CN110092722B - Method for catalytic synthesis of 4-acyl aralkyl phenol derivative - Google Patents
Method for catalytic synthesis of 4-acyl aralkyl phenol derivative Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000007036 catalytic synthesis reaction Methods 0.000 title claims description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 37
- 229960000892 attapulgite Drugs 0.000 claims abstract description 26
- 229910052625 palygorskite Inorganic materials 0.000 claims abstract description 26
- 238000006243 chemical reaction Methods 0.000 claims abstract description 19
- NKTOLZVEWDHZMU-UHFFFAOYSA-N p-cumyl phenol Natural products CC1=CC=C(C)C(O)=C1 NKTOLZVEWDHZMU-UHFFFAOYSA-N 0.000 claims abstract description 16
- QBDSZLJBMIMQRS-UHFFFAOYSA-N p-Cumylphenol Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=CC=C1 QBDSZLJBMIMQRS-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000004927 clay Substances 0.000 claims abstract description 13
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 12
- 239000011973 solid acid Substances 0.000 claims abstract description 9
- 239000011949 solid catalyst Substances 0.000 claims abstract description 8
- 230000008569 process Effects 0.000 claims abstract description 5
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 24
- 238000005917 acylation reaction Methods 0.000 claims description 9
- 230000004913 activation Effects 0.000 claims description 7
- 239000007810 chemical reaction solvent Substances 0.000 claims description 7
- 239000000047 product Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 6
- KHMOASUYFVRATF-UHFFFAOYSA-J tin(4+);tetrachloride;pentahydrate Chemical compound O.O.O.O.O.Cl[Sn](Cl)(Cl)Cl KHMOASUYFVRATF-UHFFFAOYSA-J 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 4
- 230000010933 acylation Effects 0.000 claims description 4
- 239000005457 ice water Substances 0.000 claims description 4
- 239000002243 precursor Substances 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- 238000000605 extraction Methods 0.000 claims description 3
- 230000002194 synthesizing effect Effects 0.000 claims description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 2
- 230000003213 activating effect Effects 0.000 claims description 2
- 239000000706 filtrate Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 3
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 claims 1
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 claims 1
- 239000002841 Lewis acid Substances 0.000 abstract description 10
- 150000007517 lewis acids Chemical class 0.000 abstract description 10
- 230000015572 biosynthetic process Effects 0.000 abstract description 9
- 238000003786 synthesis reaction Methods 0.000 abstract description 9
- 238000006555 catalytic reaction Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 description 9
- 238000003756 stirring Methods 0.000 description 7
- WETWJCDKMRHUPV-UHFFFAOYSA-N acetyl chloride Chemical compound CC(Cl)=O WETWJCDKMRHUPV-UHFFFAOYSA-N 0.000 description 6
- 239000012346 acetyl chloride Substances 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- WFDIJRYMOXRFFG-UHFFFAOYSA-N acetic acid anhydride Natural products CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000001354 calcination Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000002390 rotary evaporation Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- FKSAYGREWVVCIZ-UHFFFAOYSA-N 3-methyl-1-phenylbut-3-en-1-one Chemical compound CC(=C)CC(=O)C1=CC=CC=C1 FKSAYGREWVVCIZ-UHFFFAOYSA-N 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 2
- 238000005481 NMR spectroscopy Methods 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000012018 catalyst precursor Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000002431 foraging effect Effects 0.000 description 2
- 238000003760 magnetic stirring Methods 0.000 description 2
- -1 p-cumyl phenol compound Chemical class 0.000 description 2
- 229920000642 polymer Chemical class 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- FXXACINHVKSMDR-UHFFFAOYSA-N acetyl bromide Chemical compound CC(Br)=O FXXACINHVKSMDR-UHFFFAOYSA-N 0.000 description 1
- 238000007171 acid catalysis Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical class C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920002120 photoresistant polymer Polymers 0.000 description 1
- 229920005668 polycarbonate resin Chemical class 0.000 description 1
- 239000004431 polycarbonate resin Chemical class 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- OEIMLTQPLAGXMX-UHFFFAOYSA-I tantalum(v) chloride Chemical compound Cl[Ta](Cl)(Cl)(Cl)Cl OEIMLTQPLAGXMX-UHFFFAOYSA-I 0.000 description 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 1
- 229910001887 tin oxide Inorganic materials 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/14—Preparation of carboxylic acid esters from carboxylic acid halides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/28—Preparation of carboxylic acid esters by modifying the hydroxylic moiety of the ester, such modification not being an introduction of an ester group
- C07C67/293—Preparation of carboxylic acid esters by modifying the hydroxylic moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明公开了一种催化合成4‑酰基芳烷基苯酚衍生物的方法。在改性凹凸棒石固体酸催化作用下,将对枯基苯酚和酰化试剂催化生成4‑酰基芳烷基苯酚衍生物的过程,所述固体催化剂为凹凸棒石黏土,将天然凹凸棒石黏土在一定温度下热化处理,经路易斯酸在不同温度下对凹凸棒石酸性进行调控,催化对枯基苯酚和酰化试剂生成4‑酰基芳烷基苯酚衍生物。该反应具有反应条件温和,所用催化剂价格低廉,环境友好、工艺简单,催化剂易于分离和可重复使用等特点。The invention discloses a method for catalyzing synthesis of 4-acyl aralkyl phenol derivatives. Under the catalysis of modified attapulgite solid acid, the process of catalyzing p-cumylphenol and acylating reagent to generate 4-acyl aralkylphenol derivatives, the solid catalyst is attapulgite clay, and natural attapulgite is The clay is thermally treated at a certain temperature, and the acidity of attapulgite is regulated by Lewis acid at different temperatures to catalyze p-cumylphenol and acylating reagent to generate 4-acylaralkylphenol derivatives. The reaction has the characteristics of mild reaction conditions, low cost of the used catalyst, environmental friendliness, simple process, easy separation and reusability of the catalyst and the like.
Description
技术领域technical field
本发明属于小分子化合物合成领域,涉及一种催化合成4-酰基芳烷基苯酚衍生物的方法。The invention belongs to the field of synthesis of small molecular compounds, and relates to a method for catalyzing synthesis of 4-acyl aralkyl phenol derivatives.
背景技术Background technique
三酚类化合物主要用于环氧树脂,聚碳酸树酯等高分子化合物的原料,也可用于此类高分子化合物的光阻剂和添加剂。4-酰基芳烷基苯酚衍生物是合成三酚类化合物的重要中间体。Triphenolic compounds are mainly used as raw materials for epoxy resins, polycarbonate resins and other polymer compounds, and can also be used as photoresists and additives for such polymer compounds. 4-Acyl aralkylphenol derivatives are important intermediates in the synthesis of triphenolic compounds.
目前,已知的合成三酚类化合物前体4-酰基芳烷基苯酚衍生物的主要方法是异丙烯基苯乙酮和苯酚类合成。(专利文献:日本特开昭62-084035公报)。众所众知的,原料异丙烯基苯乙酮不仅活泼难以保存,而且价格高合成收率低。而已知的以对枯基苯酚类化合物为原料的合成方法(专利文献:CN 107011124 A),以三氯化铝为催化剂,催化对枯基苯酚类化合物和酰化试剂反应。该方法催化剂不利于回收,且反应后的废水中含有大量铝盐,对环境造成一定危害。因此,需要寻求一种绿色高效的催化剂合成4-酰基芳烷基苯酚衍生物。At present, the main methods for synthesizing 4-acyl aralkyl phenol derivatives, which are precursors of triphenolic compounds, are known to be the synthesis of isopropenyl acetophenone and phenols. (Patent Document: Japanese Patent Laid-Open No. 62-084035). It is well known that the raw material isopropenyl acetophenone is not only active and difficult to store, but also has a high price and a low synthesis yield. And the known synthesis method using p-cumyl phenol compound as raw material (patent document: CN 107011124 A), uses aluminum trichloride as catalyst to catalyze the reaction between p-cumyl phenol compound and acylating reagent. In this method, the catalyst is unfavorable for recovery, and the waste water after the reaction contains a large amount of aluminum salts, which causes certain harm to the environment. Therefore, it is necessary to seek a green and efficient catalyst for the synthesis of 4-acylaralkylphenol derivatives.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种经济绿色4-酰基芳烷基苯酚衍生物制备方法,此过程环境友好、条件温和、催化剂可重复使用,以克服已有技术中污染严重,废液多,后处理复杂等缺点。The object of the present invention is to provide an economical and green preparation method of 4-acyl aralkyl phenol derivatives, which is environmentally friendly, mild in conditions, and reusable catalyst, so as to overcome the serious pollution in the prior art, the large amount of waste liquid, and the need for post-processing Complexity and other disadvantages.
本发明的另一目的是提供一种绿色高效的用于催化合成4-酰基芳烷基苯酚衍生物的催化剂。Another object of the present invention is to provide a green and efficient catalyst for catalyzing the synthesis of 4-acyl aralkyl phenol derivatives.
为实现上述目的,本发明采用的技术方案如下:For achieving the above object, the technical scheme adopted in the present invention is as follows:
一种催化合成4-酰基芳烷基苯酚衍生物的方法,以改性凹凸棒石固体酸为催化剂,将对枯基苯酚和酰化试剂催化生成4-酰基芳烷基苯酚衍生物,其中,改性凹凸棒石固体酸催化剂是以凹凸棒石为前体,经质子酸或路易斯酸对其酸性修饰并在100-1000℃焙烧活化得到;反应路线如下:A method for catalyzing synthesis of 4-acyl aralkyl phenol derivatives, using modified attapulgite solid acid as a catalyst to catalyze p-cumyl phenol and an acylating agent to generate 4-acyl aralkyl phenol derivatives, wherein, The modified attapulgite solid acid catalyst is obtained by using attapulgite as a precursor, modifying its acidity with protonic acid or Lewis acid, and calcining and activating it at 100-1000 ℃; the reaction route is as follows:
所述的酰化试剂选自 The acylating reagent is selected from
式中,X为卤素原子。X=Cl,BrIn the formula, X is a halogen atom. X=Cl, Br
在制备催化剂时,所述的路易斯酸优选钛酸四丁酯、五水合四氯化锡、偏钨酸铵、五氯化钽,路易斯酸与凹凸棒石的重量比优选1:1-20,焙烧活化时间优选1小时到24小时。进一步优选路易斯酸为五水合四氯化锡,焙烧活化时间为2-5小时。When preparing the catalyst, the Lewis acid is preferably tetrabutyl titanate, tin tetrachloride pentahydrate, ammonium metatungstate, tantalum pentachloride, and the weight ratio of Lewis acid to attapulgite is preferably 1:1-20, The firing activation time is preferably 1 hour to 24 hours. Further preferably, the Lewis acid is tin tetrachloride pentahydrate, and the calcination activation time is 2-5 hours.
所述的酰化试剂优选乙酰氯、乙酰溴、醋酸、醋酸酐。进一步优选乙酰氯。The acylating reagents are preferably acetyl chloride, acetyl bromide, acetic acid and acetic anhydride. Acetyl chloride is further preferred.
对枯基苯酚与酰化试剂的摩尔比优选1:2-4,进一步优选1:3。The molar ratio of p-cumylphenol to the acylating agent is preferably 1:2-4, more preferably 1:3.
反应溶剂优选二氯甲烷、氯仿、甲苯、二氯乙烷;优选二氯甲烷。The reaction solvent is preferably dichloromethane, chloroform, toluene, and dichloroethane; preferably dichloromethane.
所述的催化合成4-酰基芳烷基苯酚衍生物的反应温度优选0-30℃,反应时间优选2-4h。The reaction temperature for the catalytic synthesis of 4-acyl aralkylphenol derivatives is preferably 0-30° C., and the reaction time is preferably 2-4 hours.
对枯基苯酚与改性凹凸棒石固体酸催化剂重量比优选1:1-2,进一步优选1:1.3-1.7,最优选1:1.5。The weight ratio of p-cumylphenol to the modified attapulgite solid acid catalyst is preferably 1:1-2, more preferably 1:1.3-1.7, and most preferably 1:1.5.
作为本发明方法的进一步优选,在反应容器中加入反应溶剂和催化剂,室温滴加酰化试剂,滴加完毕后搅拌数分钟后,加入对枯基苯酚,加完后保温搅拌反应,分离过滤出固体催化剂,滤液倒入冰水中,加入反应溶剂提取,分层,水洗,旋蒸出溶剂,得到目标产物4-酰基芳烷基苯酚衍生物,滤出的固体催化剂活化后可再次使用。As a further preference of the method of the present invention, a reaction solvent and a catalyst are added to the reaction vessel, an acylating reagent is added dropwise at room temperature, and after the dropwise addition is completed, stirring for a few minutes, p-cumylphenol is added, and after the addition is completed, the reaction is maintained and stirred, and separated and filtered. Solid catalyst, the filtrate is poured into ice water, the reaction solvent is added to extract, layered, washed with water, and the solvent is distilled off by rotary evaporation to obtain the target product 4-acyl aralkyl phenol derivative, and the filtered solid catalyst can be used again after activation.
优选地,所述反应中,酰化试剂乙酰氯滴加以10℃,滴加完毕后,以25℃反应最佳,反应最佳时间为2.5h。Preferably, in the reaction, the acylating reagent, acetyl chloride, is dropwise at 10°C, and after the dropwise addition, the best reaction is at 25°C, and the optimum reaction time is 2.5h.
优选地,所述的催化剂是以凹凸棒石黏土为前体,经路易斯酸对其酸性修饰并在300-600℃焙烧活化得到。Preferably, the catalyst is obtained by using attapulgite clay as a precursor, acid modification of the catalyst by Lewis acid, and calcination and activation at 300-600°C.
优选地,固载氧化锡的固体催化剂,以五水合四氯化锡与凹凸棒重量比为1:15,搅拌温度为45℃,搅拌48h,在马弗炉中以500℃烘焙制得最佳。Preferably, the solid catalyst for immobilized tin oxide, the weight ratio of tin tetrachloride pentahydrate to attapulgite is 1:15, the stirring temperature is 45 ° C, and the stirring temperature is 48 h, and the best preparation is obtained by baking at 500 ° C in a muffle furnace. .
本发明具有如下优点:The present invention has the following advantages:
1,本发明使用的固体酸催化剂活性高,对产物有很好的选择性,环境友好,不溶于水,易于分离,催化剂成本低廉。1. The solid acid catalyst used in the present invention has high activity, good selectivity to products, is environmentally friendly, insoluble in water, easy to separate, and has low catalyst cost.
2以天然矿物凹凸棒石作为催化剂前体,不仅经济易得,而且能提升矿产资源的附加值,推动我国矿产资源的开发利用。2 Using the natural mineral attapulgite as a catalyst precursor is not only economical and easy to obtain, but also can enhance the added value of mineral resources and promote the development and utilization of mineral resources in my country.
3催化剂分离简单,可重复使用,且催化效率无明显降低。3. The catalyst is simple to separate, can be reused, and the catalytic efficiency is not significantly reduced.
具体实施方式Detailed ways
下列实施例将进一步详细说明本发明,但本发明的内容并不局限于此。The following examples will further illustrate the present invention in detail, but the content of the present invention is not limited thereto.
实施例1Example 1
一种催化4-酰基芳烷基苯酚衍生物的制备方法,包括以下步骤:A preparation method for catalyzing 4-acyl aralkyl phenol derivatives, comprising the following steps:
催化剂制备:取凹凸棒石黏土1.5g,加入配制好的1M硫酸20mL,室温搅拌52h,静置老化12h,离心分离出下层沉淀物,然后用水洗涤至pH成中性,60℃干燥,研磨,之后于真空干燥箱中110℃干燥2h,再于马弗炉中缓慢升温至300℃活化3h,即得到所需催化剂,其为经硫酸处理的凹凸棒石黏土催化剂。Catalyst preparation: take 1.5 g of attapulgite clay, add 20 mL of prepared 1M sulfuric acid, stir at room temperature for 52 h, let stand for aging for 12 h, centrifuge to separate the lower sediment, then wash with water until the pH becomes neutral, dry at 60 °C, grind, After that, it was dried at 110 °C for 2 h in a vacuum drying oven, and then slowly heated to 300 °C in a muffle furnace for activation for 3 h to obtain the desired catalyst, which was a sulfuric acid-treated attapulgite clay catalyst.
酰化:在100mL圆底烧瓶中加入溶剂二氯甲烷30mL,取上述催化剂0.32g,放入圆底烧瓶中。圆底烧瓶放入磁力搅拌子,放置在10℃油浴锅中保温搅拌,取酰化试剂乙酰氯0.213mL,缓慢滴加至圆底烧瓶,滴加完毕后,将称量好的0.2121g的对枯基苯酚缓慢加入到圆底烧瓶中,升温至25℃,搅拌回流反应2.5h。Acylation: Add 30 mL of dichloromethane as a solvent to a 100 mL round-bottomed flask, take 0.32 g of the above catalyst, and put it into the round-bottomed flask. The round-bottomed flask was placed in a magnetic stirring bar, placed in an oil bath at 10°C for thermal insulation and stirring, and 0.213 mL of acylating reagent acetyl chloride was slowly added dropwise to the round-bottomed flask. P-cumylphenol was slowly added to the round-bottomed flask, the temperature was raised to 25°C, and the reaction was stirred and refluxed for 2.5h.
过滤:将上述体系经过减压分离,将固体催化剂与反应体系液体分离。Filtration: The above system is separated under reduced pressure, and the solid catalyst is separated from the liquid of the reaction system.
水洗:将上述滤过的液体倒入梨型分液漏斗中,加入100ml冰水震荡洗涤。静置后,加入30ml二氯甲烷萃取。静置分层,分离下层溶液。Washing with water: Pour the filtered liquid into a pear-shaped separatory funnel, add 100 ml of ice water to shake and wash. After standing, 30 ml of dichloromethane was added for extraction. The layers were left to stand, and the lower layer solution was separated.
旋蒸:将上述下层溶液减压旋蒸出溶剂。只得到酯化产物,未得到目标产物4-酰基芳烷基苯酚。Rotary evaporation: The above lower layer solution was rotary evaporated under reduced pressure to remove the solvent. Only the esterified product was obtained, but the target product 4-acylaralkylphenol was not obtained.
实施例2-3Example 2-3
仅改变催化剂制备中加入的质子酸,其余同实施例1相同。结果如表1所示Only the protonic acid added in the catalyst preparation was changed, and the rest were the same as in Example 1. The results are shown in Table 1
表1Table 1
实施例1-3可见,质子酸并不适用于制备催化4-酰基芳烷基苯酚衍生物的催化剂。It can be seen from Examples 1-3 that protic acids are not suitable for preparing catalysts for catalyzing 4-acylaralkylphenol derivatives.
实施例4Example 4
一种催化4-酰基芳烷基苯酚衍生物的制备方法,包括以下步骤:A preparation method for catalyzing 4-acyl aralkyl phenol derivatives, comprising the following steps:
催化剂制备:取凹凸棒石黏土1.5g,加入配制好的0.1g五水合四氯化锡水溶液10mL,45℃搅拌48h,静置老化12h,于鼓风干燥箱中干燥12h,再于马弗炉中缓慢升温至500℃活化3h,即得到所需催化剂。Catalyst preparation: take 1.5 g of attapulgite clay, add 10 mL of prepared 0.1 g tin tetrachloride pentahydrate aqueous solution, stir at 45°C for 48 h, let stand for aging for 12 h, dry in a blast drying oven for 12 h, and then put it in a muffle furnace The desired catalyst was obtained by slowly heating up to 500 °C for 3 h and activation.
酰化:在100ml圆底烧瓶中加入溶剂二氯甲烷30ml,取上述催化剂0.32g,放入圆底烧瓶中。圆底烧瓶放入磁力搅拌子,放置在10℃油浴锅中保温搅拌,取酰化试剂乙酰氯0.213ml(3mol),缓慢滴加至圆底烧瓶,滴加完毕后,将称量好的0.2121g的对枯基苯酚缓慢加入到圆底烧瓶中,升温至25℃,搅拌回流反应2.5h。Acylation: add 30 ml of dichloromethane as a solvent to a 100 ml round-bottomed flask, take 0.32 g of the above catalyst, and put it into the round-bottomed flask. Put the magnetic stirring bar into the round-bottomed flask, place it in an oil bath at 10°C and keep stirring, take 0.213ml (3mol) of acylating reagent acetyl chloride, and slowly add it dropwise to the round-bottomed flask. 0.2121g of p-cumylphenol was slowly added to the round-bottom flask, the temperature was raised to 25°C, and the reaction was stirred and refluxed for 2.5h.
过滤:将上述体系经过减压分离,将固体催化剂与反应体系液体分离。Filtration: The above system is separated under reduced pressure, and the solid catalyst is separated from the liquid of the reaction system.
水洗:将上述过滤的液体倒入梨型分液漏斗中,加入100ml冰水震荡洗涤。静置后,加入30ml二氯甲烷萃取。静置分层,分离下层溶液。Washing with water: Pour the filtered liquid into a pear-shaped separatory funnel, add 100 ml of ice water and shake for washing. After standing, 30 ml of dichloromethane was added for extraction. The layers were left to stand, and the lower layer solution was separated.
旋蒸:将上述溶液减压旋蒸出溶剂。得到目标产物,产率为84%。目标产物经核磁谱图确认为4-酰基芳烷基苯酚。Rotary evaporation: The above solution was rotary evaporated under reduced pressure to remove the solvent. The target product was obtained in 84% yield. The target product was confirmed to be 4-acylaralkylphenol by NMR spectroscopy.
1H NMR(400MHz,CDCl3)δ(ppm)1.69(s,6H,2×CH3),2.28(s,3H,OCOCH3),2.57(s,3H,CH3CO),6.99(d,J=5.76,2H,ArH),7.20(d,J=5.64,2H,ArH),7.32(d,J=5.48,2H,ArH),7.87(d,J=5.84,2H,ArH) 1 H NMR (400MHz, CDCl 3 )δ(ppm) 1.69(s, 6H, 2×CH 3 ), 2.28(s, 3H, OCOCH 3 ), 2.57(s, 3H, CH 3 CO), 6.99(d, J=5.76, 2H, ArH), 7.20 (d, J=5.64, 2H, ArH), 7.32 (d, J=5.48, 2H, ArH), 7.87 (d, J=5.84, 2H, ArH)
催化剂再活化:将过滤步骤中所得的固体,先用蒸馏水洗涤干净,在于马弗炉中500℃活化三小时备用。Catalyst reactivation: The solid obtained in the filtration step was washed with distilled water, and activated in a muffle furnace at 500° C. for three hours for use.
实施例5-7Examples 5-7
仅改变催化剂制备中加入的路易斯酸,其余同实施例4相同。结果如表2所示。Only the Lewis acid added in the catalyst preparation was changed, and the rest were the same as in Example 4. The results are shown in Table 2.
表2Table 2
实施例4-7可见,利用五水合四氯化锡改性凹凸棒黏土制备的催化剂选择性和催化效率方面显著优越于其他路易斯酸。It can be seen from Examples 4-7 that the catalysts prepared by using tin tetrachloride pentahydrate modified attapulgite clay are significantly superior to other Lewis acids in terms of selectivity and catalytic efficiency.
实施例8-10Examples 8-10
仅改变催化剂制备中的凹凸棒黏土质量,调整路易斯酸与凹凸棒黏土的质量比,其余同实施例4相同。结果如表3所示:Only the quality of attapulgite clay in catalyst preparation was changed, and the mass ratio of Lewis acid to attapulgite clay was adjusted, and the rest were the same as in Example 4. The results are shown in Table 3:
表3table 3
实施例11-13Examples 11-13
仅改变酰化反应中的溶剂,其余同实施例4相同。结果如表4所示:Only the solvent in the acylation reaction was changed, and the rest were the same as in Example 4. The results are shown in Table 4:
表4Table 4
实施例14-16Examples 14-16
仅改变酰化反应中的酰化试剂,其余同实施例4相同。结果如表5所示:Only the acylation reagent in the acylation reaction was changed, and the rest were the same as those in Example 4. The results are shown in Table 5:
表5table 5
实施例17-18Examples 17-18
仅改变酰化反应中乙酰氯的用量,其余同实施例4相同。结果如表6所示:Only the consumption of acetyl chloride in the acylation reaction was changed, and the rest were the same as in Example 4. The results are shown in Table 6:
表6Table 6
实施例19-21Examples 19-21
仅改变酰化反应中反应温度,其余同实施例4相同。结果如表7所示:Only the reaction temperature in the acylation reaction was changed, and the rest were the same as those in Example 4. The results are shown in Table 7:
表7Table 7
实施例22-24Examples 22-24
仅改变酰化反应中反应时间,其余同实施例4相同。结果如表8所示:Only the reaction time in the acylation reaction was changed, and the rest were the same as in Example 4. The results are shown in Table 8:
表8Table 8
实施例25-28Examples 25-28
使用回收的催化剂,其余同实施例4相同。结果如表9所示:The recovered catalyst was used, and the rest were the same as in Example 4. The results are shown in Table 9:
表9Table 9
通过以上实施例可以看出,本发明是以凹凸棒石黏土作为催化剂前体,经过不同酸进行改性,实现对枯基苯酚和酰化试剂反应生成4-酰基芳烷基苯酚衍生物。与路易斯酸催化过程相比,该催化过程绿色无污染,催化剂可重复使用,表现出很好的工业应用前景。It can be seen from the above examples that the present invention uses attapulgite clay as a catalyst precursor, and is modified with different acids to realize the reaction of p-cumylphenol and acylating reagent to generate 4-acylaralkylphenol derivatives. Compared with the Lewis acid catalysis process, the catalysis process is green and pollution-free, and the catalyst can be reused, showing a good industrial application prospect.
尽管已经详细描述了本发明的实施方式,但是应该理解的是,在不偏离本发明的精神和范围的情况下,可以对本发明的实施方式做出各种改变、替换和变更。Although the embodiments of the present inventions have been described in detail, it should be understood that the various changes, substitutions, and alterations could be made hereto without departing from the spirit and scope of the inventions.
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