Catalyst and process for preparing carboxylic acid esters
    1.
    发明授权
    Catalyst and process for preparing carboxylic acid esters 有权
    催化剂和制备羧酸酯的方法

    公开(公告)号:US08053593B2

    公开(公告)日:2011-11-08

    申请号:US12716947

    申请日:2010-03-03

    Abstract: A catalyst and a process for preparing carboxylic acid esters from an aldehyde and an alcohol in the presence of molecular oxygen are disclosed. The catalyst comprises metals supported on a silica-containing support, wherein the metals consist essentially of palladium, lead, an alkali or alkaline earth metal, and at least one of niobium and zirconium. The process for preparing a carboxylic acid ester comprises reacting an aldehyde with an alcohol in the presence of molecular oxygen and the aforementioned catalyst.

    Abstract translation: 公开了一种在分子氧存在下由醛和醇制备羧酸酯的催化剂和方法。 催化剂包含负载在含二氧化硅的载体上的金属,其中金属基本上由钯,铅,碱金属或碱土金属和至少一种铌和锆组成。 制备羧酸酯的方法包括在分子氧和上述催化剂的存在下使醛与醇反应。

    Catalyst and process for preparing carboxylic acid esters
    2.
    发明授权
    Catalyst and process for preparing carboxylic acid esters 有权
    催化剂和制备羧酸酯的方法

    公开(公告)号:US07696125B2

    公开(公告)日:2010-04-13

    申请号:US11174593

    申请日:2005-07-06

    Abstract: A catalyst and a process for preparing carboxylic acid esters from an aldehyde and an alcohol in the presence of molecular oxygen are disclosed. The catalyst comprises metals supported on a silica-containing support, wherein the metals consist essentially of palladium, lead, an alkali or alkaline earth metal, and at least one of niobium and zirconium. The process for preparing a carboxylic acid ester comprises reacting an aldehyde with an alcohol in the presence of molecular oxygen and the aforementioned catalyst.

    Abstract translation: 公开了一种在分子氧存在下由醛和醇制备羧酸酯的催化剂和方法。 催化剂包含负载在含二氧化硅的载体上的金属,其中金属基本上由钯,铅,碱金属或碱土金属和至少一种铌和锆组成。 制备羧酸酯的方法包括在分子氧和上述催化剂的存在下使醛与醇反应。

    Catalyst and process for preparing carboxylic acid esters
    3.
    发明申请
    Catalyst and process for preparing carboxylic acid esters 有权
    催化剂和制备羧酸酯的方法

    公开(公告)号:US20070010684A1

    公开(公告)日:2007-01-11

    申请号:US11174593

    申请日:2005-07-06

    Abstract: A catalyst and a process for preparing carboxylic acid esters from an aldehyde and an alcohol in the presence of molecular oxygen are disclosed. The catalyst comprises metals supported on a silica-containing support, wherein the metals consist essentially of palladium, lead, an alkali or alkaline earth metal, and at least one of niobium and zirconium. The process for preparing a carboxylic acid ester comprises reacting an aldehyde with an alcohol in the presence of molecular oxygen and the aforementioned catalyst.

    Abstract translation: 公开了一种在分子氧存在下由醛和醇制备羧酸酯的催化剂和方法。 催化剂包含负载在含二氧化硅的载体上的金属,其中金属基本上由钯,铅,碱金属或碱土金属和至少一种铌和锆组成。 制备羧酸酯的方法包括在分子氧和上述催化剂的存在下使醛与醇反应。

    Preparation of methyl isobutyl ketone
    4.
    发明授权
    Preparation of methyl isobutyl ketone 失效
    甲基异丁基酮的制备

    公开(公告)号:US5684207A

    公开(公告)日:1997-11-04

    申请号:US683911

    申请日:1996-07-19

    CPC classification number: C07C45/73

    Abstract: A one-step process for selective production of methyl isobutyl ketone includes reacting in the vapor/liquid phase acetone and hydrogen at a temperature of about 100.degree. to 300.degree. C. and a pressure of about 100 to 1000 psig, in the presence of a modified ZSM-5 catalyst having a molar ratio of SiO.sub.2 /Al.sub.2 O.sub.3 from about 20:1 to 680:1, the catalyst being prepared by treating a ZSM-5 zeolite with an organic acid having a pKa of 2 to 5, ion-exchanging or impregnating the ZSM-5 zeolite with a cation selected from the group consisting of palladium cation, platinum cation, copper cation and nickel cation, and activating the resultant catalyst in a reducing atmosphere.

    Abstract translation: 选择性生产甲基异丁基酮的一步法包括在气相/液相丙酮和氢气中,在约100至300℃的温度和约100至1000psig的压力下,在 具有SiO 2 / Al 2 O 3摩尔比为约20:1至680:1的改性ZSM-5催化剂,该催化剂通过用pKa为2至5的有机酸处理ZSM-5沸石,离子交换或 用选自钯阳离子,铂阳离子,铜阳离子和镍阳离子的阳离子浸渍ZSM-5沸石,并在还原气氛中活化所得催化剂。

    CATALYST AND PROCESS FOR PREPARING CARBOXYLIC ACID ESTERS
    5.
    发明申请
    CATALYST AND PROCESS FOR PREPARING CARBOXYLIC ACID ESTERS 有权
    催化剂和制备羧酸酯的方法

    公开(公告)号:US20100160668A1

    公开(公告)日:2010-06-24

    申请号:US12716947

    申请日:2010-03-03

    Abstract: A catalyst and a process for preparing carboxylic acid esters from an aldehyde and an alcohol in the presence of molecular oxygen are disclosed. The catalyst comprises metals supported on a silica-containing support, wherein the metals consist essentially of palladium, lead, an alkali or alkaline earth metal, and at least one of niobium and zirconium. The process for preparing a carboxylic acid ester comprises reacting an aldehyde with an alcohol in the presence of molecular oxygen and the aforementioned catalyst.

    Abstract translation: 公开了一种在分子氧存在下由醛和醇制备羧酸酯的催化剂和方法。 催化剂包含负载在含二氧化硅的载体上的金属,其中金属基本上由钯,铅,碱金属或碱土金属和至少一种铌和锆组成。 制备羧酸酯的方法包括在分子氧和上述催化剂的存在下使醛与醇反应。

    Process for preparing pentenoic esters from formylvaleric esters using a mixed oxide supported noble metal catalyst
    6.
    发明授权
    Process for preparing pentenoic esters from formylvaleric esters using a mixed oxide supported noble metal catalyst 有权
    使用混合氧化物负载的贵金属催化剂由甲酰基戊酸酯制备戊烯酸酯的方法

    公开(公告)号:US06355831B1

    公开(公告)日:2002-03-12

    申请号:US09494423

    申请日:2000-01-31

    CPC classification number: B01J27/1856 B01J27/1806 C07C67/317 C07C69/533

    Abstract: The present invention provides a process for preparing a pentenoic ester, comprising heating a 3-, 4-formylvaleric ester or mixtures thereof at 50° C. to 400° C. in the presence of a supported noble metal catalyst. The noble metal catalyst is supported on a mixed oxide (M1)a(M2)b(M3)cPdAle SiOx, wherein M1 is an alkali metal, M2 is an alkaline earth metal, M3 is a Group IVB metal, a=0.5˜1.5, b=0.2˜0.8, c=0.2˜0.8, d=2˜8, e=3˜10, and x is the stoichiometric value. By means of the specific supported catalyst of the present invention, the selectivity of the 3- and 4-pentenoic esters can be increased and that of the 2-pentenoic ester can be greatly decreased.

    Abstract translation: 本发明提供一种制备戊烯酸酯的方法,包括在负载的贵金属催化剂存在下,在50℃至400℃下加热3-,4-甲酰基戊酸酯或其混合物。 贵金属催化剂负载在混合氧化物(M1)a(M2)b(M3)cPdAle SiOx上,其中M1是碱金属,M2是碱土金属,M3是ⅣB族金属,a = 0.5〜1.5 ,b = 0.2〜0.8,c = 0.2〜0.8,d = 2〜8,e = 3〜10,x为化学计量值。 通过本发明的特定载体催化剂,可以提高3-和4-戊烯酸酯的选择性,并且可以大大降低2-戊烯酸酯的选择性。

    Chlorination process with high para selectivity
    7.
    发明授权
    Chlorination process with high para selectivity 失效
    氯化过程具有较高的对位选择性

    公开(公告)号:US5473084A

    公开(公告)日:1995-12-05

    申请号:US71445

    申请日:1993-06-02

    CPC classification number: C07D213/61 B01J29/60 C07C17/12 B01J2229/16

    Abstract: A heterogeneous catalytic chlorination process for making chlorinated aromatic compounds with high para-selectivity. Examples of chlorinated aromatic compounds that can be prepared using the process disclosed in the present invention include those compounds represented by the following formula: ##STR1## wherein R can be a C1-C3 alkyl, floride, chloride, bromide, iodide, or hydroxyl group. The chlorination process utilizes a de-aluminated zeolite which is prepared by H.sub.4 EDTA or Na.sub.4 EDTA extraction of L-type zeolite to reduce the alumina content thereof. The SiO.sub.2 /Al.sub.2 O.sub.3 ratio of the de-aluminated zeolite is preferably between about 9 and about 40. The de-aluminated zeolite can be ion-exchanged with Group IA or IIA metal ions to further improve its para-selectivity.

    Abstract translation: 用于制备具有高对位选择性的氯化芳族化合物的多相催化氯化方法。 可以使用本发明公开的方法制备的氯化芳族化合物的实例包括由下式表示的那些化合物:其中R可以是C 1 -C 3烷基,氟,氯,溴,碘或羟基 。 氯化方法使用脱铝沸石,其通过H 4 EDTA或Na 4 EDTA萃取L型沸石制备以降低其氧化铝含量。 脱铝沸石的SiO 2 / Al 2 O 3比优选为约9至约40.脱铝沸石可与IA或IIA族金属离子进行离子交换,以进一步提高其对选择性。

    Catalytic processes for esterification of carboxylic acids
    8.
    发明授权
    Catalytic processes for esterification of carboxylic acids 失效
    羧酸酯化的催化方法

    公开(公告)号:US5719311A

    公开(公告)日:1998-02-17

    申请号:US752013

    申请日:1996-11-19

    CPC classification number: C07C67/08 Y02P20/582

    Abstract: An improved process for the esterification of carboxylic acid and alcohols into carboxylic ester is disclosed. It comprises the steps of: (a) charging the esterification reactants into a fixed bed reactor under a predetermined reaction condition; and (b) reacting the esterification reactants in the fixed bed reactor. The fixed bed reactor contains acidic catalysts that are present in a solid phase, and the reaction condition is controlled such that (i) the reactants and the products co-exist in a gas-liquid two-phase equilibrium in the fixed bed reactor and that (ii) at least one component of the reactants is present in one phase and at least one component of the products is present in another phase. Because a phase change is always taking place concurrently with the esterification reaction; the reaction stream is maintained at a relatively uniform temperature. This greatly reduces the chances of catalyst poisoning and minimizes the formation of undesired by-products such as polymers/oligmers and ethers, which are often produced at high temperatures. The concurrent phase change also contributes to the extremely high reaction yield and selectivity, typically better than 90%, observed in the present invention.

    Abstract translation: 公开了一种将羧酸和醇酯化成羧酸酯的改进方法。 它包括以下步骤:(a)在预定的反应条件下将酯化反应物装入固定床反应器; 和(b)使酯化反应物在固定床反应器中反应。 固定床反应器含有存在于固相中的酸性催化剂,并且控制反应条件使得(i)反应物和产物在固定床反应器中以气液两相平衡共存,而且 (ii)反应物的至少一种组分存在于一相中,并且产物的至少一种组分存在于另一相中。 因为酯化反应总是同时发生相变; 反应流保持在相对均匀的温度。 这大大降低了催化剂中毒的机会,并最大限度地减少了常常在高温下生产的不需要的副产物如聚合物/低聚物和醚。 同时的相变也有助于在本发明中观察到的非常高的反应产率和选择性,通常优于90%。

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