碳酸二甲酯与苯酚酯交换合成碳酸二苯酯的热力学性质及均相催化剂

在298.15K,101.325kPa条件下,液态碳酸二甲酯(DMC)的标准Gibbs自由能和熵分别估算为-472.3kJ*mol-1和245.2J*mol-1*K-1.在298K～523K计算了由DMC和苯酚生成碳酸二苯酯(DPC)和苯甲醚反应的热力学性质(ΔrH0m,ΔrS0m,ΔrG0m和平衡常数).计算出的热力学性质表明,DMC和苯酚酯交换合成DPC反应是吸热的,并且在热力学上是不利的.研究了n-Bu2SnO, Ti(OC4H9)4, AlCl3和ZnCl2四种酯交换法合成DPC反应的催化剂,其中n-Bu2SnO具有最高的催化活性.热力学计算和实验结果均表明,合成DPC反应的最佳温度为453K.当以n-Bu2SnO为催化剂,n(苯酚)∶n(DMC)＝4∶1时,DPC的产率和选择性分别为43.0%和88.7%.     

KNO3/MCM-48催化酯交换法合成碳酸二丙酯

 对KNO3/MCM-48用于丙醇和碳酸二甲酯进行酯交换合成碳酸二丙酯的催化性能进行了考察. 用X射线衍射(XRD)、红外光谱(IR)和X射线荧光法研究了催化剂的结构特征和表面性质. XRD结果表明,随着K负载量的增加,载体特征峰强度逐渐减弱,但仍保留MCM-48的晶体结构. 随着焙烧温度的升高, KNO3逐渐分解成K2O. 分别考察了活性组分负载量、焙烧温度、焙烧时间和催化剂的用量以及反应时间对反应的影响. 结果表明, KNO3/MCM-48催化剂对碳酸二丙酯的合成具有很高的催化活性. 在反应温度363 K, 反应时间6 h, 催化剂用量5%, 丙醇与碳酸二甲酯摩尔比为4的条件下,碳酸二甲酯的转化率可达99.9%, 产物碳酸二丙酯选择性93.4%, 产率93.3%.     

碳酸乙烯酯合成碳酸二苯酯的GC-MS分析

以钛酸四丁酯催化碳酸乙烯酯与乙酸苯酯酯交换合成碳酸二苯酯(DPC)。GC-MS定性分析表明,反应液中含主产物DPC,中间体2-乙酰氧乙基苯基碳酸酯(1),副产物乙二醇二乙酸酯、乙二醇苯醚乙酸酯和苯酚。1的结构经1H NMR,13C NMR,FT-IR和EI-MS确证。     

MoO3催化碳酸二甲酯与乙酸苯酯合成碳酸二苯酯

采用焙烧法制备了MoO3催化剂并将其用于碳酸二甲酯(DMC)与乙酸苯酯(PA)合成碳酸二苯酯(DPC)反应,考察了焙烧温度对催化荆性能的影响,并用X射线衍射(XRD)对催化剂结构进行了表征.结果发现,在400或500℃焙烧的催化剂具有良好的催化性能,DMC转化率为73.9%,DPC和甲基苯基碳酸酯的选择性分别为39.5%和56.5%.XRD结果表明,该催化剂物相组成为正交晶系MoO3,且(021)或/和(110)晶面有利于酯交换反应.催化剂使用5次后DMC转化率从73.9%降至10.2%,多次重复使用后的催化剂在窄气气氛中于400或500℃焙烧即可再生,再生后催化剂的性能几乎和新鲜催化剂相当.     

Zn-Al水滑石催化碳酸二甲酯与苯酚酯交换反应的研究

用共沉淀法制备了Zn-Al水滑石,并用于多相催化酯交换合成碳酸二苯酯的反应.研究了不同n(Zn)/n(Al)比的水滑石及其焙烧产物等对酯交换反应的催化活性.结果表明,Zn-Al水滑石催化剂对该反应的催化活性和选择性很高,当n(Zn)/n(Al)=3时,在150～180℃,n(PhOH)/n(DMC)=2,催化剂用量为反应物总质量的1.5%,在反应时间为12h的条件下,DMC的转化率达到55.9%,DPC和MPC的收率分别为25.3%和27.0%,酯交换产物的选择性达到93.6%.利用XRD,TG-DTA和TEM等手段对催化剂进行了表征.     

杂原子介孔分子筛Me-HMS催化酯交换合成碳酸二苯酯

以水热合成法制备了杂原子介孔分子筛Me-HMS(Me指金属杂原子),用于催化碳酸二甲酯与苯酚酯交换合成碳酸二苯酯的反应.小角度的X射线衍射显示,所有样品均具有典型的HMS介孔结构.Me-HMS中,Ti-HMS显示最好的催化性能,其活性与骨架钛含量密切相关,当溶胶中Ti/Si比达1/30时,骨架钛趋于饱和,苯酚转化率达到最大值31.4%,酯交换选择性为99.9%.     

甲基苯基碳酸酯标准品的制备及其定量分析

利用甲基苯基碳酸酯(MPC)歧化反应的可逆性及逆反应在热力学上有利进行的特点,提出了以碳酸二甲酯 (DMC)和碳酸二苯酯 (DPC)为原料,在TiO2/SiO2催化下合成DMC与苯酚酯交换反应的中间产物MPC的新方法。反应产物经减压精馏、碱洗、水洗、干燥等精制处理,得到了纯度较高的MPC标准品。采用气相色谱-质谱法对所制备的MPC样品进行定性分析,结果表明其中还含有少量的苯酚和DPC杂质。卡尔·费休水分测定结果表明,MPC样品中的含水量为0.26%(质量分数)。使用常规气相色谱仪,采用OV-101毛细管色谱柱,以苯甲酸乙酯为内标物,对自制的MPC标准品中的微量苯酚和DPC进行定量分析,苯酚和DPC的含量分别为2.04%和1.59%（均为质量分数）。根据杂质分析结果可知自制的MPC标准品的纯度为96.11%。以此作为标准品,解决了对DMC与苯酚酯交换反应的中间产物MPC的准确定量问题。     

乙酰丙酮氧钛催化苯酚和碳酸二甲酯的酯交换反应

首次将乙酰丙酮氧钛用于苯酚和碳酸二甲酯的酯交换反应合成碳酸二苯酯,显示出较好的催化活性和很高的酯交换选择性,催化剂经180℃热处理后,苯酚转化率可达45.8%,转化数(n(苯酚)/n(Ti))为96,高于有机钛类均相催化剂.结果表明,当乙酰丙酮氧钛用量为0.2g以上,开始有副产物苯甲醚生成,酯交换选择性随催化剂用量的增加而降低.该催化剂重复使用5次后,苯酚转化率仍可达40%以上,酯交换选择性为99.9%,表现出较高的重复使用性能.     

二丁基锡磺酸酯催化酯交换合成碳酸二苯酯

研究了不同类型的酸催化剂对碳酸二甲酯与苯酚酯交换合成碳酸二苯酯的影响. 实验结果表明, 碳酸二甲酯与苯酚的酯交换反应是软碱(酚氧)亲硬酸(羰基碳)的反应; 硬Lewis酸比软Lewis酸、交界Lewis酸和Brönsted酸有更高的酯交换选择性. 将不同的磺基引入n-Bu₂SnO分子中, 制得一系列硬Lewis酸催化剂[n-Bu₂Sn(OH)OS(O)₂R(H₂O)]₂[R=p-NH₂C₆H₄(Ⅰ), p-CH₃C₆H₄(Ⅱ), C₆H₅(Ⅲ), p-ClC₆H₄(Ⅳ), Me(Ⅴ), CF₃(Ⅵ)]. 在酯交换反应中, 由于磺基的强吸电子效应增强了[n-Bu₂Sn(OH)OS(O)₂R(H₂O)]₂中Sn的Lewis酸性, 其催化活性比n-Bu₂SnO的高, 而且磺基上取代基的吸电子效应越强, 催化剂中Sn的Lewis酸性越强, 催化活性越高, 但取代基的吸电子效应过强会降低其对酯交换反应的选择性.     

TiO(acac)2催化碳酸二甲酯和苯基乙酸酯合成碳酸二苯酯

碳酸二苯酯(DPC)是非光气法生产聚碳酸酯(PCs)的重要原料,具有多种酯交换法合成路线,如碳酸二甲酯(DMC)与苯酚酯交换法、DMC与苯基乙酸酯(PA)酯交换法、草酸二甲酯(DMO)与苯酚酯交换法等.本文对比测定了几种金属乙酰丙酮配合物和有机钛化合物对碳酸二甲酯(DMC)与苯基乙酸酯(PA)酯交换合成DPC反应的催化性能,结果表明,乙酰丙酮氧钛[TiO(acac)2]是一种良好的酯交换催化剂,具有优良的催化性能.在反应条件θ=180℃,n(PA)=0.8 mol,n(DMC)/n(PA)=1/2,n(TiO(acac)2)/n(PA)=0.006,t=4 h下,DMC转化率可达74.9%,甲基苯基碳酸酯(MPC)和DPC的选择性分别可达56.9%和38.9%.探索并提出了TiO(acac)2催化DMC与PA酯交换合成DPC反应的机理.     

Magnesium Acetate Used as an Effective Catalyst for Synthesizing Aliphatic Polycarbonates via Melt Transesterification Process

High-molecular-weight aliphatic polycarbonates(APCs) were synthesized through a two-step transesterification process under solvent-free conditions. Oligomers with equal numbers of hydroxyl and phenyl carbonate terminal groups could be easily controlled by using equimolar amounts of diphenyl carbonate(DPC) and aliphatic diols as feedstocks in the first step. In the second step, the high-molecular-weight APCs can be obtained by connecting -OH with -OC(O)OC₆H₅ end-group upon removing the generated phenol at reduced pressure. Mg(OAc)₂ was found to be the best catalyst for this process among the screened catalysts, which gave the poly(1,4-butylene carbonate)(PBC) a weight-average molecular weight(M_w) of 148600 and a yield of 84.8% under its suitable reaction conditions. In addition, based on the results of X-ray diffraction(XRD), scanning electron microscopy(SEM) and fourier transform infrared spectroscopy(FTIR), a possible reaction mechanism over Mg(OAc)₂ was proposed for APCs synthesis.     

Transesterification of dimethyl carbonate with phenol over a bimetallic molybdenum and copper catalyst

Mo-Cu bimetallic oxides were found to be efficient heterogeneous catalysts for the transesterification of dimethyl carbonate (DMC) with phenol. When the reaction was carried out between 150 and 180°C, with a molar of Mo/Cu of 1:1, molar ratio of phenol/DMC of 1:1, 4.8 wt.% of the catalyst, 9 h, the conversion of phenol was 49.9%, and the total yield of MPC and DPC was 45.4%. Catalyst reuse showed a gradual decline in the catalytic activity. The decrease in catalytic activity might be due to leaching out of Mo and Cu, and/or carbon deposition.     

A New Process for Synthesis of Dimethyl Carbonate from Ethylene Carbonate and Methanol without any Catalyst under Supercritical Conditions

Dimethyl carbonate was synthesized by transesterification reaction between ethylene carbonate and methanol under supercritical conditions without any catalyst. Experimental results showed that the residence time and the molar ratio of methanol to ethylene carbonate all can affect the conversion of ethylene carbonate. When the molar ratio of methanol to ethylene carbonate was 8:1, 81.2% conversion can be achieved at 9.0 MPa and 250℃ after 8 h.     

二丁基氧化锡催化碳酸二甲酯与苯酚酯交换反应机理研究

研究了二丁基氧化锡催化碳酸二甲酯与苯酚酯交换合成碳酸二苯酯的反应机理, 发现原料苯酚和产物DPC都能与二丁基氧化锡生成同一种中间体, 并测定了其晶体结构. 该晶体属于单斜晶系, P2₁/n空间群; 晶胞参数: a＝1.3336(2) nm, b＝1.7208(2) nm, c＝1.3759(3) nm, β＝101.00(2)°; V＝3.0993(9) nm³; D_c＝1.432 g/cm³; Z＝4; F(000)＝1352; μ＝1.635 mm^－1. 分析结果显示该中间体是一种新型的二聚四烃基二锡氧烷化合物[Bu₂Sn(OPh)OSnBu₂O(Ph)]₂ (I), 该化合物具有中心对称的层状结构. MS和XPS结果证实I在酯交换反应条件下能稳定存在. 基于实验结果, 本文提出了一个合理的酯交换反应机理.     

Synthesis of polycarbonate diol catalyzed by metal-organic framework Zn_4O[CO_2-C_6H_4-CO_2]_3

The metal-organic framework Zn4O[1,4-benzenedicarboxylate]3(Zn4O[CO2-C6H4-CO2]3,commonly known as MOF-5,was prepared by the ultrasonic irradiation method.The catalyst was characterized by X-ray diffraction(XRD) and Fourier transform infrared(FTIR) spectroscopy.It was then used as the catalyst for the preparation of polycarbonate diol(PCDL) via the transesterification between diphenyl carbonate(DPC) and 1,6-hexandiol(1,6-HD).Its catalytic activity in the transesterification process is evaluated by the yield ...     

Kinetic model of transesterification of diphenyl carbonate and 1, 4-butyldiol

The transesterification of diphenyl carbonate(DPC)with 1,4-butyldiol(BD)was kinetically investigated in the presence of lithium acetate catalyst at 465K.The reaction was followed by the measurement of the quantity of phenol which was distilled from the reactor.The experiments supported the assumption that the phenyl ester groups in DPC and phenyl hdroxybutyl carbonate(PHBH)had the same reactivity,and the transesterification obeyed first-order kinetics with respect to DPC and BD,and a rate equation was derived.The reaction rate was found to be first order with respect to the catalyst concentration as well.When those data were incorporated in the rate equation,excellent agreement between calculated values and the observed ones was recognized over a wide range.     

Development and optimization of a method for analysis of the products from the transesterification of dimethyl carbonate and phenol

A high-purity sample of methyl phenyl carbonate (MPC) was obtained by developing a novel reaction route followed by a series of separation and purification procedures. Identification and quantification of the MPC sample (98.32%) was performed by a gas chromatography–mass spectrometry and Karl Fisher titration. The laboratory-prepared MPC was then used as a standard to optimize quantitative analysis of the products synthesized by transesterification of dimethyl carbonate and phenol. The advantage of the improved method was that MPC can be quantified directly rather than being calculated by subtracting the yield of diphenyl carbonate (DPC) and by-product anisole from the conversion of dimethyl carbonate (DMC). The resulting method was validated for linearity, precision, accuracy, detection limit, and quantification limit. With the improved method, simultaneous accurate quantification of DMC, MPC, DPC, phenol, and anisole in the transesterification products can be achieved. This enables evaluation of the activity and selectivity of different catalysts and control of the reaction processes.      

Sulfonate-bonded tin complexes for the production of diphenyl carbonate

Various tin complexes including dibutyltin oxide and dibutyltin diacetate were tested for their activities in the transesterification between dimethyl carbonate (DMC) and phenol to produce diphenyl carbonate (DPC). The activities of tin complexes were significantly enhanced by the co-presence of alkyl or arylsulfonic acid, possibly due to the in situ formation of sulfonate-bonded tin complexes. Highly active triflate-bonded tin species, [Bu₂Sn(OH)(OTf)]₂ and [Bu₂Sn(OAc)(OTf)]₂, were isolated from the reaction of triflic acid with dibutyltin oxide and dibutyltin diacetate, and characterized by single crystal X-ray diffraction study.     

Significant Heterogeneous Carbonate Salt Catalyzed Acetylation of Alcohols via a Transesterification Process with Carbonate Salt‐activated Alcohol 1H NMR Evidence

Heterogeneous carbonate salt catalyzed acetylation of alcohols via a transesterification process has been developed. Various esters are furnished up to 97% yield. Established procedure is simple and air‐tolerant with readily available reagents. Ethyl acetate and isobutyl acetate are used as not only acetylating agents, but also reaction solvents in transesterification. Aliphatic linear alcohols, allylic alcohols and benzyl alcohols show high reactivities in the presence of 1 or 5 mol% Cs₂CO₃ at 125°C. Cesium carbonate can be recycled by pumping liquid phase out of reactor after reaction. During four cycle runs for reaction of 2‐phenylethanol and ethyl acetate, high yields of phenethyl acetate are provided (>60% yield). Based on experiments and ¹H NMR investigation, bifunctional catalysis is proposed, alcohol activated by carbonate ion is confirmed, and higher activity of catalytic amount than stoichiometric cesium carbonate is interpreted.     

碳酸二甲酯与苯酚酯交换法反应精馏合成碳酸二苯酯的定量分析

采用OV-101毛细管色谱柱分别对碳酸二甲酯与苯酚酯交换法反应精馏塔底产物和塔顶馏分进行了定量分析。以苯甲酸乙酯为内标物,一次性同时分析了塔釜产物中各组分含量。碳酸二甲酯、碳酸二苯酯和苯甲醚与内标物的峰面积比与各标准品的质量百分比浓度呈良好的线性关系,回归方程分别为Y=48．92X＋0．69、Y=32．82X-1．75和Y=13．17X＋0．07,相关系数分别为0．9976,0．9972和0．9978;以丙酮为内标,对塔顶馏分进行了定量分析。DMC的回归方程为Y=150．57X＋0．37,相关系数为0．9985;甲醇的回归方程为Y=71.20X-0.07,相关系数为0．9996。精密度实验表明,4次平行测定结果重复性良好,各待测物的相对标准偏差都小于2．00％;准确度结果表明,各待测物真实值与测定值的相对标准偏差在0．33％～1．50％之间,该法准确可靠。