Manufacturing process for 6-aminocapronitrile
    1.
    发明授权
    Manufacturing process for 6-aminocapronitrile 有权
    6-氨基己腈的制备方法

    公开(公告)号:US6048997A

    公开(公告)日:2000-04-11

    申请号:US230742

    申请日:1999-02-01

    摘要: Manufacture of 6-aminocapronitrile or 6-aminocapronitrile/hexamethylene diamine mixtures, involving a) the reaction of at least one pentennitrile, selected from the group consisting of 2,3 and 4-pentennitrile with carbon monoxide and hydrogen in the presence of catalysts, which contain at least one element of the eighth subgroup as active components, obtaining a hydrogenation formylating discharge (I), b) the optional separation of carbon monoxide, hydrogen and the catalyst from the hydrogenation formylating discharge (I), obtaining a hydrogenation formylating discharge (II), c) the separation of 5-formyl valeronitrile from the hydrogenation formylating discharge (I) or (II), d) the reaction of separated 5-formyl valeronitrile with ammonia and hydrogen in the presence of hydrogenating catalysts, selected from the group consisting of rhenium, copper and its compounds as well as metals and metallic compounds of the eighth group, obtaining a hydrogenation discharge, and e) obtaining 6-aminocapronitrile and if necessary hexamethylene diamine.

    摘要翻译: PCT No.PCT / EP97 / 03988 Sec。 371日期1999年2月1日 102(e)1999年2月1日PCT 1997年7月23日PCT公布。 第WO98 / 05632号公报 日期1998年2月12日6-氨基己腈或6-氨基己腈/六亚甲基二胺混合物的制造,涉及a)选自2,3和4-戊腈中的至少一种戊腈与一氧化碳和氢的反应 存在含有第八亚组中的至少一种元素作为活性组分的催化剂,获得加氢甲酰化放电(I),b)任选从氢化甲酰化放电(I)中分离一氧化碳,氢和催化剂,获得 加氢甲酰化放电(II),c)从加氢甲酰化放电(I)或(II)中分离5-甲酰基戊腈; d)在氢化催化剂存在下,分离的5-甲酰基戊腈与氨和氢的反应 ,选自铼,铜及其化合物以及第八组的金属和金属化合物,获得氢化放电,以及 e)获得6-氨基己腈,如果需要的话,得到六亚甲基二胺。

    Process for preparing 6-aminocapronitrile
    2.
    发明授权
    Process for preparing 6-aminocapronitrile 失效
    6-氨基己腈的制备方法

    公开(公告)号:US6121481A

    公开(公告)日:2000-09-19

    申请号:US230837

    申请日:1999-02-01

    CPC分类号: C07C253/30 C07C209/60

    摘要: The invention concerns a process for the preparation of 6-aminocapronitrile or 6-aminocapronitrile-hexamethylene diamine mixtures by: a) reacting 5-formylvaleronitrile with ammonia and hydrogen in the presence of hydrogenation catalysts selected from the group consisting of metals or metal compounds rhenium, copper and elements of group VIII of the periodic table of elements, a hydrogenation discharge product being obtained; and b) extracting from the hydrogenation discharge product 6-aminocapronitrile and optionally hexamethylene diamine, provided that the hydrogenation catalyst does not contain copper, nickel or copper and nickel as it's only components.

    摘要翻译: PCT No.PCT / EP97 / 03987第 371日期1999年2月1日 102(e)1999年2月1日PCT 1997年7月23日PCT公布。 公开号WO98 / 05631 日期1998年2月12日本发明涉及通过以下方法制备6-氨基己腈或6-氨基己腈 - 六亚甲基二胺混合物的方法:a)在选自金属的氢化催化剂存在下,使5-甲酰基戊腈与氨和氢反应 或金属化合物铼,铜和元素周期表第Ⅷ族元素,得到氢化放电产物; 和b)从氢化放电产物6-氨基己腈和任选的六亚甲基二胺中提取,条件是氢化催化剂不含铜,镍或铜和镍,因为它是唯一的组分。

    Preparation of n-butyraldehyde and/or n-butanol
    3.
    发明授权
    Preparation of n-butyraldehyde and/or n-butanol 失效
    正丁醛和/或正丁醇的制备

    公开(公告)号:US5705707A

    公开(公告)日:1998-01-06

    申请号:US676185

    申请日:1996-07-12

    摘要: A process for the preparation of n-butyraldehyde and/or n-butanol, wherein a) 1,3-butadiene is caused to react with an alcohol of the formula I ROH I, to form a mixture of adducts of the formulas II ##STR1## and III ##STR2## b) the adduct III is isomerized to the adduct II, c) the adduct II is isomerized in the presence of a homogeneous or heterogeneous transition metal element catalyst to form the enol ether of the formula IV ##STR3## and d) n-butyraldehyde and/or n-butanol is/are produced from this ether IV by the reaction thereof with hydrogen and water or water only in the presence of a homogeneous or heterogeneous catalyst.

    摘要翻译: PCT No.PCT / EP94 / 00114 Sec。 371日期:1996年7月12日 102(e)日期1996年7月12日PCT提交1995年1月12日PCT公布。 公开号WO95 / 19334 日期1995年7月20日一种用于制备正丁醛和/或正丁醇的方法,其中使a)1,3-丁二烯与式IROHI的醇反应,形成下式的加合物的混合物 II)III和III IIIa)b)加合物III异构化为加合物II,c)加合物II在均相或不均匀的过渡金属元素催化剂的存在下异构化以形成式 IV和d)只有在均相或多相催化剂的存在下,通过与氢和水或水的反应,由该醚IV产生正丁醛和/或正丁醇。

    Preparation of n-butyraldehyde and/or n-butanol
    4.
    发明授权
    Preparation of n-butyraldehyde and/or n-butanol 失效
    正丁醛和/或正丁醇的制备

    公开(公告)号:US5892125A

    公开(公告)日:1999-04-06

    申请号:US793480

    申请日:1997-07-23

    摘要: A process for the preparation of n-butyraldehyde and/or n-butanol, in whicha) 1,3-butadiene is caused to react with an amine of the formula IR.sup.1 R.sup.2 NH, I in which R.sup.1 and R.sup.2 independently denote hydrogen, optionally substituted aliphatic or cycloaliphatic radicals, or aryl or aralkyl radicals or are linked to form a bridging member which can contain hetero atoms, at elevated temperature and under superatmospheric pressure in the presence of a compound of a Group VIIIb element and in the presence of an alkali metal amide or a basic metal oxide to form a mixture of the adducts of the formulas II ##STR1## and III ##STR2## b) the adduct III is isomerized to the adduct II, c) the adduct II is isomerized in the presence of a homogeneous or heterogeneous transition metal element catalyst in the liquid phase or in the presence of a heterogeneous catalyst containing a transition metal element in the gaseous phase to form the enamine of the formula IV ##STR3## and d) n-butyraldehyde and/or n-butanol is/are produced from this enamine.

    摘要翻译: PCT No.PCT / EP95 / 03358 Sec。 371日期1997年7月23日 102(e)日期1997年7月23日PCT 1995年8月24日PCT PCT。 出版物WO96 / 07630 日期:1996年3月14日制备正丁醛和/或正丁醇的方法,其中a)使1,3-丁二烯与式ⅠR1R2NH,Ⅰ的胺反应,其中R1和R2独立地为 表示氢,任选取代的脂族或脂环族基团,或芳基或芳烷基,或连接形成可含有杂原子的桥连构件,在高温和超大气压下,在VIIIb族元素的化合物存在下, 存在碱金属酰胺或碱性金属氧化物以形成式II II和III III的加合物的混合物b)加合物III异构化为加合物II,c)加合物II为 在均相或非均相过渡金属元素催化剂存在下在液相中或在气相中含有过渡金属元素的多相催化剂存在下异构化,形成式IV的烯胺IV和d)n -但 从该烯胺产生乙醛和/或正丁醇。

    Process for producing aldehydes by hydroformylation of olefins
    5.
    发明授权
    Process for producing aldehydes by hydroformylation of olefins 失效
    通过烯烃加氢甲酰化生产醛的方法

    公开(公告)号:US6107524A

    公开(公告)日:2000-08-22

    申请号:US101692

    申请日:1998-07-15

    摘要: A process for the preparation of aldehydes or aldehydes and alcohols by hydroformylation of olefins containing more than 3 carbon atoms comprising a hydroformylation stage, in which the olefin is hydroformylated under a pressure of from 50 to 1000 bar and at a temperature of from 50.degree. to 180.degree. C. using a rhodium catalyst that is dissolved in a homogeneous reaction medium and by extraction of the rhodium catalyst, in whicha) the hydroformylation is carried out in the presence of a rhodium complex, which exhibits, as ligand, a polydentate, organic nitrogen compound that is free from phosphorus and capable of forming complexes with Group VIII metals, which additionally contains at least one tertiary nitrogen radical that is capable of being protonized by a weak acid,b) the effluent of the hydroformylation stage is subjected to extraction with an aqueous solution of a distillable acid optionally following separation or partial separation of aldehydes and alcohols,(c) the aqueous acid extract is subjected to thermal treatment in the presence of an organic solvent or solvent mixture, which is inert under the hydroformylation conditions, with distillation of the aqueous acid, by means of which treatment the complex is deprotonized and transferred to the organic phase, and(d) the organic phase containing the catalyst complex is recycled to the hydroformylation stage.

    摘要翻译: PCT No.PCT / EP97 / 00372 Sec。 371日期:1998年7月15日 102(e)1998年7月15日PCT PCT 1997年1月28日PCT公布。 公开号WO97 / 28113 日期:1997年8月7日一种通过加氢甲酰化含有多于3个碳原子的烯烃制备醛或醛和醇的方法,该方法包括加氢甲酰化阶段,其中烯烃在50至1000巴的压力和温度下加氢甲酰化 使用溶解在均匀的反应介质中并通过萃取铑催化剂的铑催化剂,其中a)在铑配合物的存在下进行加氢甲酰化,其表现出作为 配体,多齿,有机氮化合物,其不含磷并能够与VIII族金属形成络合物,其另外含有至少一个能够被弱酸质子化的叔氮基团,b)加氢甲酰化的流出物 任选在醛和醇的分离或部分分离后,用可蒸馏的酸的水溶液萃取阶段,(c )酸性水提取物在有机溶剂或溶剂混合物存在下进行热处理,所述有机溶剂或溶剂混合物在加氢甲酰化条件下是惰性的,同时蒸馏酸水溶液,通过该处理将络合物去质子化并转移到有机溶剂 相,和(d)含有催化剂络合物的有机相再循环到加氢甲酰化阶段。

    Processes for the preparation of n-butyraldehyde, n-butanol and mixtures
thereof
    8.
    发明授权
    Processes for the preparation of n-butyraldehyde, n-butanol and mixtures thereof 失效
    制备正丁醛,正丁醇及其混合物的方法

    公开(公告)号:US6166265A

    公开(公告)日:2000-12-26

    申请号:US381452

    申请日:1999-09-15

    摘要: Process for the preparation of n-butyraldehyde and/or n-butanol, whereina) 1,3-Butadiene or a butadiene-containing hydrocarbon mixture is reacted with an alcohol of the formula IROH I, where R is C.sub.2 -C.sub.20 -alkyl or alkenyl which is unsubstituted or substituted by 1 or 2 C.sub.1 -C.sub.10 -alkoxy or hydroxyl groups, or is C.sub.6 -C.sub.10 -aryl, C.sub.7 -C.sub.11 -aralkyl or methyl, at elevated temperatures and superatmospheric pressure in the presence of a Bronsted acid or in the presence of a complex of an element of Group Ia, VIIA or VIIIA of the Periodic Table of Elements with phosphorus- or nitrogen-containing ligands to give a mixture of the adducts of the formulae II ##STR1## and III ##STR2## b) the adduct III is isomerized to the adduct II, c) the adduct II is converted into the acetal of the formula IV ##STR3## d) n-butyraldehyde and/or n-butanol are then produced from this acetal IV by reacting it, in the liquid phase, with hydrogen and water or water in the presence of a homogeneous or heterogeneous transition metal catalyst which differs from dicobaltoctacarbonyl or hydridocobalttetracarbonyl.

    摘要翻译: PCT No.PCT / EP98 / 01324 Sec。 371日期1999年9月15日 102(e)1999年9月15日PCT 1998年3月6日PCT PCT。 第WO98 / 41494号公报 日期1998年9月24日制备正丁醛和/或正丁醇的方法,其中a)1,3-丁二烯或含丁二烯的烃混合物与式IROHI的醇反应,其中R是C2- C 1 -C 10 - 芳基,C 7 -C 11 - 芳烷基或甲基未被取代或被1或2个C 1 -C 10 - 烷氧基或羟基取代的C 1 -C 20 - 烷基或烯基,在高温和超大气压的存在下, Br + E,uml + EE ed ed ed ed ed acid acid the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the the 式II和III b)加合物III异构化为加合物II,c)加合物II转化为式IV的缩醛d)然后由该缩醛IV由该缩醛IV制备正丁醛和/或正丁醇,通过使 在液相中,在均相或不均匀转变的存在下,用氢和水或水进行反应 金属催化剂不同于二羰基羰基或氢化钴四羰基。

    Preparation of alcohols and/or aldehydes
    9.
    发明授权
    Preparation of alcohols and/or aldehydes 失效
    醇和/或醛的制备

    公开(公告)号:US5919987A

    公开(公告)日:1999-07-06

    申请号:US716216

    申请日:1996-09-13

    摘要: An industrial preparation of aldehydes and/or alcohols from olefins of more than 3 carbon atoms by a catalytic hydroformylation of the olefin reactant at a pressure of from 50 to 1000 bar and a temperature of from 50 to 180.degree. C. in the presence of an uncomplexed rhodium catalyst homogeneously dissolved in the reaction medium. The catalytic activity of the rhodium is maintained, first by extracting it from the initially discharged reaction mixture by means of an aqueous solution of a nitrogen-containing complexing agent such as sulfonated or carboxylated pyridines, quinolines or the like. In a recycle of the complexed rhodium to be reused in the hydroformylation reaction, the aqueous rhodium-containing extract is fed to a precarbonylation stage where it subjected to a required precarbonylation in the presence of an essentially water-insoluble organic liquid and in the presence of carbon monoxide, synthesis gas or another gas mixture containing carbon monoxide at from 50 to 1000 bar and from 50 to 180.degree. C. The mixture discharged from this precarbonylation stage is then separated into an organic phase containing the main part of the rhodium and an aqueous phase containing the complexing agent. The resulting rhodium-containing organic phase with the regenerated catalyst is then fed into the hydroformylation stage to complete its recycle.

    摘要翻译: PCT No.PCT / EP95 / 00825 Sec。 371日期1996年9月13日 102(e)日期1996年9月13日PCT 1995年3月6日PCT公布。 WO95 / 25080 PCT公开 日期1995年9月21日通过在50至1000巴的压力和50至180℃的温度下通过烯烃反应物的催化加氢甲酰化来工业制备大于3个碳原子的烯烃的醛和/或醇。 在均匀溶解在反应介质中的未络合的铑催化剂存在下进行。 保持铑的催化活性,首先通过含氮络合剂如磺化或羧化吡啶,喹啉等的水溶液从最初排出的反应混合物中提取铑的催化活性。 在加氢甲酰化反应中重复使用的复合铑的再循环中,含水铑萃取物进料到预羰化阶段,其中在基本上不溶于水的有机液体存在下进行所需的预羰基化, 一氧化碳,合成气或含有一氧化碳的另一种气体混合物,从50至1000巴和50至180℃。然后将从该预羰化阶段排出的混合物分离成含有主要部分铑的有机相, 相含有络合剂。 然后将所得到的含再生催化剂的含铑有机相进料到加氢甲酰化阶段以完成其再循环。