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CN103288845B - Spiro-compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5] hendecane and synthetic method thereof - Google Patents

Spiro-compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5] hendecane and synthetic method thereof Download PDF

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CN103288845B
CN103288845B CN201310198873.3A CN201310198873A CN103288845B CN 103288845 B CN103288845 B CN 103288845B CN 201310198873 A CN201310198873 A CN 201310198873A CN 103288845 B CN103288845 B CN 103288845B
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propane
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CN103288845A (en
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彭永利
罗灿
万春杰
熊丽君
赖小莹
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Wuhan Institute of Technology
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Abstract

The invention relates to a spiro-compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5] hendecane. The molecular formula of the 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5] hendecane is C9H8O6, and the structural formula is shown in the specification. The 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5] hendecane disclosed by the invention is a highly symmetric oxygenous polybasic spiro-compound; according to the invention, the 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5] hendecane generates a linear polymer by realizing the ring-opening polymerization initiated through an initiating agent under a certain condition by being used as a curing agent in epoxide resin and generates volume expansion reaction, so that the epoxide resin is subjected to volume expansion caused by no volume shrinkage in a curing process.

Description

螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷及其合成方法Spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane and its synthesis method

技术领域technical field

本发明涉及一种螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷及其合成方法。The invention relates to a spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane and a synthesis method thereof.

背景技术Background technique

热固性环氧树脂在固化过程中会发生体积收缩,它会造成材料强度下降,甚至导致材料产生微裂纹或开裂、尺寸不稳定或交接接头的脱胶等缺陷。减少环氧树脂体积收缩率的常用方法有:降低反应体系中活性官能团的含量;选择反应温度较低的固化体系;添加无机粉状填料;增韧改性等。但是这些方法都有各自缺点和使用局限性,如不能明显改善环氧树脂体系的体积收缩问题;使反应体系粘度增大,产生气泡难以排除;成本较高难以实现工业化生产等。Thermosetting epoxy resins will shrink in volume during the curing process, which will cause the strength of the material to decrease, and even cause defects such as micro-cracks or cracks, dimensional instability, or degumming of the transfer joints. Common methods to reduce the volume shrinkage of epoxy resins include: reducing the content of active functional groups in the reaction system; selecting a curing system with a lower reaction temperature; adding inorganic powder fillers; toughening modification, etc. However, these methods have their own shortcomings and application limitations, such as not being able to significantly improve the volume shrinkage of the epoxy resin system; increasing the viscosity of the reaction system, resulting in bubbles that are difficult to eliminate; high cost and difficult to realize industrial production.

膨胀单体的出现从根本上解决了环氧树脂体系体积收缩的问题。迄今为止,已发现的膨胀单体仅仅局限在双环原酸酯、螺环原酸酯和螺环原碳酸酯等结构的化合物上。而其中又以螺环原碳酸酯类聚合时体积膨胀率较为理想。The emergence of expansion monomers fundamentally solves the problem of volume shrinkage of epoxy resin systems. So far, the expansion monomers that have been found are only limited to compounds with structures such as bicyclic orthoesters, spirocyclic orthoesters and spirocyclic orthocarbonates. Among them, the volume expansion rate of the spiro ring orthocarbonate is more ideal when it is polymerized.

目前学者们主要通过在环氧树脂体系中加入膨胀单体如3,9-二(2-降冰片烯)-1,5,7,11-四氧杂螺[5,5]十一烷、3,9-二(对甲氧基苯亚甲基)-1,5,7,11-四氧杂螺环[5,5]十一烷等的研究思路进行相关环氧树脂固化收缩的问题,但是这些究还仅局限于实验室阶段,材料研制成本高,实际应用受限。At present, scholars mainly add expansion monomers such as 3,9-bis(2-norbornene)-1,5,7,11-tetraoxaspiro[5,5]undecane, 3,9-bis(p-methoxybenzylidene)-1,5,7,11-tetraoxaspiro[5,5]undecane and other research ideas related to the curing shrinkage of epoxy resin , but these studies are still limited to the laboratory stage, the cost of material development is high, and the practical application is limited.

发明内容Contents of the invention

本发明所要解决的技术问题是针对上述现有技术存在的不足而提供一种螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷及其合成方法,操作简便,条件温和,易于实现工业化生产。The technical problem to be solved by the present invention is to provide a spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecyl for the above-mentioned deficiencies in the prior art The alkane and its synthesis method have the advantages of simple operation, mild conditions, and easy realization of industrial production.

本发明为解决上述提出的问题所采用的技术方案为:The technical scheme that the present invention adopts for solving the above-mentioned problem is:

螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷,它的分子式为C9H8O6,结构式为 The spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane has a molecular formula of C 9 H 8 O 6 and a structural formula of

上述螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,分为三步:(1)由多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷以水为溶剂,在腈化剂的作用下,由相转移催化剂和无配体的铜催化合成1,3-二腈基-2,2-二(腈甲基)丙烷;The synthetic method of above-mentioned spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane is divided into three steps: (1) by polyhalogenated hydrocarbon 1 , 3-dibromo-2,2-bis(bromomethyl)propane uses water as solvent, under the action of nitrilation agent, synthesizes 1,3-dinitrile- 2,2-bis(nitrilemethyl)propane;

(2)1,3-二腈基-2,2-二(腈甲基)丙烷在无机强酸作用下水解得到1,3-二羧基-2.2-二(乙酸基)丙烷。(2) 1,3-dicarboxy-2,2-bis(nitrilemethyl)propane is hydrolyzed under the action of strong inorganic acid to obtain 1,3-dicarboxy-2.2-bis(acetoxy)propane.

(3)由1,3-二羧基-2,2-二(乙酸基)丙烷与乙酸酐在催化剂作用下发生交换反应生成对称产物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷。(3) The exchange reaction of 1,3-dicarboxy-2,2-di(acetoxy)propane and acetic anhydride under the action of a catalyst produces the symmetrical product 2,4,8,10-tetracarbonyl-3,9-di Oxaspiro[5,5]undecane.

按上述方案,所述溶剂水与无配体的铜催化剂的摩尔比为5:1~7:1。According to the above scheme, the molar ratio of the solvent water to the ligand-free copper catalyst is 5:1˜7:1.

按上述方案,所述腈化剂为无水K4Fe(CN)6,无水K4Fe(CN)6与多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为3:2~5:4。According to the above scheme, the nitrilation agent is anhydrous K 4 Fe(CN) 6 , anhydrous K 4 Fe(CN) 6 and polyhalogenated hydrocarbon 1,3-dibromo-2,2-bis(bromomethyl ) The molar ratio of propane is 3:2 to 5:4.

按上述方案,所述相转移催化剂为四丁基溴化铵(TBAB),无配体的铜催化剂为Cu(OAc)2。According to the above scheme, the phase transfer catalyst is tetrabutylammonium bromide (TBAB), and the ligand-free copper catalyst is Cu(OAc)2.

按上述方案,所述相转移催化剂TBAB与多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1~1:1.5,无配体的铜催化剂Cu(OAc)2占相转移催化剂总质量的的8%~10%。According to the above scheme, the molar ratio of the phase transfer catalyst TBAB to the polyhalogenated hydrocarbon 1,3-dibromo-2,2-bis(bromomethyl)propane is 1:1~1:1.5, and the copper without ligand The catalyst Cu(OAc) 2 accounts for 8%-10% of the total mass of the phase transfer catalyst.

按上述方案,所述步骤(1)反应温度160℃~200℃,反应时间50~80min。According to the above scheme, the reaction temperature of the step (1) is 160° C. to 200° C., and the reaction time is 50 to 80 minutes.

按上述方案,所述水解反应步骤通过在无机强酸存在下,1,3-二腈基-2,2-二(腈甲基)丙烷与水反应,所述水解反应水的用量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1.5~1:2.0。According to the above scheme, the hydrolysis step reacts 1,3-dicyano-2,2-bis(nitrile methyl)propane with water in the presence of strong inorganic acid, and the amount of the hydrolysis reaction water is the same as that of 1,3 - The molar ratio of dinitrile-2,2-bis(nitrilemethyl)propane is 1:1.5˜1:2.0.

按上述方案,所述无机强酸为98%浓硫酸,浓硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1~1.5:1。According to the above scheme, the strong inorganic acid is 98% concentrated sulfuric acid, and the molar ratio of concentrated sulfuric acid to 1,3-dicyano-2,2-bis(nitrile methyl)propane is 1:1˜1.5:1.

按上述方案,所述步骤(3)的催化剂为冰醋酸,所述催化剂为反应物1,3-二羧基-2,2-二(乙酸基)丙烷投料摩尔量的0.1~0.15倍。According to the scheme above, the catalyst in the step (3) is glacial acetic acid, and the catalyst is 0.1 to 0.15 times the molar amount of the reactant 1,3-dicarboxy-2,2-bis(acetoxy)propane.

按上述方案,所述步骤(3)中1,3-二羧基-2,2-二(乙酸基)丙烷与乙酸酐的投料摩尔比为1:1.5~2.1。According to the scheme above, the molar ratio of 1,3-dicarboxy-2,2-di(acetoxy)propane to acetic anhydride in the step (3) is 1:1.5-2.1.

按上述方案,所述步骤(3)中反应温度为90~110℃,反应时间为6~12h。According to the above scheme, the reaction temperature in the step (3) is 90-110° C., and the reaction time is 6-12 hours.

上述螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,具体步骤如下:The synthesis method of the above-mentioned spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane, the specific steps are as follows:

(1)按照摩尔比为3:2~5:4,准备腈化剂无水K4Fe(CN)6与1,3-二溴-2,2-二(溴甲基)丙烷备用;按照转移催化剂TBAB与1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1~1:1.5准备TBAB;无配体的铜催化剂Cu(OAc)2占相转移催化剂的总质量的8%~10%;按照溶剂水的量与铜催化剂的摩尔比为5:1~7:1取水备用。(1) According to the molar ratio of 3:2 to 5:4, prepare the anhydrous K 4 Fe(CN) 6 and 1,3-dibromo-2,2-bis(bromomethyl)propane as the nitrilation agent for later use; The molar ratio of transfer catalyst TBAB to 1,3-dibromo-2,2-bis(bromomethyl)propane is 1:1~1:1.5 to prepare TBAB; ligand-free copper catalyst Cu(OAc) 2 occupies the phase transfer 8% to 10% of the total mass of the catalyst; according to the molar ratio of the amount of solvent water to the copper catalyst being 5:1 to 7:1, water is taken for later use.

将Cu(OAc)2催化剂加入到溶剂水中,搅拌至均相,再加入无水K4[Fe(CN)6]、TBAB以及1,3-二溴-2,2-二(溴甲基)丙烷,将容器密封后于160℃~200℃加热反应50min~80min,反应结束后,使体系自然冷却至室温,用乙醚萃取产物三次,用旋转蒸发仪旋蒸乙醚,GC检测分析,并使产物1,3-二腈基-2,2-二(腈甲基)丙烷通过色谱柱纯化;Add Cu(OAc) 2 catalyst to solvent water, stir until homogeneous, then add anhydrous K 4 [Fe(CN) 6 ], TBAB and 1,3-dibromo-2,2-bis(bromomethyl) Propane, seal the container and heat the reaction at 160°C to 200°C for 50min to 80min. After the reaction, let the system cool down to room temperature naturally, extract the product with ether three times, use a rotary evaporator to rotate the ether, GC detection and analysis, and make the product 1,3-dicyano-2,2-bis(nitrile methyl)propane is purified by chromatographic column;

(2)在氮气氛围下,于室温向装有搅拌器的反应器中,加入所需水总体积的2/3(所需水的总量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1.5~1:2.0);随后倾倒98%H2SO4,硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷摩尔比1:1~1.5:1,,使反应体系温度升高至120℃,然后在1h内引入上述步骤所制备得1,3-二腈基-2,2-二(腈甲基)丙烷,反应体系温度控制在120℃,随后在此温度下保温20~40min后,在10min内加入所需水总体积余下的1/3,并将温度升高到130℃保持6h,反应结束后停止搅拌,反应介质分层,使之自然冷却至90℃,将上层与下层水相分离,得到1,3-二羧基-2.2-二(乙酸基)丙烷;(2) Under a nitrogen atmosphere, add 2/3 of the total volume of required water to a reactor equipped with a stirrer at room temperature (the total amount of required water and 1,3-dinitrile-2,2- The molar ratio of bis(nitrile methyl)propane is 1:1.5~1:2.0); then pour 98% H 2 SO 4 , sulfuric acid and 1,3-dicyano-2,2-bis(nitrile methyl)propane The molar ratio is 1:1~1.5:1, the temperature of the reaction system is raised to 120°C, and then the 1,3-dicyano-2,2-bis(nitrile methyl)propane prepared in the above steps is introduced within 1h , the temperature of the reaction system is controlled at 120°C, and then kept at this temperature for 20 to 40 minutes, then add the remaining 1/3 of the total volume of water required within 10 minutes, and raise the temperature to 130°C for 6 hours, stop after the reaction is over Stirring, the reaction medium is layered, allowed to cool naturally to 90°C, and the upper layer and the lower layer are separated to obtain 1,3-dicarboxy-2.2-bis(acetoxy)propane;

(3)按照1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐的投料摩尔比为1:1.5~2.1,催化剂冰乙酸为1,3-二羧基-2,2-二(乙酸基)丙烷投料摩尔量的0.1~0.15倍,将1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐及冰乙酸置于带有搅拌器、回流冷凝管和温度计的三口烧瓶中,反应温度控制在90~110℃,反应时间为6~12h,至反应液澄清反应结束;反应结束后停止加热,将产物经减压蒸馏后,残余物经三氯甲烷重结晶,抽滤干燥称重,即得2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷。(3) According to the molar ratio of 1,3-dicarboxy-2,2-di(acetoxy)propane and acetic anhydride is 1:1.5~2.1, the catalyst glacial acetic acid is 1,3-dicarboxy-2,2- 0.1 to 0.15 times the molar amount of bis(acetoxy)propane, put 1,3-dicarboxy-2,2-bis(acetoxy)propane, acetic anhydride and glacial acetic acid in a place with agitator, reflux condenser and In the three-necked flask with a thermometer, the reaction temperature is controlled at 90-110°C, and the reaction time is 6-12 hours until the reaction liquid is clarified and the reaction is completed; stop heating after the reaction is completed, and the product is distilled under reduced pressure, and the residue is reconstituted with chloroform. Crystallize, filter, dry and weigh to obtain 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane.

本发明所述反应过程如下:The reaction process of the present invention is as follows:

与现有技术相比,本发明的优点在于:Compared with the prior art, the present invention has the advantages of:

第一,2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷是一种高度对称的含氧的多元螺环化合物,其在环氧树脂中作为固化剂在一定条件下由引发剂引发实现开环聚合,生成线形聚合物,发生体积膨胀反应,使得环氧树脂在固化过程中体积不收缩以至于体积膨胀。本发明从酸酐类固化剂着手研发出具有膨胀效果的2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷,该方法简便易行,条件温和,产物纯净,产率可达96.2%~98.5%。First, 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane is a highly symmetrical oxygen-containing multi-component spiro compound, which is used in epoxy resin As a curing agent, under certain conditions, the ring-opening polymerization is initiated by the initiator to form a linear polymer, and a volume expansion reaction occurs, so that the volume of the epoxy resin does not shrink or expand during the curing process. The present invention develops 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane with expansion effect from the acid anhydride curing agent, the method is simple and easy, and the conditions Mild, the product is pure, and the yield can reach 96.2% to 98.5%.

第二,本发明将多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷在以水为溶剂,以无毒且廉价的K4[Fe(CN)6]为腈化剂,由TBAB为相转移催化剂和无配体的Cu(OAc)2为催化剂催化合成1,3-二腈基-2,2-二(腈甲基)丙烷,再将1,3-二腈基-2,2-二(腈甲基)丙烷在无机强酸作用下水解得到1,3-二羧基-2.2-二(乙酸基)丙烷,此方法简便易行,无毒价廉,反应条件温和,产物产率高纯度大,可以得到比原料烃类碳链更长的多元羧酸。Second, the present invention uses polyhalogenated hydrocarbon 1,3-dibromo-2,2-bis(bromomethyl)propane in water as solvent and non-toxic and cheap K 4 [Fe(CN) 6 ] as Nitrilation agent, by TBAB as phase-transfer catalyst and unliganded Cu (OAc) 2 as catalyst catalytic synthesis 1,3-dicyano-2,2-two (nitrile methyl) propane, then 1,3- Dinitrile-2,2-bis(nitrile methyl)propane is hydrolyzed under the action of strong inorganic acid to obtain 1,3-dicarboxy-2.2-bis(acetoxy)propane. This method is simple, non-toxic and cheap, and the reaction The conditions are mild, the product yield is high and the purity is high, and polycarboxylic acids with longer carbon chains than raw material hydrocarbons can be obtained.

第三,本发明将1,3-二羧基-2,2-二(乙酸基)丙烷与乙酸酐在催化剂冰乙酸的作用下发生交换反应生成对称产物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷,该发明操作简便,反应条件温和,产物纯净。Thirdly, in the present invention, 1,3-dicarboxy-2,2-bis(acetoxy)propane and acetic anhydride undergo an exchange reaction under the action of catalyst glacial acetic acid to generate symmetrical product 2,4,8,10-tetracarbonyl- 3,9-dioxaspiro[5,5]undecane, the invention has simple operation, mild reaction conditions and pure product.

附图说明Description of drawings

图1是2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷分子结构图。Figure 1 is a molecular structure diagram of 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane.

图2是2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷制备工艺路线图。Figure 2 is a process route diagram for the preparation of 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane.

图3是2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的红外光谱图。Fig. 3 is an infrared spectrogram of 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane.

具体实施方式Detailed ways

为了更好地理解本发明,下面结合实例进一步阐明本发明的内容,但本发明不仅仅局限于下面的实施例。In order to better understand the present invention, the content of the present invention is further illustrated below in conjunction with examples, but the present invention is not limited only to the following examples.

本发明所述无水K4Fe(CN)6是经过如下方法得到的,将K4Fe(CN)63H2O在研钵中研磨成粉末状颗粒,平铺于表面皿上,表面皿置于真空干燥箱中,75℃干燥即可。当然,其他工艺获得的无水K4Fe(CN)6也适用于本发明。The anhydrous K 4 Fe(CN) 6 of the present invention is obtained through the following method. K 4 Fe(CN) 6 3H 2 O is ground into powder particles in a mortar, spread on a watch glass, and the watch glass Place in a vacuum drying oven at 75°C to dry. Of course, anhydrous K 4 Fe(CN) 6 obtained by other processes is also suitable for the present invention.

实施例1Example 1

2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的制备方法,步骤如下:The preparation method of 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane, the steps are as follows:

(1)按照摩尔比为3:2,准备腈化剂无水K4Fe(CN)6与1,3-二溴-2,2-二(溴甲基)丙烷备用;按照转移催化剂TBAB与1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1准备TBAB;无配体的铜催化剂Cu(OAc)2占相转移催化剂的总质量的10%,按照溶剂水的量与铜催化剂的摩尔比为5:1取水备用;(1) According to the molar ratio of 3:2, prepare nitrilation agent anhydrous K 4 Fe(CN) 6 and 1,3-dibromo-2,2-bis(bromomethyl)propane for subsequent use; according to transfer catalyst TBAB and The molar ratio of 1,3-dibromo-2,2-di(bromomethyl) propane is 1:1 to prepare TBAB; Copper catalyst Cu(OAc) without ligand accounts for 10% of the total mass of phase transfer catalyst, According to the amount of solvent water and the mol ratio of copper catalyst being 5:1, water is taken for subsequent use;

将Cu(OAc)2催化剂加入到溶剂水中,搅拌至均相,再加入无水K4[Fe(CN)6]、TBAB以及1,3-二溴-2,2-二(溴甲基)丙烷,将容器密封后于180℃加热反应50min,反应结束后,使体系自然冷却至室温,用乙醚萃取产物三次,用旋转蒸发仪旋蒸乙醚,GC检测分析,并使产物1,3-二腈基-2,2-二(腈甲基)丙烷通过色谱柱纯化;Add Cu(OAc) 2 catalyst to solvent water, stir until homogeneous, then add anhydrous K 4 [Fe(CN) 6 ], TBAB and 1,3-dibromo-2,2-bis(bromomethyl) Propane, seal the container and heat the reaction at 180°C for 50 minutes. After the reaction, let the system cool down to room temperature naturally, extract the product with ether three times, use a rotary evaporator to rotate the ether, GC detection and analysis, and make the product 1,3-di Nitrile-2,2-two (nitrile methyl) propane is purified by chromatographic column;

反应式:Reaction formula:

(2)在氮气氛围下,于室温向装有搅拌器的反应器中,加入所需水总体积的2/3(所需水的总量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1.5);随后倾倒98%H2SO4,硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷摩尔比1:1,,使反应体系温度升高至120℃,然后在1h内引入上述步骤所制备得1,3-二腈基-2,2-二(腈甲基)丙烷,反应体系温度控制在120℃,随后在此温度下保温20min后,在10min内加入所需水总体积余下的1/3,并将温度升高到130℃保持6h,反应结束后停止搅拌,反应介质分层,使之自然冷却至90℃,将上层与下层水相分离,得到1,3-二羧基-2.2-二(乙酸基)丙烷。经过蒸馏、萃取、重结晶,产率为91%,反应式如下:(2) Under a nitrogen atmosphere, add 2/3 of the total volume of required water to a reactor equipped with a stirrer at room temperature (the total amount of required water and 1,3-dinitrile-2,2- The molar ratio of bis(nitrile methyl)propane is 1:1.5); then pour 98% H 2 SO 4 , the molar ratio of sulfuric acid to 1,3-dicyano-2,2-bis(nitrile methyl)propane is 1: 1. Raise the temperature of the reaction system to 120°C, and then introduce the 1,3-dicyano-2,2-bis(nitrile methyl)propane prepared in the above steps within 1 hour, and control the temperature of the reaction system at 120°C , and then kept at this temperature for 20 minutes, added the remaining 1/3 of the total volume of water required within 10 minutes, and raised the temperature to 130°C for 6 hours, stopped stirring after the reaction, and separated the reaction medium to make it naturally After cooling to 90°C, the upper layer and the lower layer were separated to obtain 1,3-dicarboxy-2.2-di(acetoxy)propane. After distillation, extraction and recrystallization, the yield is 91%. The reaction formula is as follows:

(3)按照1,3-二羧基-2,2-二(乙酸基)丙烷、乙酸酐和催化剂冰乙酸的摩尔比为1:2.1:0.15,将1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐及冰乙酸置于带有搅拌器、回流冷凝管和温度计的三口烧瓶中,反应温度控制在90℃,反应时间为12h,至反应液澄清反应结束;反应结束后停止加热,将产物经减压蒸馏后,残余物经三氯甲烷重结晶,抽滤干燥称重,即得2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷,产率96.2%。(3) According to the molar ratio of 1,3-dicarboxy-2,2-di(acetoxy)propane, acetic anhydride and catalyst glacial acetic acid as 1:2.1:0.15, 1,3-dicarboxy-2,2- Di(acetoxy)propane, acetic anhydride and glacial acetic acid were placed in a three-necked flask equipped with a stirrer, a reflux condenser and a thermometer, the reaction temperature was controlled at 90°C, and the reaction time was 12 hours until the reaction liquid was clarified and the reaction was completed; the reaction was completed After that, the heating was stopped, and the product was distilled under reduced pressure, and the residue was recrystallized from chloroform, filtered, dried and weighed to obtain 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[ 5,5] Undecane, yield 96.2%.

反应式如下:The reaction formula is as follows:

图3为所得产物红外图谱,分析如下表,因此证实按照本发明所述方法得到的产物为2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷。Fig. 3 is the infrared spectrum of the product obtained, and the analysis is as follows, so it is confirmed that the product obtained according to the method of the present invention is 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]dec One alkane.

实施例2Example 2

2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的制备方法,步骤如下:The preparation method of 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane, the steps are as follows:

(1)按照摩尔比为4:3,准备腈化剂无水K4Fe(CN)6与1,3-二溴-2,2-二(溴甲基)丙烷备用;按照转移催化剂TBAB与1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1.5准备TBAB;无配体的铜催化剂Cu(OAc)2占相转移催化剂的总质量的9%,按照溶剂水的量与铜催化剂的摩尔比为7:1取水备用;(1) According to the molar ratio of 4:3, prepare nitrilation agent anhydrous K 4 Fe(CN) 6 and 1,3-dibromo-2,2-bis(bromomethyl)propane for subsequent use; according to transfer catalyst TBAB and The molar ratio of 1,3-dibromo-2,2-bis(bromomethyl) propane is 1:1.5 to prepare TBAB; Copper catalyst Cu(OAc) without ligand accounts for 9% of the total mass of phase transfer catalyst, According to the amount of solvent water and the mol ratio of copper catalyst being 7:1, water is taken for subsequent use;

将Cu(OAc)2催化剂加入到溶剂水中,搅拌至均相,再加入无水K4[Fe(CN)6]、TBAB以及1,3-二溴-2,2-二(溴甲基)丙烷,将容器密封后于200℃加热反应75min,反应结束后,使体系自然冷却至室温,用乙醚萃取产物三次,用旋转蒸发仪旋蒸乙醚,GC检测分析,并使产物1,3-二腈基-2,2-二(腈甲基)丙烷通过色谱柱纯化;Add Cu(OAc) 2 catalyst to solvent water, stir until homogeneous, then add anhydrous K 4 [Fe(CN) 6 ], TBAB and 1,3-dibromo-2,2-bis(bromomethyl) Propane, seal the container and heat the reaction at 200°C for 75 minutes. After the reaction, let the system cool down to room temperature naturally, extract the product with ether three times, use a rotary evaporator to rotate the ether, GC detection and analysis, and make the product 1,3-di Nitrile-2,2-two (nitrile methyl) propane is purified by chromatographic column;

(2)在氮气氛围下,于室温向装有搅拌器的反应器中,加入所需水总体积的2/3(所需水的总量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:2.0);随后倾倒98%H2SO4,硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷摩尔比1.5:1,,使反应体系温度升高至120℃,然后在1h内引入上述步骤所制备得1,3-二腈基-2,2-二(腈甲基)丙烷,反应体系温度控制在120℃,随后在此温度下保温40min后,在10min内加入所需水总体积余下的1/3,并将温度升高到130℃保持6h,反应结束后停止搅拌,反应介质分层,使之自然冷却至90℃,将上层与下层水相分离,得到1,3-二羧基-2.2-二(乙酸基)丙烷,经过蒸馏、萃取、重结晶,产率为92.5%。(2) Under a nitrogen atmosphere, add 2/3 of the total volume of required water to a reactor equipped with a stirrer at room temperature (the total amount of required water and 1,3-dinitrile-2,2- The molar ratio of bis(nitrile methyl)propane is 1:2.0); then pour 98% H 2 SO 4 , the molar ratio of sulfuric acid to 1,3-dicyano-2,2-bis(nitrile methyl)propane is 1.5: 1. Raise the temperature of the reaction system to 120°C, and then introduce the 1,3-dicyano-2,2-bis(nitrile methyl)propane prepared in the above steps within 1 hour, and control the temperature of the reaction system at 120°C , and then kept at this temperature for 40 minutes, added the remaining 1/3 of the total volume of water required within 10 minutes, and raised the temperature to 130°C for 6 hours, stopped stirring after the reaction, and separated the reaction medium to make it naturally Cool to 90°C, separate the upper and lower aqueous phases to obtain 1,3-dicarboxy-2.2-bis(acetoxy)propane, and the yield is 92.5% after distillation, extraction and recrystallization.

(3)按照1,3-二羧基-2,2-二(乙酸基)丙烷、乙酸酐和催化剂冰乙酸的摩尔比为1:1.8:0.1,将1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐及冰乙酸置于带有搅拌器、回流冷凝管和温度计的三口烧瓶中,反应温度控制在100℃,反应时间为8h,至反应液澄清反应结束;反应结束后停止加热,将产物经减压蒸馏后,残余物经三氯甲烷重结晶,抽滤干燥称重,即得2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷,产率97.6%。(3) According to the molar ratio of 1,3-dicarboxy-2,2-di(acetoxy)propane, acetic anhydride and catalyst glacial acetic acid as 1:1.8:0.1, 1,3-dicarboxy-2,2- Di(acetoxy)propane, acetic anhydride and glacial acetic acid were placed in a three-necked flask equipped with a stirrer, a reflux condenser and a thermometer, the reaction temperature was controlled at 100°C, and the reaction time was 8 hours until the reaction liquid was clarified and the reaction was completed; the reaction was completed After that, the heating was stopped, and the product was distilled under reduced pressure, and the residue was recrystallized from chloroform, filtered, dried and weighed to obtain 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[ 5,5] Undecane, yield 97.6%.

实施例3Example 3

2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的制备方法,步骤如下:The preparation method of 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane, the steps are as follows:

(1)按照摩尔比为5:4,准备腈化剂无水K4Fe(CN)6与1,3-二溴-2,2-二(溴甲基)丙烷备用;按照转移催化剂TBAB与1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1.2准备TBAB;无配体的铜催化剂Cu(OAc)2占相转移催化剂的总质量的8%,按照溶剂水的量与铜催化剂的摩尔比为6:1取水备用;(1) According to the molar ratio of 5:4, prepare nitrilation agent anhydrous K 4 Fe(CN) 6 and 1,3-dibromo-2,2-bis(bromomethyl)propane for subsequent use; according to transfer catalyst TBAB and The molar ratio of 1,3-dibromo-2,2-bis(bromomethyl)propane is 1:1.2 to prepare TBAB; Copper catalyst Cu(OAc) without ligand accounts for 8% of the total mass of phase transfer catalyst, According to the amount of solvent water and the mol ratio of copper catalyst is 6:1 to take water for subsequent use;

将Cu(OAc)2催化剂加入到溶剂水中,搅拌至均相,再加入无水K4[Fe(CN)6]、TBAB以及1,3-二溴-2,2-二(溴甲基)丙烷,将容器密封后于160℃加热反应80min,反应结束后,使体系自然冷却至室温,用乙醚萃取产物三次,用旋转蒸发仪旋蒸乙醚,GC检测分析,并使产物1,3-二腈基-2,2-二(腈甲基)丙烷通过色谱柱纯化;Add Cu(OAc) 2 catalyst to solvent water, stir until homogeneous, then add anhydrous K 4 [Fe(CN) 6 ], TBAB and 1,3-dibromo-2,2-bis(bromomethyl) Propane, seal the container and heat the reaction at 160°C for 80 minutes. After the reaction, let the system cool down to room temperature naturally, extract the product with ether three times, use a rotary evaporator to rotate the ether, GC detection and analysis, and make the product 1,3-di Nitrile-2,2-two (nitrile methyl) propane is purified by chromatographic column;

(2)在氮气氛围下,于室温向装有搅拌器的反应器中,加入所需水总体积的2/3(所需水的总量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1.7);随后倾倒98%H2SO4,硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷摩尔比1.3:1,,使反应体系温度升高至120℃,然后在1h内引入上述步骤所制备得1,3-二腈基-2,2-二(腈甲基)丙烷,反应体系温度控制在120℃,随后在此温度下保温30min后,在10min内加入所需水总体积余下的1/3,并将温度升高到130℃保持6h,反应结束后停止搅拌,反应介质分层,使之自然冷却至90℃,将上层与下层水相分离,得到1,3-二羧基-2.2-二(乙酸基)丙烷。经过蒸馏、萃取、重结晶,产率为91.6%。(2) Under a nitrogen atmosphere, add 2/3 of the total volume of required water to a reactor equipped with a stirrer at room temperature (the total amount of required water and 1,3-dinitrile-2,2- The molar ratio of bis(nitrile methyl)propane is 1:1.7); then pour 98% H 2 SO 4 , the molar ratio of sulfuric acid to 1,3-dicyano-2,2-bis(nitrile methyl)propane is 1.3: 1. Raise the temperature of the reaction system to 120°C, and then introduce the 1,3-dicyano-2,2-bis(nitrile methyl)propane prepared in the above steps within 1 hour, and control the temperature of the reaction system at 120°C , and then kept at this temperature for 30 minutes, added the remaining 1/3 of the total volume of water required within 10 minutes, and raised the temperature to 130°C for 6 hours, stopped stirring after the reaction, and separated the reaction medium to make it naturally After cooling to 90°C, the upper layer and the lower layer were separated to obtain 1,3-dicarboxy-2.2-di(acetoxy)propane. After distillation, extraction and recrystallization, the yield is 91.6%.

(3)按照1,3-二羧基-2,2-二(乙酸基)丙烷、乙酸酐和催化剂冰乙酸的摩尔比为1:1.5:0.12,将1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐及冰乙酸置于带有搅拌器、回流冷凝管和温度计的三口烧瓶中,反应温度控制在110℃,反应时间为6h,至反应液澄清反应结束;反应结束后停止加热,将产物经减压蒸馏后,残余物经三氯甲烷重结晶,抽滤干燥称重,即得2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷,产率98.5%。(3) According to the molar ratio of 1,3-dicarboxy-2,2-di(acetoxy)propane, acetic anhydride and catalyst glacial acetic acid as 1:1.5:0.12, 1,3-dicarboxy-2,2- Di(acetoxy)propane, acetic anhydride and glacial acetic acid were placed in a three-necked flask equipped with a stirrer, a reflux condenser and a thermometer, the reaction temperature was controlled at 110°C, and the reaction time was 6 hours until the reaction liquid was clarified and the reaction was completed; the reaction was completed After that, the heating was stopped, and the product was distilled under reduced pressure, and the residue was recrystallized from chloroform, filtered, dried and weighed to obtain 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[ 5,5] Undecane, yield 98.5%.

应用例:Application example:

该新型螺环化合物-螺环四甲酸二酐(2,4,8,10-四羰基-3,9-二氧杂螺环[5.5]十一烷)是一种新型的用于环氧树脂体系的膨胀固化剂,主要应用于环氧树脂浇注及其纤维增强复合材料领域,用以降低环氧树脂及其复合材料在固化过程中的体积收缩率,该环氧树脂体系体积收缩率降低至0~0.5%。The novel spiro compound-spiro tetracarboxylic dianhydride (2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5.5]undecane) is a new type of epoxy resin The expansion curing agent of the system is mainly used in the field of epoxy resin casting and fiber reinforced composite materials to reduce the volume shrinkage of epoxy resin and its composite materials during the curing process. The volume shrinkage of the epoxy resin system is reduced to 0~0.5%.

应用方法如下:按重量份数计,E51环氧树脂100份;螺环四甲酸二酐33份,混合均匀、浇注、排泡,加热至150℃固化4h;170℃后固化2h;190℃后固化2h;210℃后固化2h,采用膨胀计跟踪测量反应体系的体积变化,测定环氧树脂在固化过程中的体积收缩率低于0.5%。The application method is as follows: in parts by weight, 100 parts of E51 epoxy resin; 33 parts of spirocyclotetracarboxylic dianhydride, mix evenly, pour, defoam, heat to 150°C for 4 hours; 170°C for 2 hours; 190°C for 2 hours Curing for 2 hours; curing at 210°C for 2 hours, using a dilatometer to track and measure the volume change of the reaction system, and determine that the volume shrinkage of the epoxy resin during the curing process is less than 0.5%.

Claims (8)

1.螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于它分为三步:1. The synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane is characterized in that it is divided into three steps: (1)由多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷以水为溶剂,在腈化剂的作用下,由相转移催化剂和无配体的铜催化剂催化合成1,3-二腈基-2,2-二(腈甲基)丙烷;(1) By polyhalogenated hydrocarbon 1,3-dibromo-2,2-di(bromomethyl)propane with water as solvent, under the action of nitrilation agent, by phase transfer catalyst and ligand-free copper catalyst Catalytic synthesis of 1,3-dicyano-2,2-bis(nitrile methyl)propane; (2)1,3-二腈基-2,2-二(腈甲基)丙烷在无机强酸作用下水解得到1,3-二羧基-2.2-二(乙酸基)丙烷;(2) 1,3-dicarboxy-2,2-bis(nitrile methyl)propane is hydrolyzed under the action of strong inorganic acid to obtain 1,3-dicarboxy-2.2-bis(acetoxy)propane; (3)由1,3-二羧基-2,2-二(乙酸基)丙烷与乙酸酐在催化剂作用下发生交换反应生成对称产物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷;(3) The exchange reaction of 1,3-dicarboxy-2,2-di(acetoxy)propane and acetic anhydride under the action of a catalyst produces the symmetrical product 2,4,8,10-tetracarbonyl-3,9-di Oxaspiro[5,5]undecane; 其中,所述相转移催化剂为四丁基溴化铵,无配体的铜催化剂为Cu(OAc)2;所述腈化剂为无水K4Fe(CN)6;所述无机强酸为98%浓硫酸;所述步骤(3)的催化剂为冰醋酸。Wherein, the phase transfer catalyst is tetrabutylammonium bromide, the copper catalyst without ligand is Cu(OAc) 2 ; the nitrilation agent is anhydrous K 4 Fe(CN) 6 ; the inorganic strong acid is 98 % concentrated sulfuric acid; the catalyzer of described step (3) is glacial acetic acid. 2.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于所述溶剂水与无配体的铜催化剂的摩尔比为5:1~7:1。2. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that said solvent The molar ratio of water to ligand-free copper catalyst is 5:1-7:1. 3.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于所述腈化剂为无水K4Fe(CN)6,无水K4Fe(CN)6与多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为3:2~5:4。3. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that said nitrile The oxidizing agent is anhydrous K 4 Fe(CN) 6 , and the molar ratio of anhydrous K 4 Fe(CN) 6 to polyhalogenated hydrocarbon 1,3-dibromo-2,2-bis(bromomethyl)propane is 3 :2~5:4. 4.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于所述相转移催化剂四丁基溴化铵与多卤代烃1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1~1:1.5,无配体的铜催化剂Cu(OAc)2占相转移催化剂总质量的8%~10%。4. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that the phase The molar ratio of transfer catalyst tetrabutylammonium bromide to polyhalogenated hydrocarbon 1,3-dibromo-2,2-di(bromomethyl)propane is 1:1~1:1.5, and the ligand-free copper catalyst Cu (OAc) 2 accounts for 8%-10% of the total mass of the phase transfer catalyst. 5.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于所述步骤(1)反应温度160℃~200℃,反应时间50~80min。5. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that said step (1) The reaction temperature is 160°C-200°C, and the reaction time is 50-80min. 6.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于所述水解反应步骤通过在无机强酸存在下,1,3-二腈基-2,2-二(腈甲基)丙烷与水反应,所述水解反应水的用量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1.5~1:2.0;所述无机强酸为98%浓硫酸,浓硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1~1.5:1。6. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that the hydrolysis The reaction step is to react 1,3-dicyano-2,2-bis(nitrile methyl)propane with water in the presence of a strong inorganic acid, and the amount of the hydrolysis reaction water is equal to that of 1,3-dicyano-2, The molar ratio of 2-bis(nitrile methyl)propane is 1:1.5~1:2.0; the strong inorganic acid is 98% concentrated sulfuric acid, concentrated sulfuric acid and 1,3-dicyano-2,2-bis(nitrile base) The molar ratio of propane is 1:1~1.5:1. 7.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于所述步骤(3)的催化剂为冰醋酸,所述催化剂为反应物1,3-二羧基-2,2-二(乙酸基)丙烷投料摩尔量的0.1~0.15倍;所述步骤(3)中1,3-二羧基-2,2-二(乙酸基)丙烷与乙酸酐的摩尔投料比为1:1.5~2.1;所述步骤(3)中反应温度为90~110℃,反应时间为6~12h。7. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that said step The catalyst in (3) is glacial acetic acid, and the catalyst is 0.1 to 0.15 times the molar weight of the reactant 1,3-dicarboxy-2,2-bis(acetoxy)propane; in the step (3), 1, The molar ratio of 3-dicarboxy-2,2-bis(acetoxy)propane to acetic anhydride is 1:1.5-2.1; the reaction temperature in the step (3) is 90-110°C, and the reaction time is 6-12h . 8.根据权利要求1所述的螺环化合物2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷的合成方法,其特征在于具体步骤如下:8. the synthetic method of spiro compound 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane according to claim 1, is characterized in that concrete steps are as follows : (1)按照摩尔比为3:2~5:4,准备腈化剂无水K4Fe(CN)6与1,3-二溴-2,2-二(溴甲基)丙烷备用;按照转移催化剂四丁基溴化铵与1,3-二溴-2,2-二(溴甲基)丙烷的摩尔比为1:1~1:1.5准备TBAB;无配体的铜催化剂Cu(OAc)2占相转移催化剂的总质量的8%~10%;按照溶剂水的量与铜催化剂的摩尔比为5:1~7:1取水备用;(1) According to the molar ratio of 3:2 to 5:4, prepare the anhydrous K 4 Fe(CN) 6 and 1,3-dibromo-2,2-bis(bromomethyl)propane as the nitrilation agent for later use; The molar ratio of transfer catalyst tetrabutylammonium bromide to 1,3-dibromo-2,2-di(bromomethyl)propane is 1:1~1:1.5 to prepare TBAB; ligand-free copper catalyst Cu(OAc ) 2 accounts for 8% to 10% of the total mass of the phase transfer catalyst; according to the molar ratio of the amount of solvent water to the copper catalyst being 5:1 to 7:1, water is taken for later use; 将Cu(OAc)2催化剂加入到溶剂水中,搅拌至均相,再加入无水K4[Fe(CN)6]、四丁基溴化铵以及1,3-二溴-2,2-二(溴甲基)丙烷,将容器密封后于160℃~200℃加热反应50min~80min,反应结束后,使体系自然冷却至室温,用乙醚萃取产物三次,用旋转蒸发仪旋蒸乙醚,GC检测分析,并使产物1,3-二腈基-2,2-二(腈甲基)丙烷通过色谱柱纯化;Add Cu(OAc) 2 catalyst to solvent water, stir until homogeneous, then add anhydrous K 4 [Fe(CN) 6 ], tetrabutylammonium bromide and 1,3-dibromo-2,2-di (Bromomethyl)propane, seal the container and heat the reaction at 160°C to 200°C for 50min to 80min. After the reaction, let the system cool down to room temperature naturally, extract the product with ether three times, and use a rotary evaporator to spin distill the ether and detect it by GC. Analysis, and make product 1,3-dicyano-2,2-bis(nitrile methyl) propane pass through chromatographic column purification; (2)在氮气氛围下,于室温向装有搅拌器的反应器中,加入所需水总体积的2/3,所需水的总量与1,3-二腈基-2,2-二(腈甲基)丙烷的摩尔比为1:1.5~1:2.0;随后倾倒98%H2SO4,硫酸与1,3-二腈基-2,2-二(腈甲基)丙烷摩尔比1:1~1.5:1,使反应体系温度升高至120℃,然后在1h内引入上述步骤所制备得1,3-二腈基-2,2-二(腈甲基)丙烷,反应体系温度控制在120℃,随后在此温度下保温20~40min后,在10min内加入所需水总体积余下的1/3,并将温度升高到130℃保持6h,反应结束后停止搅拌,反应介质分层,使之自然冷却至90℃,将上层与下层水相分离,得到1,3-二羧基-2.2-二(乙酸基)丙烷;(2) Under a nitrogen atmosphere, add 2/3 of the total volume of water required to the reactor equipped with a stirrer at room temperature, the total volume of water required and 1,3-dinitrile-2,2- The molar ratio of bis(nitrile methyl)propane is 1:1.5~1:2.0; then pour 98% H 2 SO 4 , sulfuric acid and 1,3-dicyano-2,2-bis(nitrile methyl)propane Ratio 1:1~1.5:1, raise the temperature of the reaction system to 120°C, and then introduce the 1,3-dicyano-2,2-bis(nitrile methyl)propane prepared in the above steps within 1h, and react The temperature of the system is controlled at 120°C, and then kept at this temperature for 20 to 40 minutes, then add the remaining 1/3 of the total volume of water required within 10 minutes, and raise the temperature to 130°C for 6 hours, and stop stirring after the reaction is completed. The reaction medium was separated into layers, allowed to cool naturally to 90°C, and the upper layer and the lower layer were separated to obtain 1,3-dicarboxy-2.2-bis(acetoxy)propane; (3)按照1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐的摩尔投料比为1:1.5~2.1,催化剂冰乙酸为1,3-二羧基-2,2-二(乙酸基)丙烷投料摩尔量的0.1~0.15倍,将1,3-二羧基-2,2-二(乙酸基)丙烷和乙酸酐及冰乙酸置于带有搅拌器、回流冷凝管和温度计的三口烧瓶中,反应温度控制在90~110℃,反应时间为6~12h,至反应液澄清反应结束;反应结束后停止加热,将产物经减压蒸馏后,残余物经三氯甲烷重结晶,抽滤干燥称重,即得2,4,8,10-四羰基-3,9-二氧杂螺环[5,5]十一烷。(3) According to the molar feed ratio of 1,3-dicarboxy-2,2-di(acetoxy)propane and acetic anhydride is 1:1.5~2.1, the catalyst glacial acetic acid is 1,3-dicarboxy-2,2- 0.1 to 0.15 times the molar amount of bis(acetoxy)propane, put 1,3-dicarboxy-2,2-bis(acetoxy)propane, acetic anhydride and glacial acetic acid in a place with agitator, reflux condenser and In the three-necked flask with a thermometer, the reaction temperature is controlled at 90-110°C, and the reaction time is 6-12 hours until the reaction liquid is clarified and the reaction is completed; stop heating after the reaction is completed, and the product is distilled under reduced pressure, and the residue is reconstituted with chloroform. Crystallize, filter, dry and weigh to obtain 2,4,8,10-tetracarbonyl-3,9-dioxaspiro[5,5]undecane.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110534627A (en) * 2018-05-23 2019-12-03 青岛海信电器股份有限公司 A kind of LED lamp panel, preparation method and display device

Families Citing this family (5)

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CN103333322B (en) * 2013-08-09 2016-02-24 武汉工程大学 A kind of spirocyclic compound is at the application method of epoxy-resin systems
CN103965589B (en) * 2014-05-14 2016-08-31 武汉理工大学 A kind of piezo-electric damping polymer vibration isolation pad and preparation method thereof
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007133561A2 (en) * 2006-05-08 2007-11-22 Neurogen Corporation Substituted azaspiro derivatives
CN101255161A (en) * 2007-02-28 2008-09-03 上海药明康德新药开发有限公司 Method for synthesizing 3,9-diaza-2,4-dioxo-spiro[5.5] undecane template compounds
CN102372649A (en) * 2010-08-19 2012-03-14 Jnc株式会社 Diamine, liquid crystal alignment agent, liquid crystal alignment film and liquid crystal display component

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007133561A2 (en) * 2006-05-08 2007-11-22 Neurogen Corporation Substituted azaspiro derivatives
CN101255161A (en) * 2007-02-28 2008-09-03 上海药明康德新药开发有限公司 Method for synthesizing 3,9-diaza-2,4-dioxo-spiro[5.5] undecane template compounds
CN102372649A (en) * 2010-08-19 2012-03-14 Jnc株式会社 Diamine, liquid crystal alignment agent, liquid crystal alignment film and liquid crystal display component

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110534627A (en) * 2018-05-23 2019-12-03 青岛海信电器股份有限公司 A kind of LED lamp panel, preparation method and display device

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