CN113600234A - Oleophylic and hydrophobic solid base catalyst for organic condensation reaction - Google Patents

Oleophylic and hydrophobic solid base catalyst for organic condensation reaction Download PDF

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CN113600234A
CN113600234A CN202110710949.0A CN202110710949A CN113600234A CN 113600234 A CN113600234 A CN 113600234A CN 202110710949 A CN202110710949 A CN 202110710949A CN 113600234 A CN113600234 A CN 113600234A
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organic
condensation reaction
solid base
base catalyst
hydrophobic
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张巧红
叶易成
吕振国
朱祝维
王慧斌
翁郭蓥
陈晨
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Ningbo University
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    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
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Abstract

The invention discloses an oleophylic and hydrophobic solid base catalyst for organic condensation reaction, wherein the adsorbent is a catalyst applied to the condensation reaction of ketol, ketoaldehyde or aldol, the catalyst is an oleophylic and hydrophobic silica nano composite material modified by double organic groups, and the composite material is prepared by SiO2The microsphere is used as a substrate, and an alkylamino active group and a hydrophobic organic alkyl group are connected on the surface of the substrate. The invention designs and synthesizes an oleophylic and hydrophobic solid base catalyst which takes an alkylamino active group as a catalytic active center and takes a hydrophobic organic alkyl group as an oleophylic modification group aiming at the characteristics of ketone alcohol, ketone aldehyde or aldol condensation reaction.

Description

Oleophylic and hydrophobic solid base catalyst for organic condensation reaction
Technical Field
The invention belongs to the technical field of catalytic application of solid alkaline nano materials, and particularly relates to an oleophylic and hydrophobic solid base catalyst for organic condensation reaction, which is an oleophylic and hydrophobic silica nano composite material modified by double organic groups, is applied to ketone alcohol, ketone aldehyde or aldol condensation reaction, obtains the oleophylic and hydrophobic base catalyst by taking an introduced alkylamino active group as a catalytic active center and taking a hydrophobic organic alkyl group as an oleophylic modification group, further promotes the adsorption of substrate molecules and the desorption of the product molecules in the condensation reaction, and obtains high substrate conversion rate and condensation product selectivity.
Background
Acetals are a generic name for a class of organic compounds, and are products of condensation of one molecule of aldehyde with two molecules of alcohol, such as acetaldehyde diethyl acetal or benzaldehyde dimethyl acetal. Acetals generally have a pleasant fragrance. Similar to acetals, ketals are the products of condensation of one molecule of ketone with two molecules of alcohol, such as acetonitril or cyclohexanone-dimethyl acetal. In addition, aldehydes or ketones having an alpha hydrogen atom can form enolic anions under certain conditions, which then undergo addition reactions with another molecule of carbonyl compound and form beta-hydroxycarbonyl compounds, a type of reaction known as aldol condensation. The three types of reactions have common characteristics: (1) all belong to condensation reaction; (2) the reactant is organic matter; (3) the product is generated with water; (4) an acid or base is generally used as a catalyst. The three reactions are widely applied in the fields of organic synthesis, medicine and fine chemical industry. In the traditional catalytic process, inorganic acid or alkali is used as a catalyst, and the use of homogeneous inorganic acid or alkali causes the increase of separation cost and the increase of environmental protection pressure. The development of heterogeneous catalysts is considered to be an important way for solving the environmental protection pressure and realizing green production in the process. Especially, the continuous emergence of solid acid and alkali in recent years provides possibility for realizing a heterogeneous catalytic process. However, the existing catalyst has the problems of competitive adsorption caused by low acid-base amount and strong surface polarity, and the like, so that the catalytic activity needs to be improved.
Disclosure of Invention
The technical problem to be solved by the invention is to provide an oleophylic and hydrophobic solid base catalyst for organic condensation reaction aiming at the defects of the prior art, wherein the catalyst has an alkaline center and simultaneously shows oleophylic and hydrophobic characteristics, and is beneficial to adsorption conversion of organic molecules of a substrate and desorption of the product in the condensation reaction when being applied to the condensation reaction of ketol, ketoaldehyde or aldol, and high substrate conversion rate and condensation product selectivity are obtained at the same time.
The technical scheme adopted by the invention for solving the technical problems is as follows: an oleophylic and hydrophobic solid base catalyst for organic condensation reaction features that its adsorbent is the catalyst for ketone alcohol, ketone aldehyde or aldol condensation reaction, and said catalyst is the oleophylic and hydrophobic nano-class silica composite modified by dual organic radicals and prepared from SiO2The microsphere is used as a substrate, and an alkylamino active group and a hydrophobic organic alkyl group are connected on the surface of the substrate.
Preferably, the alkylamino active group is an alkylamino group NH2L, the hydrophobic organic alkyl group is R, and the composite material adopts a general formula m (NH)2L)-SiO2- (R) n represents, wherein:
alkylamino radical NH2L is selected from NH2(C3H6)-(NH2Pr)、NH2-(CH2)2-NH-(CH2)3-(NH2Et) and 4-NH2One of Ph;
the organic alkyl group R is selected from one of methyl, ethyl, propyl, amyl, phenyl, trifluoropropyl, pentafluorophenyl and perfluorodecyl;
m and n are independent numbers, m ranges from 1 to 60, n ranges from 10 to 59, and m + n is less than or equal to 70.
Preferably, the alkylamino group NH in the composite material2L accounts for 5-80% of the total organic groups in mol percent, organic alkyl groups R accounts for 0.1-99% of the total organic groups in mol percent, and the total organic groups are alkylamino groups NH2The sum of L and an organic alkyl group R, wherein the total organic group accounts for 1-60% of the composite material by mass percent.
Preferably, the alkylamino group NH in the composite material2L accounts for 10-50% of the total organic groups in mole percent.
Preferably, the composite material is prepared by a reverse microemulsion method, and the preparation method comprises the following steps:
(1) mixing a surfactant, an organic phase and a cosurfactant to prepare an inverse microemulsion A; mixing ammonia water with the mass concentration of 25-28% and deionized water to prepare a solution B;
(2) mixing low-carbon alcohol orthosilicate, alkylaminosilane and alkylsilane serving as a mixed silicon source to prepare a solution C;
(3) mixing the inverse microemulsion A and the solution B to obtain a solution D; dropwise adding the solution C into the solution D under the stirring condition, and aging for 2-48h to obtain a solution E, wherein the solution E comprises the following components in parts by mass: 4-8 parts of surfactant, 1-4 parts of deionized water, 1-2 parts of ammonia water, 5-9 parts of organic phase, 2-6 parts of cosurfactant, (1-m/100-n/100) parts of low-carbon alcohol orthosilicate ester, m/100 parts of alkylaminosilane and n/100 parts of alkylsilane;
wherein m and n are independent numbers, m ranges from 1 to 60, n ranges from 10 to 59, and m + n is less than or equal to 70; m is the mole percentage of the alkylamino silane in the total silane, n is the mole percentage of the alkyl silane in the total silane, and the total silane is the mixture of the lower alcohol orthosilicate, the alkylamino silane and the alkyl silane in the step (2);
(4) adding acetone or ethanol with the volume 1-3 times that of the cosurfactant in the step (1) into the solution E for demulsification, and centrifuging to collect solids; washing the solid with hot ethanol for 2-6 times, and drying at 80-150 deg.C to obtain uniform granular nanometer material, i.e. oleophylic and hydrophobic solid base catalyst for organic condensation reaction.
Preferably, the lower alcohol ester of ortho-silicic acid is methyl orthosilicate or ethyl orthosilicate; the alkylaminosilane is one of gamma-aminopropyltriethoxysilane, N-beta (aminoethyl) -gamma-aminopropyltriethoxysilane and 4-aminophenyltriethoxysilane; the alkyl silane is organosilane containing one of the following groups: one of methyl (Me), ethyl (Et), propyl (Pr), pentyl (Pe), phenyl (Ph), trifluoropropyl (Pf), pentafluorophenyl (Fp), and perfluorodecyl (FF).
Preferably, the surfactant is an anionic surfactant, a long-chain nonionic surfactant or a cationic surfactant, the anionic surfactant is linear alkyl benzene sodium sulfonate or alpha-alkenyl sodium sulfonate, the long-chain nonionic surfactant is an organic primary amine, an Np series surfactant or a Tween series surfactant, and the cationic surfactant is hexadecyl trimethyl ammonium bromide; the organic phase is cyclohexane, normal hexane or toluene; the cosurfactant is n-hexanol, n-butanol or n-octanol.
Preferably, the substrate molecules of the condensation reaction are ketone and alcohol, ketone and aldehyde or aldehyde and alcohol, and the condensation products are corresponding ketal, acetal and aldol condensation products.
Preferably, the reaction temperature of the condensation reaction is 0-150 ℃, the reaction time is 30-480 minutes, the substrate conversion rate is 50-99%, and the selectivity of the condensation product is more than 90%. Excellent catalytic performance can be obtained under the milder conditions.
Preferably, the condensation reaction is carried out at a temperature of 20 to 120 ℃ for 60 to 360 minutes.
Compared with the prior art, the invention has the following advantages: the invention designs and synthesizes an oleophylic and hydrophobic solid base catalyst which takes an alkylamino active group as a catalytic active center and takes a hydrophobic organic alkyl group as an oleophylic modification group aiming at the characteristics of ketone alcohol, ketone aldehyde or aldol condensation reaction.
Detailed Description
The present invention will be described in further detail with reference to examples.
The oleophilic and hydrophobic solid base catalyst for organic condensation reaction of example 1,
example 1: material A (2 NH)2-SiO2Preparation of-Pr 10)
Mixing 20g of Np-10, 30g of cyclohexane and 5g of n-octanol to prepare a reverse microemulsion A; adding 0.5g of ammonia water into 3g of deionized water to obtain a solution B; mixing 7.32g of methyl orthosilicate, 0.18g of gamma-aminopropyltriethoxysilane and 0.85g of propyltrimethoxysilane to obtain a solution C; pouring the solution B into the inverse microemulsion A to obtain a solution D, adding the solution C into the solution D under vigorous stirring, and aging for 8 hours to obtain a solution E; then, adding 10mL of acetone into the solution E, stirring for 30min, and centrifuging to obtain a light blue solid; adding 30mL of ethanol into the solid, heating and stirring for 10min, and centrifuging; repeating the steps for multiple times until the surfactant is completely removed; drying at 80 ℃ to obtain a silicon dioxide nano composite material A: 2NH2-SiO2-Pr10。
Example 2-example 8: preparation of Material B to Material H
Materials B to H were prepared according to the method of preparation of material A in example 1, with the difference that the type or ratio of alkylaminosilane and alkylsilane used was different, as shown in Table 1, and the general formula of the materials prepared is also shown in Table 1.
TABLE 1
Figure BDA0003132976260000041
2NH prepared as in example 12-SiO2the-Pr 10 silicon dioxide nano composite material is taken as an example, and is used as a solid base catalyst for catalyzing ketone alcohol condensation reaction.
Take 0.1g 2NH2-SiO2The catalyst-Pr 10 was added to the reactor, and 5.8g of acetone and 6.4g of methanol were added thereto. Starting a stirring device, reacting at the temperature of 25 ℃, and stopping the reaction after 120 minutes; and (3) taking out part of reactants after cooling, carrying out quantitative analysis on the acetone and the methanol and the product acetone formal by adopting a gas chromatograph internal standard method, and calculating the conversion rate and the selectivity according to the change of the reactants and the product before and after the reaction. The reaction results are shown in Table 2.
Materials B to H are respectively used as catalysts and applied to organic condensation reaction, the activity evaluation method of the catalysts is the same as that of the embodiment, internal standard gas chromatography is adopted for analysis, and specific substrate types, reaction conditions and reaction results are shown in Table 2.
TABLE 2
Figure BDA0003132976260000042
Figure BDA0003132976260000051

Claims (10)

1. The oleophylic and hydrophobic solid base catalyst for organic condensation reaction features that the adsorbent is catalyst for ketone alcohol, ketone aldehyde or aldol condensation reaction, the catalyst is oleophylic and hydrophobic silica nanometer composite material modified with double organic radicals and the composite material is SiO2The microsphere is used as a substrate, and an alkylamino active group and a hydrophobic organic alkyl group are connected on the surface of the substrate.
2. The lipophilic and hydrophobic solid base catalyst for organic condensation reaction as claimed in claim 1, wherein the alkylamino active group is alkylamino NH2L, the hydrophobic organic alkyl group is R, and the composite material adopts a general formula m (NH)2L)-SiO2- (R) n represents, wherein:
alkylamino radical NH2L is selected from NH2(C3H6)-(NH2Pr)、NH2-(CH2)2-NH-(CH2)3-(NH2Et) and 4-NH2One of Ph;
the organic alkyl group R is selected from one of methyl, ethyl, propyl, amyl, phenyl, trifluoropropyl, pentafluorophenyl and perfluorodecyl;
m and n are independent numbers, m ranges from 1 to 60, n ranges from 10 to 59, and m + n is less than or equal to 70.
3. According to the rightThe lipophilic and hydrophobic solid base catalyst for organic condensation reaction of claim 2, wherein the alkylamino group NH in the composite material2L accounts for 5-80% of the total organic groups in mol percent, organic alkyl groups R accounts for 0.1-99% of the total organic groups in mol percent, and the total organic groups are alkylamino groups NH2The sum of L and an organic alkyl group R, wherein the total organic group accounts for 1-60% of the composite material by mass percent.
4. The lipophilic and hydrophobic solid base catalyst for organic condensation reaction as claimed in claim 3, wherein the alkylamino group NH in the composite material2L accounts for 10-50% of the total organic groups in mole percent.
5. The oleophilic and hydrophobic solid base catalyst for organic condensation reaction as claimed in claim 2, wherein the composite material is prepared by reverse microemulsion method, which comprises the following steps:
(1) mixing a surfactant, an organic phase and a cosurfactant to prepare an inverse microemulsion A; mixing ammonia water with the mass concentration of 25-28% and deionized water to prepare a solution B;
(2) mixing low-carbon alcohol orthosilicate, alkylaminosilane and alkylsilane serving as a mixed silicon source to prepare a solution C;
(3) mixing the inverse microemulsion A and the solution B to obtain a solution D; dropwise adding the solution C into the solution D under the stirring condition, and aging for 2-48h to obtain a solution E, wherein the solution E comprises the following components in parts by mass: 4-8 parts of surfactant, 1-4 parts of deionized water, 1-2 parts of ammonia water, 5-9 parts of organic phase, 2-6 parts of cosurfactant, (1-m/100-n/100) parts of low-carbon alcohol orthosilicate ester, m/100 parts of alkylaminosilane and n/100 parts of alkylsilane;
wherein m and n are independent numbers, m ranges from 1 to 60, n ranges from 10 to 59, and m + n is less than or equal to 70; m is the mole percentage of the alkylamino silane in the total silane, n is the mole percentage of the alkyl silane in the total silane, and the total silane is the mixture of the lower alcohol orthosilicate, the alkylamino silane and the alkyl silane in the step (2);
(4) adding acetone or ethanol with the volume 1-3 times that of the cosurfactant in the step (1) into the solution E for demulsification, and centrifuging to collect solids; washing the solid with hot ethanol for 2-6 times, and drying at 80-150 deg.C to obtain uniform granular nanometer material, i.e. oleophylic and hydrophobic solid base catalyst for organic condensation reaction.
6. A lipophilic hydrophobic type solid base catalyst for organic condensation reaction according to claim 5, characterized in that the lower alcohol ester of ortho-silicic acid is methyl orthosilicate or ethyl orthosilicate; the alkylaminosilane is one of gamma-aminopropyltriethoxysilane, N-beta (aminoethyl) -gamma-aminopropyltriethoxysilane and 4-aminophenyltriethoxysilane; the alkyl silane is organosilane containing one of the following groups: one of methyl, ethyl, propyl, pentyl, phenyl, trifluoropropyl, pentafluorophenyl and perfluorodecyl.
7. The lipophilic and hydrophobic solid base catalyst for organic condensation reaction of claim 5, wherein the surfactant is anionic surfactant, long-chain nonionic surfactant or cationic surfactant, the anionic surfactant is sodium linear alkylbenzene sulfonate or sodium alpha-olefin sulfonate, the long-chain nonionic surfactant is organic primary amine, Np series surfactant or Tween series surfactant, and the cationic surfactant is hexadecyl trimethyl ammonium bromide; the organic phase is cyclohexane, normal hexane or toluene; the cosurfactant is n-hexanol, n-butanol or n-octanol.
8. The lipophilic and hydrophobic solid base catalyst for organic condensation reaction of claim 1, wherein the substrate molecules of the condensation reaction are ketone and alcohol, ketone and aldehyde or aldehyde and alcohol, and the condensation products are corresponding ketal, acetal and aldol condensation products.
9. The lipophilic hydrophobic solid base catalyst for organic condensation reaction as claimed in claim 8, wherein the reaction temperature of condensation reaction is 0-150 ℃, the reaction time is 30-480 minutes, the substrate conversion rate is 50-99%, and the selectivity of condensation product is more than 90%.
10. The lipophilic and hydrophobic solid base catalyst for organic condensation reaction as claimed in claim 9, wherein the condensation reaction is carried out at 20-120 deg.C for 60-360 min.
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Publication number Priority date Publication date Assignee Title
CN115215730A (en) * 2022-06-17 2022-10-21 宁波大学 High-efficiency removal method of aldehyde impurities in alcohols
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