CN109942405B - 二异丁烯的经Pd催化的羟基羰基化方法:配体/Pd比率 - Google Patents
二异丁烯的经Pd催化的羟基羰基化方法:配体/Pd比率 Download PDFInfo
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Abstract
本发明涉及二异丁烯的经Pd催化的羟基羰基化方法:配体/Pd比率。
Description
技术领域
本发明涉及二异丁烯的经Pd催化的羟基羰基化方法:配体/Pd比率。
背景技术
包括丙酸、己二酸和脂肪酸的羧酸用于制备聚合物、药物、溶剂和食品添加剂。产生羧酸的路线通常包括烃、醇或醛的氧化、通过臭氧分解的烯烃的氧化裂解、甘油三酯、腈、酯或酰胺的水解、格氏或有机锂试剂的羧化,以及在卤仿反应中甲基酮的卤化和随后水解。
烯烃的加氢羧化是用于获得羧酸的非常有前途和环境友好的方法。通过甲醇的羰基化制备乙酸,其用碘化物进行。在Koch反应中,通过强碱催化而使水和一氧化碳加成到烯烃上。该方法对于形成二级和三级碳阳离子的烯烃,例如异丁烯产生特戊酸而言是有效的。通过同时将CO和H2O加成到烯烃/炔烃上而发生的加氢羧化提供了合成羧酸的直接且方便的方法。
发明内容
本发明的目的是提供在二异丁烯(DIBN)的经Pd催化的羟基羰基化中提供良好转化的方法。该反应应在一个步骤中进行。
该目的通过根据权利要求1的方法实现。
包括下列方法步骤的方法:
a) 添加二异丁烯;
b) 添加含Pd的化合物,其中Pd能够形成络合物,
c) 添加配体L1:
其中配体L1的加入量为每摩尔Pd 1.0mol至2.0mol配体,
d) 添加乙酸,
e) 进料CO,
f) 将反应混合物加热以使得二异丁烯转化为化合物P1:
在该方法的一个变体中,方法步骤b)中的化合物选自:PdCl2、PdBr2、Pd(acac)2、Pd(dba)2 (dba = 二亚苄叉丙酮)、PdCl2(CH3CN)2。
在该方法的一个变体中,方法步骤b)中的化合物是Pd(acac)2。
在该方法的一个变体中,配体L1的加入量为每摩尔Pd 1.25mol至1.75mol配体。
在该方法的一个变体中,在方法步骤f)中将反应混合物加热至80℃至160℃的温度,优选100℃至140℃的温度。
在该方法的一个变体中,在方法步骤e)中进料CO,以使得所述反应在10 bar至40bar,优选10 bar至30 bar的CO压力下进行。
在该方法的一个变体中,该方法包括额外的方法步骤g):
g) 添加硫酸。
具体实施方式
下面参考实施例更详细地阐述本发明。
向4ml小瓶中装入[Pd(acac)2](1.75mg,0.25mol%)、L1(4.44mg,0.375mol)、H2SO4(3.1mg,1.4mol%)和经烘箱干燥的搅拌棒。然后用隔膜(经PTFE涂覆的苯乙烯-丁二烯橡胶)和酚树脂盖密封小瓶。将小瓶抽真空并用氩气再填充三次。用注射器将H2O(0.29ml)、乙酸(0.85ml)和二异丁烯(DIBN)(2.3mmol)加入到小瓶中。将小瓶置于合金板中,将其转移至氩气气氛下的来自Parr Instruments的4560系列的高压釜(300ml)中。在用CO吹扫高压釜三次后,CO压力增加至室温下15 bar,随后用N2增加至25 bar的压力。反应在120℃下进行3小时。在反应结束后,将高压釜冷却至室温并小心地减压。然后加入异辛烷(100 µl)作为内标。通过GC分析测量转化率。
重复上述实验,其中改变L1/Pd比率。保持所有其它参数。
结果汇编在下表中。
条目 | L1/Pd (mmol/mmol) – L1 (x mol%) | 转化率(%) |
1* | 1.5/1 – 0.375 | 92 |
2* | 2/1 – 0.5 | 83 |
3 | 3/1 – 0.75 | 74 |
4 | 4/1 – 1.0 | 69 |
* 本发明的方法。
如实验结果所示,该目的通过本发明的方法实现。
Claims (6)
2.根据权利要求1的方法,
其中方法步骤b)中的化合物选自:
PdCl2、PdBr2、Pd(acac)2、Pd(dba)2、PdCl2(CH3CN)2,其中dba表示二亚苄叉丙酮。
3.根据权利要求1至2任一项的方法,
其中配体L1的加入量为每摩尔Pd 1.25mol至1.75mol配体。
4.根据权利要求1至2任一项的方法,
其中在方法步骤f)中将反应混合物加热至80℃至160℃的温度。
5.根据权利要求1至2任一项的方法,
其中在方法步骤e)中进料CO,以使得所述反应在10 bar至40 bar的CO压力下进行。
6.根据权利要求1至2任一项的方法,
其中所述方法包括额外的方法步骤g):
g) 添加硫酸。
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EP17209329.6A EP3502083B1 (de) | 2017-12-21 | 2017-12-21 | Verfahren zur pd-katalysierten hydroxycarbonylierung von diisobuten: verhältnis ligand/pd |
EP17209329.6 | 2017-12-21 |
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EP (1) | EP3502083B1 (zh) |
JP (1) | JP6751752B2 (zh) |
KR (1) | KR102146328B1 (zh) |
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MX (1) | MX2018015531A (zh) |
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EP3502084B1 (de) * | 2017-12-21 | 2020-02-12 | Evonik Operations GmbH | Verfahren zur direkten umsetzung von diisobuten zu einer carbonsäure |
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US4619790A (en) * | 1977-03-04 | 1986-10-28 | Basf Aktiengesellschaft | Manufacture of higher alkylcarboxylic acids |
CN106187735A (zh) * | 2016-07-07 | 2016-12-07 | 河北华旭化工有限公司 | 二异丁烯羰基合成特戊酸和2,2,4,4‑四甲基戊酸的方法 |
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ZA965990B (en) | 1995-07-17 | 1997-02-24 | Shell Int Research | Process for the continuous carbonylation of olefins. |
DE102004055252A1 (de) * | 2004-11-16 | 2006-05-24 | Celanese Chemicals Europe Gmbh | Verfahren zur Herstellung von aliphatischen geradkettigen und ß-alkylverzweigten Carbonsäuren |
GB0915946D0 (en) * | 2009-09-11 | 2009-10-28 | Univ St Andrews | Metal-catalysed carbonylation of unsaturated compounds |
SG10201605921SA (en) * | 2015-07-23 | 2017-02-27 | Evonik Degussa Gmbh | Ferrocene-based compounds and palladium catalysts based thereon for the alkoxycarbonylation of ethylenically unsaturated compounds |
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US4619790A (en) * | 1977-03-04 | 1986-10-28 | Basf Aktiengesellschaft | Manufacture of higher alkylcarboxylic acids |
CN106187735A (zh) * | 2016-07-07 | 2016-12-07 | 河北华旭化工有限公司 | 二异丁烯羰基合成特戊酸和2,2,4,4‑四甲基戊酸的方法 |
Non-Patent Citations (1)
Title |
---|
Efficient Palladium-Catalyzed Alkoxycarbonylation of Bulk Industrial Olefins Using Ferrocenyl Phosphine Ligands;Kaiwu Dong et al;《Angewandte Chemie International Edition》;20170330;第56卷;第5267-5271页 * |
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ZA201808495B (en) | 2019-09-25 |
EP3502083B1 (de) | 2020-07-01 |
TWI798315B (zh) | 2023-04-11 |
KR102146328B1 (ko) | 2020-08-21 |
CN109942405A (zh) | 2019-06-28 |
KR20190075835A (ko) | 2019-07-01 |
CA3028186A1 (en) | 2019-06-21 |
JP2019135227A (ja) | 2019-08-15 |
EP3502083A1 (de) | 2019-06-26 |
US20190194114A1 (en) | 2019-06-27 |
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MY197498A (en) | 2023-06-19 |
TW201930250A (zh) | 2019-08-01 |
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