Density functional theory study on mechanisms of epoxy‐phenol curing reaction

A comprehensive picture on the mechanism of the epoxy‐phenol curing reactions is presented using the density functional theory B3LYP/ 6‐31G(d,p) and simplified physical molecular models to examine all possible reaction pathways. Phenol can act as its own promoter by using an addition phenol molecule to stabilize the transition states, and thus lower the rate‐limiting barriers by 27.0–48.9 kJ/mol. In the uncatalyzed reaction, an epoxy ring is opened by a phenol with an apparent barrier of about 129.6 kJ/mol. In catalyzed reaction, catalysts facilitate the epoxy ring opening prior to curing that lowers the apparent barriers by 48.9–50.6 kJ/mol. However, this can be competed in highly basic catalysts such as amine‐based catalysts, where catalysts are trapped in forms of hydrogen‐bonded complex with phenol. Our theoretical results predict the activation energy in the range of 79.0–80.7 kJ/mol in phosphine‐based catalyzed reactions, which agrees well with the reported experimental range of 54–86 kJ/mol. © 2014 Wiley Periodicals, Inc.     

Investigation of curing kinetics of various cycloaliphatic epoxy resins using dynamic thermal analysis

Curing reactions of three cycloaliphatic epoxy resins with methyltetrahydrophthalic anhydride (MTHPA) was investigated by differential scanning calorimetry at different heating rates. Activation energy was calculated based on Kissinger method and varied in the range of 67-72 kJ/mol depending on sample. The curing kinetic behavior was well described by Sestak-Berggren (SB) model and the order of the curing reaction is observed to be from 0.02 to 2.11 according to sample.     

Theoretical study of mechanism of cycloaddition reaction between dimethylmethylenesilylene and formaldehyde

The mechanism of cycloaddition reaction between singlet dimethylmethylenesilylene and formaldehyde has been investigated with MP2/6‐31G* method, including geometry optimization and vibrational analysis for the involved stationary points on the potential energy surface. The energies of different conformations are calculated by CCSD(T)//MP2/6‐31G* method. From the potential energy surface, it can be considered in thermodynamics and dynamics that reaction (1) and reaction (4) are the two dominant competitive reaction channels of cycloaddition reaction between dimethylmethylenesilylene and formaldehyde. The reaction process of reaction (1) is that: the two reactants (R1, R2) first form intermediates INT1a and INT1b through two reaction paths, a and b, which are barrier‐free exothermic reactions of 31.8 and 43.9 kJ/mol; then, INT1a and INT1b isomerize to a four‐membered ring product P1 via transition states TS1a and TS1b, with energy barriers of 26.3 and 24.4 kJ/mol. Reaction (4) also has two reaction paths, a and b, each of which consists of three steps are as follows: (i) the two reactants (R1, R2) first form intermediates INT3a and INT3b, which are barrier‐free exothermic reactions of 64.5 and 44.2 kJ/mol. (ii) INT3a and INT3b further react with formaldehyde (R2) to form intermediates INT4a and INT4b, through barrier‐free exothermic reactions of 22.9 and 22.2 kJ/mol. (iii) INT4a and INT4b then isomerize to form silapolycyclic product P4 via transition states TS4a and TS4b, with energy barriers of 39.7 and 29.3 kJ/mol. © 2008 Wiley Periodicals, Inc. Int J Quantum Chem, 2008     

双酚A型环氧磺酸酯的合成与表征

用双酚A型环氧树脂(E-51)和2-丙烯酰胺基-2-甲基丙磺酸(AMPS)合成了可用于紫外光固化的双酚A型环氧磺酸酯(AMPS-EP).研究了影响反应的多种因素,优化的合成条件为:以N,N-二甲基甲酰胺(DMF)为溶剂,AMPS与E-51的摩尔投料比为1:0.5,对苯二酚为阻聚剂,用量为环氧树脂质量的0.2％,反应时间...     

松香改性酚醛环氧树脂的固化反应动力学研究

以自制的松香改性酚醛环氧树脂（RPAE）为对象,采用差示扫描量热法研究了其与4,4．二氨基二苯砜组成的体系（RPAE／DDS）的固化动力学,利用Kissinger方程计算得到体系的固化热约为109．29J／g,表观活化能为51．56kJ／mol,该体系反应级数为0．85,近似为1级反应,反应速率常数为2．69×10^4／s。采用Ozawa-Flynn-Wall方程分析,得到体系的表观活化能为70。1kJ／mol。     

Ab initio Study of Mechanism of Forming Germanic Hetero-Polycyclic Compound between Germylene Carbene (H2Ge=C: ) and Formaldehyde

The mechanism of the cycloaddition reaction of forming germanic hetero‐polycyclic compound between singlet germylene carbene and formaldehyde has been investigated with MP2/6‐31G* method, including geometry optimization and vibrational analysis for the involved stationary points on the potential energy surface. The energies of the different conformations are calculated by CCSD (T)//MP2/6‐31G* method. From the potential energy profile, we predict that the cycloaddition reaction of forming germanic hetero‐polycyclic compound between singlet germylene carbene and formaldehyde has two competitive dominant reaction pathways. First dominant reaction pathway consists of four steps: (1) the two reactants (R1, R2) first form an intermediate (INT1) through a barrier‐free exothermic reaction of 117.5 kJ/mol; (2) intermediate (INT1) then isomerizes to a four‐membered ring compound (P2) via a transition state (TS2) with an energy barrier of 25.4 kJ/mol; (3) four‐membered ring compound (P2) further reacts with formaldehyde (R2) to form an intermediate (INT3), which is also a barrier‐free exothermic reaction of 19.6 kJ/mol; (4) intermediate (INT3) isomerizes to a germanic bis‐heterocyclic product (P3) via a transition state (TS3) with an energy barrier of 5.8 kJ/mol. Second dominant reaction pathway is as follows: (1) the two reactants (R1, R2) first form an intermediate (INT4) through a barrier‐free exothermic reaction of 197.3 kJ/mol; (2) intermediate (INT4) further reacts with formaldehyde (R2) to form an intermediate (INT5), which is also a barrier‐free exothermic reaction of 141.3 kJ/mol; (3) intermediate (INT5) then isomerizes to a germanic bis‐heterocyclic product (P5) via a transition state (TS5) with an energy barrier of 36.7 kJ/mol.     

聚酯型扩链脲改性环氧树脂E-51/DDS体系反应活性研究

提高二氨基二苯砜(DDS)固化环氧树脂体系的反应活性,降低反应温度、提高反应速率,具有重要的研究意义和实用价值.本研究以聚酯(PEGA1000,2000,PNGA1000,2000)、甲苯-2,4-二异氰酸酯(TDI)、二甲胺为原料合成了含有聚酯型柔性间隔基的扩链脲U-PEGA1000,2000,U-PNGA1000,2000,用其改性环氧树脂E-51/DDS体系,采用DSC系统考察了改性体系的固化反应活性.结果表明,改性体系固化反应活性明显提高,固化反应表现活化能降低,固化反应峰顶温度从230℃降至170℃,固化反应的表观活化能由67.74kJ/mol降至47.80kJ/mol.     

Curing and Glass Transition of Epoxy Resins from Ester-Carboxylic Acid Derivatives of Mono- and Disaccharides,and Alcoholysis Lignin

Mono- and disaccharides (SAC) such as glucose (Glc), fructose (Frc) and sucrose (Suc), and also alcoholysis lignin (AL) were dissolved in ethylene glycol and each of the obtained mixtures was reacted with succinic anhydride to form a mixture of ester-carboxylic acid derivatives such as SAC-polyacid, SACPA, and AL-polyacid, ALPA. Ethylene glycol-polyacid (EGPA) was also prepared from ethylene glycol. Each of the obtained mixtures of ester carboxylic acid derivatives was reacted with ethylene glycol diglycidyl ether in the presence of a catalytic amount of dimethylbenzylamine to form ester-epoxy resins. The molar ratios of epoxy groups to carboxylic acid groups ([EPOXY]/[ACID] ratios, mol mol⁻¹) was maintained at 1.0. The contents of SACPA and ALPA in the mixtures of SACPA/EGPA, and ALPA/EGPA, respectively, were also varied from 0 to 100 %. The curing reaction of SucPA and ALPA was studied by differential scanning calorimetry (DSC). Activation energy of the curing reaction for the SucPA system was 80.5 kJ/mol. Thermal properties of epoxy resins were studied by DSC. Glass transition temperatures (T_g) decreased with increasing numbers of repeating units in ester chains between cross-linking points, suggesting that ester chain lengths between cross-linking points mainly affect the mobility of ester chains in epoxy resin networks.     

HZSM-5催化甲苯和甲醇烷基化反应机理的密度泛函理论研究

对二甲苯(PX)是重要的有机化工原料,主要用于生产对苯二甲酸(PTA)和对苯二甲酸二甲酯(DMT), PTA和 DMT可经缩聚生产化纤、合成树脂和塑料等聚酯产品. PX主要通过甲苯歧化、二甲苯异构化或甲苯与 C9芳烃烷基转移等方式生产.由于三种二甲苯和乙苯的沸点接近,需要经过吸附分离或深冷分离才能得到高纯度的 PX,传统工艺物料循环量大,设备庞大,操作费用高.而通过甲苯和甲醇烷基化反应直接高选择性生成 PX,可大大降低成本,具有非常高的经济效益和研究价值.自1970年代以来,国内外众多科研院所对甲苯和甲醇烷基化催化剂进行了广泛研究,但催化剂选择性和稳定性仍需进一步提高.为了加深对甲苯和甲醇烷基化反应的认识,指导催化剂开发,有必要对甲苯和甲醇烷基化生成二甲苯的反应机理进行深入研究.当前甲苯和甲醇烷基化机理研究主要存在以下问题：(1)计算得到的能量多为电子能,而非自由能;(2)所采用的模型多为团簇模型,使用 ONIOM方法,对长程作用力描述不充分;(3)认为甲苯只有一种吸附状态;(4)没有考虑偕烷基化反应.本文采用周期性模型,通过密度泛函理论研究了 HZSM-5分子筛上甲苯和甲醇烷基化反应机理,通过计算熵得到了反应自由能,并考虑了偕烷基化反应.由于甲基的存在,在甲苯的吸附态中,甲基会伸向孔道的不同方向,因此我们认为甲苯有多种吸附态,而不同的吸附态会生成不同的二甲苯.结果表明,甲苯可以在对位、间位、邻位和偕位上通过协同机理或分步机理发生烷基化反应.在协同机理中,甲苯在对位、间位、邻位和偕位发生烷基化反应的自由能垒分别为167,138,139和183 kJ/mol.在分步机理中,甲醇脱水生成甲氧基的自由能垒为145 kJ/mol,是决速步骤;而甲苯和甲氧基对位、间位、邻位和偕位烷基化的自由能垒分别为127,105,106和114 kJ/mol.两种机理中 PX的生成能垒均比 MX和 OX高,与文献报道的结果不同.文献均认为, PX的生成能垒最低.一方面这可能是由于所采用模型的不同,本文采用周期性模型,能更充分考虑长程作用力的影响;另一方面可能是由于对甲苯吸附态的不同处理,我们认为甲苯有多种吸附态,不同的吸附态会生成不同的二甲苯,而文献均只考虑了一种甲苯吸附态.但是,在实验中, PX选择性最高.这可能是由于：(1) PX在 HZSM-5孔道的扩散速率比 MX和 OX高2–3个数量级;(2)甲苯和甲醇烷基化生成的 MX和OX迅速发生异构化反应生成 PX,异构化反应速率高于甲苯烷基化速率.两种机理中, C8H11+都是重要的中间物种,它可以反馈一个质子给分子筛骨架,生成二甲苯;也可以脱烷基生成甲烷和乙烯等气相产物.研究发现,甲烷的生成是由于 C8H11+物种中的一个 H质子从苯环上的碳原子转移到甲基上的碳原子造成的,计算得到的对位、间位和邻位 C8H11+生成甲烷的能垒分别为136,132和134 kJ/mol.由于十元环孔道的限制, HZSM-5孔道中很难通过甲苯歧化反应生成苯;偕烷基化生成的碳正离子有可能脱烷基生成乙烯和乙烷等产物,进而生成苯.碳正离子脱烷基反应生成了大量气相产物,造成反应液收降低.碳正离子脱烷基反应与甲醇制烯烃过程的烃池机理相一致,因此甲苯和甲醇烷基化反应也遵循烃池机理.     

不同温度下环氧树脂代木搪塑模具的固化过程

采用流变学的方法研究了环氧树脂代木搪塑模具在不同温度下的固化过程。 为了找到合适的测试条件,首先研究了应变和振荡频率对环氧树脂代木搪塑模具的测试结果的影响。 环氧树脂代木搪塑模具固化过程中,体系交联程度逐渐变大;在不同的固化阶段,固化程度的变化快慢不同,先缓慢增加,然后迅速增加,最后缓慢增加至平台值;储能模量和损耗模量的变化速度在不同阶段的变化与固化程度的变化相似,根据储能模量和损耗模量的最快增长速率与温度的关系得到体系的活化能约为27.2 kJ/mol;随着固化温度升高,环氧树脂代木搪塑模具固化完全所需的时间减少,同时环氧树脂的施工容留时间也相应地减少。     

Analysis of curing of diglycidyl ether of bisphenol A (BADGE n = 0) with 2‐adamantylethanamine

The epoxy resin diglycidyl ether of Bisphenol A (BADGE n = 0) has been cured with a new synthesized hardener (2‐adamantylethanamine) and the crosslinking reaction was characterized by DSC. Values of 413.3 J/g and 95°C have been obtained for the enthalpy of the reaction and the glass transition temperature, respectively. The experimental results obey Kamal's model over all conversion range of temperatures (70°C‐100°C). The activation energies of the mechanisms involved in the curing reaction have been determined for both the autocatalytic and the n‐order mechanism, the values being 63.3 and 29.8 kJ/mol, respectively. The value for T_g is 23°C higher than the one for (BADGE n = 0)/amantadine, while the activation energy for the n‐order mechanism is around 13 kJ/mol lower. This is consistent with a higher steric effect of the adamantyl group in the second hardener since it will hinder the opening the oxirane ring by the nitrogen atom of the amino group. As the polymerization reaction progress, this effect will disappear as the distance adamantyl‐oxirane increase when new oxirane groups react with the hydroxyl groups (autocatalyzed reaction). Consequently, by selecting the appropriate cross‐linking agent, it is possible to simultaneously increase T_g while reducing theactivation energy, two effects which may be desirable for some industrial applications of the material.     

Studies on curing kinetics of a novel combined liquid crystalline epoxy containing tetramethylbiphenyl and aromatic ester‐type mesogenic group with diaminodiphenylsulfone

The curing kinetics of a novel liquid crystalline epoxy resin with combining biphenyl and aromatic ester‐type mesogenic unit, diglycidyl ether of 4,4′‐bis(4‐hydroxybenzoyloxy)‐3,3′,5,5′‐tetramethyl biphenyl (DGE‐BHBTMBP), and the curing agent diaminodiphenylsulfone (DDS) was studied using the advanced isoconvensional method (AICM). DGE‐BHBTMBP/DDS curing system was investigated the curing behavior by means of differential scanning calorimetry (DSC) during isothermal and nonisothermal processes. Only one exothermal peak appeared in isothermal DSC curves. A variation of the effective activation energy with the extent of conversion was obtained by AICM. Three different curing stages were confirmed. In the initial curing stage, the value of E_a is dramatically decreased from ～90 to ～20 kJ/mol in the conversion region 0–0.2 for the formation of LC phase. In the middle stage, the value of E_a keeps about ～80 kJ/mol for cooperative effect of reaction mechanism and diffusion control. In the final stage, a significant increase of E_a from 84 to 136 kJ/mol could be caused by the mobility of longer polymer chains. © 2007 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 45: 3922–3928, 2007     

THE MECHANISM OF CURE REACTION OF 4,4''''-DIAMINODIPHENYL METHANE WITH TETRAGLYCIDYL 4,4''''-DIAMINODIPHENYL METHANE EPOXY

The cure reaction of tetraglycidyl 4,4'-diaminodiphenyl methane (TGDDM) epoxy resin with 4,4'-diaminodiphenyl methane (DDM) has been studied by using DSC. Instead of one exothermic peak, two exothermic peaks, indicative of a complex reaction mechanism, are shown in the DSC curve of TGDDM-DDM mixtures in nonisothermal cure experiments when the content of DDM is lower than stoichiometric ratio. The result of the kinetic analysis of the cure reaction shows that the activation energy of the lower temperature exotherm peak is about 56 kJ/mol and that of the higher temperature exotherm peak is about 136 kJ/mol. The lower temperature cure reaction peak can be attributed to the primary amine-epoxide and secondary amine-epoxide reactions, and the higher temperature cure reaction peak can be attributed to the epoxide-hydroxy reaction under catalysis of tertiary amine in the TGDDM epoxy resin. Because the network density of the cured epoxy resin is determined by these two reactions, the content of DDM has little effect on the glass transition temperature of cured epoxy resin.     

TBBPAER/DDM的固化反应动力学

用等温差示扫描量热法研究了4，4’-二氨基二苯甲烷固化四溴双酚-A环氧树脂的反应动力学，测定了固化反应热，得出了不同温度下固化反应速率与反应程度、固化反应程度与反应时间的关系曲线．结果表明等温固化反应按自催化反应机理进行，用Kamal方程较好地描述了不同温度下其固化反应的自催化反应过程，并反映出不同温度下扩散作用的差别，其动力学参数k1、k2、m、n由非线性回归法拟合而出，k1、k2对应的反应表现活化能分别为52．2kJ·mol-1和46．5kJ·mol-1。     

单分子水对CH_2SH+NO_2反应机理影响的理论研究

在B3LYP/6-311++G(2df,p)水平下对单分子水参与下的CH_2SH+NO_2反应的微观机理进行了研究.为了获得更准确的能量信息,采用HL复合方法和CCSD(T)/aug-ccpvtz方法进行单点能校正.结果表明,加入单分子水后的CH_2SH+NO_2反应体系,共经过10条不同的反应路径,得到6种反应产物.与裸反应(CH_2SH+NO_2)相比,水分子在反应中起到了明显的正催化作用.不仅使生成产物trans-HONO的能垒(-52.84kJ·mol~(-1))降低了176.94kJ·mol~(-1),而且不需经过复杂的重排和异构化过程便可得到产物cis-HONO.在生成产物cis-HONO通道(Path3和Path4)中,活化能垒分别为143.65和126.70kJ·mol~(-1),而其裸反应的活化能垒却高达238.34kJ·mol~(-1).生成HNO_2的通道中(Path5和Path6)活化能垒分别为295.23和-42.19kJ·mol~(-1).其中Path6的无势垒过程使HNO_2也成为该反应的主要产物.另外,单分子水还可通过氢迁移的方式直接参与CH_2SH+NO_2的反应,活化能垒(TS7-TS10)分别为-10.62,151.03,186.22和155.10kJ·mol~(-1).除直接抽氢通道中的(Path8-Path10)外,其余反应通道均为放热反应,在热力学上是可行的.     

Kinetics and mechanisms of transalkylation and disproportionation of meta‐diethylbenzene by triflic acid catalyst

The kinetics of transalkylation and isomerization of meta‐diethylbenzene in the presence of benzene using triflic acid as a catalyst has been investigated. High catalytic activity of the triflic acid catalyst was observed in homogeneous liquid‐phase reactions. On the basis of the product distribution obtained, transalkylation, disproportionation, and isomerization reactions have been considered and the main product of the reaction was ethylbenzene. These reactions are conducted in a closed liquid batch reactor with continuous stirring under dry nitrogen and atmospheric pressure over the temperature range of 288–308 K. The main transalkylation, disproportionation, and isomerization reactions occurred simultaneously and were considered as elementary reactions. The apparent activation energy of the transalkylation reaction was found to be 35.5 kJ/mol, while that of disproportionation reaction was 42.3 kJ/mol. The reproducibility of the experimental product distribution occurred with an average relative error of ±2%. © 2003 Wiley Periodicals, Inc. Int J Chem Kinet 35: 555–563, 2003     

二氯亚甲基锗烯与乙烯环加成反应机理的理论研究

The mechanism of a cycloaddition reaction between singlet dichloromethylene germylene and ethylene has been investigated with B3LYP/6-31G＊ method, including geometry optimization and vibrational analysis for the involved stationary points on the potential energy surface. Energies for the involved conformations were calculated by CCSD（T）//B3LYP/6-31G＊ method. On the basis of the surface energy profile obtained with CCSD（T）// B3LYP/6-31G＊ method for the cycloaddition reaction between singlet dichloromethylene germylene and ethylene, it can be predicted that the dominant reaction pathway is that an intermediate INT1 is firstly formed between the two reactants through a barrier-free exothermic reaction of 61.7 kJ/mol, and the intermediate INT1 then isomerizes to an active four-membered ring product P2.1 via a transition state TS2, an intermediate INT2 and a transition state TS2.1, in which energy barriers are 57.7 and 42.2 kJ/mol, respectively.     

Isothermal differential scanning calorimetry study of a glass/epoxy prepreg

Isothermal differential scanning calorimetry (DSC) was used to study the curing behavior of epoxy prepreg Hexply®1454 system, based on diglycidyl ether of bisphenol A (DEGBA)/dicyandiamid (DICY) reinforced by glass fiber. Cure kinetics of an autocatalytic‐type reaction were analyzed by general form of conversion‐dependent function. The characteristic feature of conversion‐dependent function was determined using a reduced‐plot method where the temperature‐dependent reaction rate constant was analytically separated from the isothermal data. An autocatalytic kinetic model was used; it can predict the overall kinetic behavior in the whole studied cure temperature range (115–130°C). The activation energy and pre‐exponential factor were determined as: E = 94.8 kJ/mol and A = 1.75 × 10¹⁰ sec^?1 and reaction order as 2.11 (m + n = 0.65 + 1.46 = 2.11). A kinetic model based on these values was developed by which the prediction is in good agreement with experimental values. Copyright © 2009 John Wiley & Sons, Ltd.     

等温DSC法研究树枝状大分子PAMAM与环氧树脂的固化反应动力学

聚酰胺-胺(PAMAM)树枝状大分子是近些年来在科学界引起广泛关注的一种聚合物[1~3].它具有高度规整的分子结构,形状接近球体,表面存在密集的官能团,而内部则存在大量的空腔,这些特殊结构导致了它的许多性质与线性高分子存在很大差异,从而吸引了众多的科学家投入对它特殊性能和特     

聚氨酯改性不饱和聚酯树脂的反应动力学

通过差示扫描量热法(DSC)和傅里叶红外光谱(FT-IR)分析,探讨了聚氨酯改性不饱和聚酯树脂(UPR)体系反应特征及固化反应动力学。结果表明:体系中聚氨酯网络的形成远快于UPR网络的形成。UPR和聚氨酯改性UPR体系的表观活化能分别为58.0 kJ/mol和64.8 kJ/mol,改性后体系的活化能并无较大变化;反应的级数分别为0.90和0.91。