2009-04-16
    • KR1020097004633
    • 2007-08-01
    • 바스프 에스이
    • 하데르라인,게르트아에흐트너,토비아스라이트너,안드레아스루이켄,헤르만파프,페터쉐이델,젠스하우너트,안드레아젠거,토마스
    • C07C253/10C07C255/07
    • C07C253/10C07C255/07
    • Distillation of water, 1-and 2 butene and 1,3 butadiene containing a stabilizer in a distillation device K4 to obtain a stream 15 as a bottom product, containing dried 1,3-butadiene, 1-und 2-butene and the stabilizer, and a stream 16 as the top product, containing an azeotropic 1,3-butadiene/water mixture, condensation of the stream 16 in a condenser W, transfer of the obtained condensate (stream 17) in a phase separation device, recycling of the upper liquid phase (stream 18) consisting of 1,3-butadiene as a return flow to column K4 and removal of the lower aqueous phase (stream 19), (a) reaction of stream 15 in a reactor R1 with hydrogen cyanide on at least one catalyst (stream 6a) to obtain stream 1, containing 3-pentenenitrile, 2-methyle-3-butenenitrile, the at least one catalyst, unreacted 1,3-butadiene, 1-and 2-butene and optionally any remaining unreacted hydrogen cyanide, (b) distillation of stream 1 in a distillation device K1 to obtain a stream 2 as a top product, containing the majority of the 1,3-butadiene from stream 1 and to obtain a stream 3 as a bottom product, containing 3-pentenenitrile, the at least one catalyst, 2-methyl 3-butenenitrile, 1-and 2-butene and the remainder of the 1,3 butadiene from stream 1 that was not separated in stream 2, c) distillation of the stream 3 in a distillation device K2 to obtain a stream 5 in a side-tap of the column, said stream containing 3-pentenenitrile and 2-methyl-3-butenenitrile, a stream 6 as bottom product, containing the at least one catalyst and a stream 4 as a top product, d) compression of stream 4 in the compressor V1, separation of a gaseous partial stream 4b containing 1-and 2-butene, transfer of the compressed stream 4a to the condenser W1, common condensation with stream 2 from b) and transfer of the condensate as stream 9, partially as a return flow to column K1 (stream 9b), partially as areturn stream in the reactor R1 (stream 9a) and e) separation of stream 5 by distillation to obtain 3-pentenenitrile and 2-methyl-3-butenenitrile.
    • 在蒸馏装置K4中蒸馏水,1-丁烯和2-丁烯和含有稳定剂的1,3-丁二烯,以获得含有干燥的1,3-丁二烯,1-丁-2-丁烯和稳定剂的作为底部产物的物流15, 和作为顶部产物的料流16,含有共沸的1,3-丁二烯/水混合物,流16在冷凝器W中的冷凝,将获得的冷凝物(物流17)转移到相分离装置中,将上部 由1,3-丁二烯组成的液相(物流18)作为回流至塔K4并除去下部水相(物流19),(a)反应器R1中的物流15与氰化氢在至少一个 催化剂(流6a),以获得含有3-戊烯腈,2-甲基-3-丁烯腈,至少一种催化剂,未反应的1,3-丁二烯,1-和2-丁烯以及任选的任何残留的未反应的氰化氢的料流1, (b)在蒸馏装置K1中蒸馏料流1以获得作为顶部产物的料流2,其包含 大部分来自料流1的1,3-丁二烯,并得到含有3-戊烯腈,至少一种催化剂,2-甲基3-丁烯腈,1-丁烯和2-丁烯的剩余物的作为底部产物的料流3, 来自流2中未在料流2中分离的1,3-丁二烯,c)在蒸馏装置K2中蒸馏料流3以在塔的侧馏分中获得料流5,所述料流含有3-戊烯腈和 2-甲基-3-丁烯腈,作为底部产物的料流6,含有至少一种催化剂和作为顶部产物的料流4,d)压缩机V1中的料流4的压缩,含有1 和2-丁烯,将压缩物流4a转移到冷凝器W1,与b)的物流2共同冷凝,并将作为流9的冷凝物部分地作为返回流转移到柱K1(料流9b),部分地作为转动 反应器R1(料流9a)中的流,e)通过蒸馏分离料流5,得到3-戊烯 三环和2-甲基-3-丁烯腈。