CN109942402B - 二异丁烯的经Pd催化的羟基羰基化方法:溶剂的影响 - Google Patents
二异丁烯的经Pd催化的羟基羰基化方法:溶剂的影响 Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 33
- FXNDIJDIPNCZQJ-UHFFFAOYSA-N 2,4,4-trimethylpent-1-ene Chemical group CC(=C)CC(C)(C)C FXNDIJDIPNCZQJ-UHFFFAOYSA-N 0.000 title claims abstract description 12
- 239000002904 solvent Substances 0.000 title abstract description 7
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- 239000011541 reaction mixture Substances 0.000 claims description 4
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- FGUUSXIOTUKUDN-IBGZPJMESA-N C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 Chemical compound C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 FGUUSXIOTUKUDN-IBGZPJMESA-N 0.000 claims description 2
- 229910021605 Palladium(II) bromide Inorganic materials 0.000 claims description 2
- 229910002666 PdCl2 Inorganic materials 0.000 claims description 2
- RBYGDVHOECIAFC-UHFFFAOYSA-L acetonitrile;palladium(2+);dichloride Chemical compound [Cl-].[Cl-].[Pd+2].CC#N.CC#N RBYGDVHOECIAFC-UHFFFAOYSA-L 0.000 claims description 2
- WMKGGPCROCCUDY-PHEQNACWSA-N dibenzylideneacetone Chemical compound C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1 WMKGGPCROCCUDY-PHEQNACWSA-N 0.000 claims description 2
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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:溶剂的影响。
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:溶剂的影响。
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:
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,所述方法包括额外的反应步骤g):
g) 添加对甲苯磺酸(PTSA)。
在该方法的一个变体中,将反应混合物在方法步骤f)中加热到80°C至160°C的温度,优选100°C至140°C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20 bar至60bar,优选30 bar至50 bar的CO压力下进行。
具体实施方式
下面通过实施例更详细地阐述本发明。
向4ml小瓶中装入[Pd(acac)2](3.05mg,0.25mol%)、L1(20.64mg,1.0mol%)、PTSA*H2O(28.5mg,3.75mol%)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(0.5ml)、乙酸(1.5ml)和二异丁烯(DIBN)(4.0mmol)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。用CO吹扫高压釜三次后,CO的压力增加到室温下40 bar。反应在120℃下进行20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,其中改变溶剂。保持所有其它参数。
结果汇编在下表中。
条目 | 溶剂 | 转化率(%) |
1 | 3,5,5-三甲基己酸 | 88 |
2 | 甲酸 | 48 |
3* | 乙酸 | >99 |
* 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 (5)
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 (dba = 二亚苄叉丙酮)、PdCl2(CH3CN)2。
3.根据权利要求1或2的方法,
其中所述方法包括额外的反应步骤g):
g) 添加对甲苯磺酸。
4.根据权利要求1或2的方法,
其中在方法步骤f)中将反应混合物加热至80°C至160°C的温度。
5.根据权利要求1或2的方法,
其中在方法步骤e)中进料CO,以使得所述反应在20巴至60巴的CO压力下进行。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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EP17209307.2A EP3502082B1 (de) | 2017-12-21 | 2017-12-21 | Verfahren zur pd-katalysierten hydroxycarbonylierung von diisobuten: einfluss des lösungsmittels |
EP17209307.2 | 2017-12-21 |
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CN109942402A CN109942402A (zh) | 2019-06-28 |
CN109942402B true CN109942402B (zh) | 2022-06-03 |
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CN201811562680.0A Active CN109942402B (zh) | 2017-12-21 | 2018-12-20 | 二异丁烯的经Pd催化的羟基羰基化方法:溶剂的影响 |
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US (1) | US10494324B2 (zh) |
EP (1) | EP3502082B1 (zh) |
JP (1) | JP6665272B2 (zh) |
KR (1) | KR102144335B1 (zh) |
CN (1) | CN109942402B (zh) |
CA (1) | CA3028181C (zh) |
ES (1) | ES2777632T3 (zh) |
MX (1) | MX2018015528A (zh) |
MY (1) | MY191766A (zh) |
PL (1) | PL3502082T3 (zh) |
TW (1) | TWI789467B (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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DE887644C (de) * | 1943-07-21 | 1953-08-24 | Chemische Verwertungsgesellsch | Verfahren zur Herstellung von Carbonsaeuren |
US2470859A (en) * | 1948-02-25 | 1949-05-24 | Du Pont | Nonanoic acid |
US3641074A (en) * | 1969-02-25 | 1972-02-08 | Union Oil Co | Carbonylation of olefins |
US3968133A (en) * | 1974-11-25 | 1976-07-06 | Texaco Inc. | Carboxylation process for preparing linear fatty acids or esters |
DE2709438C3 (de) * | 1977-03-04 | 1980-01-17 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Herstellung von C6. bis C20 Alkylcarbonsäuren |
KR100277526B1 (ko) * | 1992-04-08 | 2001-02-01 | 오노 알버어스 | 팔라듐 포스핀 촉매를 사용하는 카르보닐화 방법 |
TW349088B (en) * | 1994-12-19 | 1999-01-01 | Eastman Chem Co | Carbonylation of olefins |
ZA965990B (en) | 1995-07-17 | 1997-02-24 | Shell Int Research | Process for the continuous carbonylation of olefins. |
DE102012105879A1 (de) * | 2012-07-02 | 2014-01-02 | Oxea Gmbh | Verfahren zur Herstellung von Isononylderivaten |
MY172677A (en) * | 2015-07-23 | 2019-12-10 | Evonik Operations Gmbh | Benzene-based diphosphine ligands for alkoxycarbonylation |
CN106187735B (zh) * | 2016-07-07 | 2019-04-09 | 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 |
EP3502084B1 (de) * | 2017-12-21 | 2020-02-12 | Evonik Operations GmbH | Verfahren zur direkten umsetzung von diisobuten zu einer carbonsäure |
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EP3502082B1 (de) | 2020-02-12 |
EP3502082A1 (de) | 2019-06-26 |
PL3502082T3 (pl) | 2020-07-27 |
ZA201808496B (en) | 2019-09-25 |
CN109942402A (zh) | 2019-06-28 |
CA3028181A1 (en) | 2019-06-21 |
MY191766A (en) | 2022-07-14 |
JP2019112399A (ja) | 2019-07-11 |
ES2777632T3 (es) | 2020-08-05 |
KR20190075842A (ko) | 2019-07-01 |
US10494324B2 (en) | 2019-12-03 |
JP6665272B2 (ja) | 2020-03-13 |
KR102144335B1 (ko) | 2020-08-13 |
CA3028181C (en) | 2021-02-09 |
TWI789467B (zh) | 2023-01-11 |
TW201930248A (zh) | 2019-08-01 |
US20190194111A1 (en) | 2019-06-27 |
MX2018015528A (es) | 2019-06-24 |
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