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    • 72. 发明公开
    • VERFAHREN ZUR HERSTELLUNG VON DINITRILEN
    • 用于生产二腈
    • EP1713760A1
    • 2006-10-25
    • EP05701204.9
    • 2005-01-27
    • BASF Aktiengesellschaft
    • JUNGKAMP, TimBAUMANN, RobertBARTSCH, MichaelHADERLEIN, GerdLUYKEN, HermannSCHEIDEL, Jens
    • C07C253/10C07C255/04
    • C07C253/10C07C255/04
    • The invention relates to a method for producing adipodinitrile and methylglutar nitrile, said method being characterised by the following steps: (a) an educt flow containing pentenenitriles is reacted with hydrogen cyanide in the presence of at least one catalyst and at least one promoter to obtain a reaction flow containing pentenenitriles, the at least one catalyst, catalyst breakdown products, the at least one promoter, adipodinitrile and methylglutar nitrile; (b) the reaction flow is distilled to obtain a bottom product flow (3) that is depleted of pentenenitriles and contains the at least one catalyst, catalyst breakdown products, the at least one promoter, adipodinitrile and methylglutar nitrile, and a top product flow (4) enriched in pentenenitriles; (c) the flow (3) is extracted by an extraction means contained in flow (5) to obtain a top product flow (6) that is enriched with extraction means and contains the catalyst, and a bottom product flow (7) that is depleted of extraction means and contains catalyst breakdown products, the at least one promoter, pentenenitriles, adipodinitrile and methylglutar nitrile; (d) the flow (6) is distilled to obtain a bottom product flow (8) containing the catalyst, and a top product flow (9) containing the extraction means; (e) the flow (7) is distilled to obtain a bottom product flow (10) containing catalyst breakdown products, the at least one promoter, pentene nitriles, adipodinitrile and methylglutarnitrile, and a top product flow (11) containing the extraction means; (f) the flow (10) is distilled to obtain a bottom product flow (12) containing catalyst breakdown products, the at least one promoter, pentenenitriles, adipodinitrile and methylglutarnitrile, and a top product flow (13) containing pentenenitriles; (g) the flow (12) is distilled to obtain a bottom product flow (14) containing catalyst breakdown products and the at least one promoter, and a top product flow (15) containing adipodinitrile and methylglutar nitrile; and (h) the flow (15) is distilled to obtain a bottom product flow (16) containing adipodinitrile, and a top product flow (17) containing methylglutarnitrile.
    • 77. 发明公开
    • VERFAHREN ZUR R CKF HRUNG EINER LEWIS-S URE
    • EP1521737A1
    • 2005-04-13
    • EP03763704.8
    • 2003-07-04
    • BASF AKTIENGESELLSCHAFT
    • JUNGKAMP, TimSCHEIDEL, JensLUYKEN, HermannBARTSCH, MichaelBAUMANN, RobertHADERLEIN, Gerd
    • C07C253/10
    • B01J31/24B01J27/32B01J31/1845B01J31/4015B01J31/403B01J2231/343C07C253/10Y02P20/584C07C255/07
    • The invention relates to a method for the recycling of a Lewis acid from a reaction mixture (I), obtained from the hydrocyanation of an olefinically-unsaturated compound to give a nitrile, which has a miscibility gap with water under certain concentration, pressure and temperature conditions, in the presence of a catalyst system comprising a Lewis acid and a complex compound of a phosphorus-containing compound suitable as a ligand and a central atom suitable for said compound, characterised in that a) said complex compound is separated from a mixture (I) to give a mixture (II), b) mixture (II) is treated with water and undergoes a transformation generating pressure and temperature conditions to give a phase (III) with a higher proportion of water than said nitrile and a phase (IV) which has a higher proportion of said nitrile than of water, whereby phase (III) has a higher content of said Lewis acid than phase (IV), c) phase (III) is treated with a liquid diluent (V) which c1) does not form an azeotrope with water and the boiling point of which is higher than that of water under certain pressure conditions, or c2) forms an azeotrope or heteroazeotrope with water under certain pressure conditions, d) the mixture of phase (III) and liquid diluent (V) is distilled under the pressure conditions given in step c1) or c2) to give a mixture (VI) which has a higher proportion of water than of liquid diluent (V) and a mixture (VII) which has a higher proportion of diluent (V) than water, whereby mixture (VII) has a higher content of said Lewis acid than mixture (VI), and e) mixture (VII) is fed to a hydrocyanation of an olefinically-unsaturated compound to give a nitrile, which has a miscibility gap with water under certain concentration, pressure and temperature conditions, in the presence of a catalyst system comprising a Lewis acid and a complex compound of a phosphorus-containing compound suitable as a ligand and a central atom suitable for said compound.
    • 本发明涉及从反应混合物(I)中回收路易斯酸的方法,所述反应混合物(I)由烯属不饱和化合物的氢氰化获得,得到腈,其在一定的浓度,压力和温度下与水具有可混合的间隙 条件下,在包含路易斯酸和适合作为配体的适合于所述化合物的中心原子的含磷化合物的络合物的催化剂体系存在下进行,其特征在于a)将所述络合物从混合物中分离( (II),b)用水处理混合物(II)并进行产生压力和温度条件的相变,得到具有比所述腈更高比例的水的相(III)和相(IV) ),其中所述腈的比例高于水,其中相(III)具有比相(IV)更高含量的所述路易斯酸,c)用液体稀释剂(V)处理相(III),其中c1) 才不是 与水形成共沸物并且在一定压力条件下其沸点高于水的沸点,或者c2)在一定压力条件下与水形成共沸物或非均相共沸混合物,d)相(III)和液体稀释剂 V)在步骤c1)或c2)中给出的压力条件下蒸馏以得到比液体稀释剂(V)具有更高比例的水的混合物(VI)和具有更高比例的稀释剂的混合物(VII) (Ⅴ)的混合物,其中混合物(Ⅶ)比混合物(Ⅵ)具有更高含量的所述路易斯酸,和e)将混合物(Ⅶ)加入烯属不饱和化合物的氢氰化得到腈, 在包含路易斯酸和适合作为配体的含磷化合物和适用于所述化合物的中心原子的配位化合物的催化剂体系存在下,在一定浓度,压力和温度条件下与水混溶的间隙。