TWI798315B - 以配位體/鈀之比率進行二異丁烯之鈀催化羥基羰基化的方法 - Google Patents
以配位體/鈀之比率進行二異丁烯之鈀催化羥基羰基化的方法 Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 35
- 239000003446 ligand Substances 0.000 title claims abstract description 12
- FXNDIJDIPNCZQJ-UHFFFAOYSA-N 2,4,4-trimethylpent-1-ene Chemical compound CC(=C)CC(C)(C)C FXNDIJDIPNCZQJ-UHFFFAOYSA-N 0.000 title claims abstract description 11
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 21
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 12
- 229910052763 palladium Inorganic materials 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- JKDRQYIYVJVOPF-FDGPNNRMSA-L palladium(ii) acetylacetonate Chemical compound [Pd+2].C\C([O-])=C\C(C)=O.C\C([O-])=C\C(C)=O JKDRQYIYVJVOPF-FDGPNNRMSA-L 0.000 claims description 4
- 239000011541 reaction mixture Substances 0.000 claims description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 3
- GNFTZDOKVXKIBK-UHFFFAOYSA-N 3-(2-methoxyethoxy)benzohydrazide Chemical compound COCCOC1=CC=CC(C(=O)NN)=C1 GNFTZDOKVXKIBK-UHFFFAOYSA-N 0.000 claims description 2
- 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
- 101150003085 Pdcl gene Proteins 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
- 230000006315 carbonylation Effects 0.000 claims description 2
- 238000005810 carbonylation reaction Methods 0.000 claims description 2
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims 1
- PJANXHGTPQOBST-VAWYXSNFSA-N Stilbene Natural products C=1C=CC=CC=1/C=C/C1=CC=CC=C1 PJANXHGTPQOBST-VAWYXSNFSA-N 0.000 claims 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims 1
- PJANXHGTPQOBST-UHFFFAOYSA-N stilbene Chemical compound C=1C=CC=CC=1C=CC1=CC=CC=C1 PJANXHGTPQOBST-UHFFFAOYSA-N 0.000 claims 1
- 235000021286 stilbenes Nutrition 0.000 claims 1
- 150000001336 alkenes Chemical class 0.000 description 5
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 4
- 150000001735 carboxylic acids Chemical class 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 238000005658 halogenation reaction Methods 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical class CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000001345 alkine derivatives Chemical class 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000012300 argon atmosphere Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000021523 carboxylation Effects 0.000 description 1
- 238000006473 carboxylation reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 230000026030 halogenation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 125000001979 organolithium group Chemical group 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000007248 oxidative elimination reaction Methods 0.000 description 1
- 238000005949 ozonolysis reaction Methods 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- IUGYQRQAERSCNH-UHFFFAOYSA-N pivalic acid Chemical compound CC(C)(C)C(O)=O IUGYQRQAERSCNH-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 150000003626 triacylglycerols Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
- C07C51/14—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on a carbon-to-carbon unsaturated bond in organic compounds
-
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- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
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- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
- B01J31/2234—Beta-dicarbonyl ligands, e.g. acetylacetonates
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- B01J31/22—Organic complexes
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- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/24—Phosphines, i.e. phosphorus bonded to only carbon atoms, or to both carbon and hydrogen atoms, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, phosphole or anionic phospholide ligands
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- B01J31/2404—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring
- B01J31/2409—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring with more than one complexing phosphine-P atom
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Abstract
以配位體/鈀之比率進行二異丁烯之鈀催化羥基羰基化的方法。
Description
本發明係關於以配位體/鈀之比率進行二異丁烯之鈀催化羥基羰基化的方法。
包括丙酸、己二酸以及脂肪酸的羧酸用於製備聚合物、藥物、溶劑和食品添加劑。產生羧酸的途徑通常包括烴、醇或醛的氧化,經由臭氧分解的烯烴的氧化裂解,甘油三酯、腈、酯或醯胺的水解,格氏試劑(Grignard)或有機鋰試劑的羧化,以及鹵化和隨後鹵代反應中的甲基酮的水解。
烯烴的羥基羧化是用於獲得羧酸的非常有前途以及環境友好的方法。經由甲醇的羰基化產生乙酸,其用碘化物進行。在Koch反應中,向烯烴中加入水和一氧化碳是經由強鹼催化的。該方法對於形成二級和三級碳陽離子的烯烴是有效的,例如,異丁烯至新戊酸。通過同時向烯烴/炔烴中加入CO和H2
O而發生的羥基羧化提供合成羧酸的直接且方便的方法。
本發明之目的係提供在二異丁烯(DIBN)之鈀催化羥基羰基化中的良好轉換方法。該反應必須在一個步驟中進行。
經由如申請專利範圍第1項所述之方法完成該目的。
方法,其包含以下步驟:
a) 加入二異丁烯,
b) 加入含有鈀的化合物,其中該鈀係具有能形成錯合物之能力,
c) 加入配位體L1:
其中該配位體L1係以每mole鈀加入1.0 mol 至2.0 mol之範圍的配位體L1的量,
d) 加入乙酸,
e) 在CO中進料,
f) 加熱該反應混合物以使該二異丁烯轉變為該化合物P1:。
在該方法的一個變化形中,該化合物在方法步驟b)係選自於:PdCl2
、PdBr2
、Pd(acac)2
、Pd(dba)2
(dba=二苯乙烯基丙酮)、PdCl2
(CH3
CN)2
。
在該方法的一個變化形中,該方法步驟b)係Pd(acac)2
。
在該方法的一個變化形中,該配位體L1係以每mole鈀加入1.25 mol至1.75 mol之範圍的配位體L1的量。
在該方法的一個變化形中,在方法步驟f)中該反應混合物係加熱至80°C至160°C的範圍之溫度,較佳係在100°C至140°C的範圍之溫度。
在該方法的一個變化形中,在方法步驟e)中進料該CO以使該反應在10巴至40巴之範圍的CO壓力下進行,較佳係10巴至30巴之範圍。
在該方法的一個變化形中,該方法包含其他的方法步驟g):
g) 加入硫酸。
經由以下的工作實施例更詳細地闡述本發明。
在4 mL小燒瓶中加入[Pd(acac)2
](1.75 mg, 0.25 mol%)、L1(4.44 mg, 0.375 mol%)、H2
SO4
(3.1 mg, 1.4 mol%)和已烘箱乾燥的攪拌棒。然後用隔膜(PTFE塗覆的苯乙烯-丁二烯橡膠)和酚醛樹脂蓋密封小燒瓶。將小燒瓶抽真空並用氬氣再填充三次。H2
O(0.29 ml)、乙酸(0.85 ml)以及二異丁烯(DIBN)(2.3 mmol)經由針筒加入至小燒瓶。將小燒瓶至於合金板上,在氬氣氛下將其轉移至Parr Instruments的4560系列高壓滅菌器(300 ml)中。用CO沖洗高壓滅菌器三次後,在室溫下CO的壓力增加到15巴,且接著以N2
將壓力增加到25巴。反應在120℃下進行3小時。在反應結束時,將高壓滅菌器冷卻至室溫並小心地解壓。然後加入異辛烷(100 µl)作為內部標準。經由GC分析測量轉化率。
以改變L1/Pd的比率重複上述實驗。維持所有其他的參數。
該結果整理如下表中。
*本發明方法
如實驗結果所示,該目的通過本發明的方法實現。
Claims (6)
- 如申請專利範圍第1項所述之方法,其中在方法步驟b)中之該化合物係選自於:PdCl2、PdBr2、Pd(acac)2、Pd(dba)2(dba=二苯乙烯基 丙酮)、PdCl2(CH3CN)2。
- 如申請專利範圍第1項至第2項中任一項所述之方法,其中該配位體L1係以每莫耳鈀加入1.25mol至1.75mol之範圍的配位體的量。
- 如申請專利範圍第1項至第2項中任一項所述之方法,其中在方法步驟f)中該反應混合物係加熱至80℃至160℃的範圍之溫度。
- 如申請專利範圍第1項至第2項中任一項所述之方法,其中在方法步驟e)中進料該CO以使該反應在10巴至40巴之範圍的CO壓力下進行。
- 如申請專利範圍第1項至第2項中任一項所述之方法,其中該方法包含額外的方法步驟g):g)加入硫酸。
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ??17209329.6 | 2017-12-21 | ||
| 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 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201930250A TW201930250A (zh) | 2019-08-01 |
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| PL3502084T3 (pl) * | 2017-12-21 | 2020-07-13 | Evonik Operations Gmbh | Sposób bezpośredniej przemiany diizobutenu w kwas karboksylowy |
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| JPS53111008A (en) * | 1977-03-04 | 1978-09-28 | Basf Ag | Process for preparing higer alkyl carboxylate |
| TW201716422A (zh) * | 2015-07-23 | 2017-05-16 | 贏創德固賽有限責任公司 | 二茂鐵基化合物及以其為基礎之用於乙烯系不飽和化合物之烷氧羰基化的鈀觸媒 |
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| CA1231346A (en) * | 1982-09-30 | 1988-01-12 | Eit Drent | Process for the carbonylation of olefinically unsaturated compounds with a palladium catalyst |
| GB8605034D0 (en) * | 1986-02-28 | 1986-04-09 | Shell Int Research | Carbonylation of compounds |
| 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 |
| 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 |
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| JPS53111008A (en) * | 1977-03-04 | 1978-09-28 | Basf Ag | Process for preparing higer alkyl carboxylate |
| TW201716422A (zh) * | 2015-07-23 | 2017-05-16 | 贏創德固賽有限責任公司 | 二茂鐵基化合物及以其為基礎之用於乙烯系不飽和化合物之烷氧羰基化的鈀觸媒 |
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| ZA201808495B (en) | 2019-09-25 |
| EP3502083A1 (de) | 2019-06-26 |
| US10519091B2 (en) | 2019-12-31 |
| CN109942405B (zh) | 2021-09-17 |
| US20190194114A1 (en) | 2019-06-27 |
| KR20190075835A (ko) | 2019-07-01 |
| JP2019135227A (ja) | 2019-08-15 |
| JP6751752B2 (ja) | 2020-09-09 |
| EP3502083B1 (de) | 2020-07-01 |
| CA3028186A1 (en) | 2019-06-21 |
| MX384079B (es) | 2025-03-14 |
| KR102146328B1 (ko) | 2020-08-21 |
| MY197498A (en) | 2023-06-19 |
| ES2807998T3 (es) | 2021-02-25 |
| CN109942405A (zh) | 2019-06-28 |
| TW201930250A (zh) | 2019-08-01 |
| MX2018015531A (es) | 2019-06-24 |
| CA3028186C (en) | 2021-01-12 |
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