乙炔基封端聚酰亚胺增韧改性的相结构

以双酚A二醚二酐(BPADA)和3乙-炔苯胺(APA)为原料,通过两步法合成一种热固性可交联的聚酰亚胺预聚体.将此预聚体分别与不同结构的热塑性聚酰亚胺(PI)共混,对其进行增韧改性,通过调控热塑性聚酰亚胺的质量分数,引入结构相似且含有更多柔性基团的热塑性聚酰亚胺(如含有醚键和对称甲基结构的二酐),得到了热固/热塑性聚酰亚胺复合膜.利用差示扫描量热仪(DSC)及扫描电镜(SEM)对该体系的相分离结构和相容性进行研究,并讨论其机械性能和热性能.结果表明,相分离结构使体系的机械性能得到改善,同时也保持了原有的优异热性能.     

PMPS/PMAc相容性与同步互贯聚合物网络的阻尼性能研究

互贯聚合物网络是一种聚合物合金 ,其组分的热力学性质决定组分间的相容性和微相结构 ,从而影响材料的阻尼性能 .采用同步互贯聚合物网络 (SIN)技术制备了一种新型的聚苯基硅氧烷 (PMPS) 聚甲基丙烯酸酯 (PMAc)阻尼材料 ,用DMA和AFM等表征研究了其玻璃化温度转变行为与微观相态结构 .结果表明 ,由相容性好的组分制备的SIN材料阻尼值最高 ,tanδmax 可达 1 4,只有一个玻璃化温度转变峰 ,其微相结构为双相连续 ;组分介于相容与不相容之间时 ,所构成的SIN样品的tanδ≥ 0 3的温度区间最宽 ,可达 170℃ ,微相结构为单相连续 ;由相容性差的组分制得的SIN阻尼材料的内耗峰裂分为两个区间 .PMPS PMAcSIN材料的阻尼性能可以通过调节组分的相容性进行控制 .     

聚硫醚酰亚胺

全芳香的聚酰亚胺具有优良的综合性能,而其耐热性和耐热氧化性则更为突出,但是这类聚合物中的主要品种,例如由均苯四甲酸二酐与二苯醚二胺所得到的聚酰亚胺,由于没有明显的软化点而不易加工成型.为了改进聚酰亚胺的加工性能,往往在大分子主链中引入醚链.醚链的引入能够增加大分子链的柔性,改善聚合物的加工性能,同时又不致于降低聚合物的耐热性和耐热氧化性,典型的代表是由3、3′,4、4′-二苯醚四甲酸二酐及1,4-双(3′,4′-二羧基苯氧基)苯二酐分别与4,4′-二苯醚二胺所合成的可熔性聚酰亚胺.这类聚酰亚胺可以方便地模压成型,后者以邻苯二甲酸酐调节分子量后,还可以进行注射和挤塑成型.     

聚酰亚胺对高性能树脂共混体系界面的反应增强

研究了以5-降冰片烯-2,3-二羧酸单甲酯为端基的PMR型聚酰亚胺(POI)作为界面介质对部分相容的聚醚砜/聚苯硫醚(PES/PPS)、聚醚醚酮/聚醚砜(PEEK/PES)共混体系的界面性质、形态结构及结晶行为的影响.结果表明,POI可以有效地增强两相间的界面粘结,显著降低PPS/PES共混物中PPS分散区的尺寸,改善两组分间的相容性.在熔融共混过程中,POI从本体向界面扩散并同PPS,PES产生交联和/或接枝,POI同PPS的反应活性远高于PES,但POI与PES发生反应.POI是PPS结晶的有效成核剂.     

聚酰亚胺/纳米MgO复合材料的制备与性能研究

采用直接分散法将纳米MgO颗粒均匀分散在聚酰胺酸溶液中,经旋涂、热亚胺化制得聚酰亚胺/纳米MgO复合材料.利用傅里叶变换红外光谱(FTIR)、X射线衍射(XRD)、扫描电子显微镜(SEM)、紫外可见光谱(UV-Vis)、热重分析(TGA)和纳米划痕等测试技术对复合材料的结构和性能进行了表征.结果表明,平均粒径约为20 nm的纳米MgO颗粒均匀地分散在聚酰亚胺基体中,有机无机两组分相容性良好;复合材料在可见光区具有优良的光学透明性,在近紫外光区随着纳米MgO含量的增加呈现出了显著的紫外屏蔽性能;纳米MgO的加入能大幅提高复合薄膜的抗划伤性能,在100μN的划痕力下,划痕深度由纯聚酰亚胺的57.4 nm降至10 nm左右,且划痕的宽度也明显减小;尽管复合材料的热稳定性能较纯聚酰亚胺略有下降,但在300℃以下仍具有较好的热稳定性.     

用[BMIM][Cu2Cl3]离子液体萃取脱除汽油中的硫化物

以不同的IL（ionic liquid）/油质量比,采用[BMIM][Cu2Cl3]（[BMIM]=1-butyl-3-methylimidazolium）对模型汽油和商品汽油进行单步和多步萃取脱硫实验;并合成几种具有不同阴离子和阳离子结构的离子液体,评价和比较了离子液体对商品汽油的萃取脱硫性能的影响。实验结果表明,具有较好的水稳定性和常温流动性的[BMIM] [Cu2Cl3]离子液体硫容较高,在IL/油质量比为1∶3时,经多步萃取后,油品中的硫质量分数降至20×10-6～30×10-6,累计脱硫率超过95%。汽油中其他组分对脱硫效果影响很小。[BMIM][Cu2Cl3]与汽油形成稳定的两相系统,分离方便。离子液体脱硫能力可以通过四氯化碳反萃取完全恢复。     

聚醚砜与含萘环的聚芳醚酮增容共混物的研究

以双酚S型含萘环的聚芳醚酮为增容剂,研究了对聚醚砜(PES)与对苯二酚型-1,4-萘环的聚芳醚酮(1,4-NA-PAEK)共混体系的相容性及力学性能.结果表明,双酚S型含萘环的聚芳醚酮可显著降低PES/NA-PAEK共混体系中NA-PAEK分散相尺寸,改善两组分间的相容性,并且增容剂的加入使共混体系形成了双连续的互锁结构,提高了共混物的力学性能.     

固相微萃取涂层及其形貌特征研究

采用物理涂渍、溶胶-凝胶技术(sol-gel)制备了固相微萃取(SPME)固相涂层：),γ-Al2O3涂层、聚丙烯酸树脂涂层、聚酰亚胺-二氧化硅溶胶凝胶涂层、聚酰亚胺-二氧化钛涂层。通过扫描电镜显示涂层表面形貌,并比较了萃取容量与涂层形貌间的关系.证明涂层的微观形态结构对涂层性能具有一定的影响,可以通过微观形态分析,了解不同微观结构对宏观性质的影响。     

可见光响应Fe3+-聚酰亚胺网络的合成及光诱导自由基聚合

将清洁、安全的太阳能(尤其是可见光)转化为化学能以合成高分子材料,一直是光催化领域的研究热点和难点.其关键问题是发展新型光催化材料,提升其在高分子合成环境下的光催化活性及稳定性.由于共轭微孔聚合物网络的独特优点,例如光电性能易调控、比表面积高以及结构相对稳定等,在光催化领域应用日益广泛.与其它共轭微孔聚合物网络相比,聚酰亚胺网络具有更高的光稳定性和耐化学腐蚀能力;同时,可用于合成聚酰亚胺网络的单体丰富,合成方法可靠,易于从分子层面调控其光电活性,提升其光催化活性.由于以上优点,基于聚酰亚胺网络的光催化体系在光诱导合成高分子材料领域展现出良好的应用前景.然而在实际应用中,聚酰亚胺网络却面临光催化活性不足的困扰.为解决此问题,本研究组曾设计,合成了以4,4',4'-三氨基三苯胺为核的聚酰亚胺网络,利用4,4',4'-三氨基三苯胺的给电子能力,促进聚酰亚胺网络中光生电子/空穴对的分离,有效提升了聚酰亚胺网络在可见光作用下对水相中有机污染物的光降解效率.在已有工作的基础上,本文设计、合成出一种新型聚酰亚胺网络,并通过配位作用,在聚酰亚胺网络网络中引入Fe^3+离子掺杂,提升其光催化性能,在有机环境中实现可见光诱导自由基聚合.首先,以三聚氰胺为电子给体单元,以1,4,5,8-萘四甲酸二酐为电子受体单元,通过酰亚胺缩聚反应构建出含电子给体-受体交替结构的聚酰亚胺网络(MPI);然后,通过浸渍法将Fe^3+离子引入到MPI网络内,制备出Fe^3+-聚酰亚胺网络(Fe@MPI).通过傅里叶变换红外光谱,粉末X射线衍射(XRD)和X射线光电子能谱对Fe@MPI的结构进行表征.结果显示,Fe^3+主要通过配位键的形式与MPI网络结合.同时,结合XRD谱图与扫描电子显微镜和透射电子显微镜结果可见,Fe^3+并非以氧化物或其它铁盐的形式简单地沉积在聚酰亚胺网络上,而是以Fe^3+-MPI配位作用均匀分布在MPI网络内.此外,XRD及氮气吸附实验结果表明,引入Fe^3+会破坏MPI网络的有序程度,导致复合材料的结晶度下降,但并不影响其多孔结构.通过紫外漫反射光谱和光电流谱对Fe@MPI的光吸收能力和光生电子/空穴对分离能力进行表征,结果显示,MPI网络与Fe^3+配位后,其光谱响应范围可拓宽至1250 nm,而其光电流响应强度也较纯MPI提升了3.5倍,表明引入Fe^3+配位可有效促进光生电子/空穴对的分离.基于其优异的光电性能,我们以Fe@MPI为光催化剂,在30℃下实现了甲基丙烯酸甲酯的可见光诱导自由基聚合,制备出分子量可达31.3×10^4 g mol^-1的聚甲基丙烯酸甲酯.同时,与MPI和FeCl3相比,Fe@MPI在相同条件下具有更高的催化效率,与其光电性能相吻合.最后,催化剂回收、循环实验表明,Fe@MPI易于回收,且具有良好的结构和性能稳定性:四次循环实验后,其结构和光催化活性均可基本保持不变.     

用气相色谱-质谱和气相色谱-红外联用技术分析热裂解汽油C9馏分中的组成

采用气相色谱-质谱和气相色谱-红外联用技术对热裂解汽油C9馏分中的组分进行分离和定性分析。实验使用了50m聚甲基硅氧烷毛细管色谱柱,EI电离源,电离能70eV和10eV,红外光谱仪的检测器为MCT。通过分析确定了热裂解汽油C9馏分中52个化合物的结构。降低质谱的电离能有利于确定组分的分子量。质谱可以提供被测组分的裂解碎片离子和分子量的信息,红外在确定官能团和同分异构体时要优于质谱。两种联用技术的使用较好地解决了单一方法测定复杂混合物中组分结构所存在的缺陷。     

The study of thiophene adsorption onto La(III)-exchanged zeolite NaY by FT-IR spectroscopy

Zeolites NaY and LaNaY (ion-exchanged with aqueous lanthanum nitrate solution) were used as adsorbents for removing organic sulfur compounds from model gasoline solutions (without and with toluene) and fluid catalytic cracked gasoline in fixed-bed adsorption equipment at room temperature and atmosphere pressure. The adsorptive selectivity for organic sulfur compounds was significantly increased when Na(+) ions in zeolite NaY were exchanged with lanthanum ions. IR spectra of thiophene adsorption indicate that thiophene is adsorbed onto La(3+) ions via direct S-La(3+) interaction and Na(+) ions via pi-electronic interaction for La(3+)-exchanged zeolite NaY, but only via pi-electronic interaction with Na(+) ions for NaY. The amount of adsorbed thiophene on La(3+)-exchanged zeolite Y was slightly decreased by coadsorption of benzene, but greatly reduced on NaY. The adsorption of thiophene via interaction with La(3+) on La(3+)-exchanged zeolite Y is hardly replaced by benzene coadsorption. The direct S-La(3+) interaction might be the essential reason for the evidently improved adsorptive selectivity of LaNaY for removing organic sulfur compounds from solutions containing large amount of aromatics.     

吸附法脱除烷基化用汽油中的碱性氮化物

考察了磺酸树脂NKC-9、CT-175、D005-Ⅱ和LSI-600以及13X分子筛对催化裂化汽油(FCC 汽油)中碱性氮化物的脱除能力,以及对汽油中的烯烃和噻吩类硫化物的吸附影响.结果表明,以LSI-600为吸附剂时,对FCC汽油中碱性氮化物的吸附选择性最佳.在室温25℃左右、常压,剂油质量比1:35,碱性氮的脱除率达到100%所需要的吸附时间为15min,经溶剂再生,可重复使用.对这5种吸附剂,增大孔径和比表面积均有利于碱性氮化物的吸附,但当孔径足够大时,孔径和比表面积对碱性氮吸附的影响程度减弱.     

一种可溶性聚酰亚胺的合成及其渗透汽化脱有机硫化物性能测试

由3,3′,4,4′-二苯醚四甲酸二酐(ODPA)和3,3′-二甲基4,4′二氨基二苯甲烷(DMMDA)二胺为单体,利用低温溶液缩聚化学亚胺化法合成了ODPA DMMDA聚酰亚胺.利用FT IR、NMR与DSC等手段对聚酰亚胺的结构进行了表征;研究了其溶解性能、耐热性能和力学性能.结果表明,此聚酰亚胺可溶于DMF、DMAc等极性溶剂;玻璃化转变温度为264℃,其10%的热分解温度为521℃;断裂强度为137MPa;断裂伸长率为18%.采用相转化法将其制成非对称膜,采用扫描电子显微镜(SEM)观察内部结构,在渗透汽化脱硫实验中,对噻吩有良好的选择透过性能.350K时,硫富集率为3.68,渗透通量为0.92kg m2h.     

Pervaporation separation of alkane/thiophene mixtures with PDMS membrane

Worldwide concerns over environment have stimulated increasing interest both in academic and industry for deep desulfurization of gasoline. Polydimethylsiloxane (PDMS) composite membrane was used to separate the binary and multicomponent alkane/thiophene mixtures by pervaporation. Effect of carbon number and concentration of alkane, and of feed temperature, on the separation efficiency of alkane/thiophene mixtures was investigated experimentally. Experimental results of binary mixtures indicated that the total fluxes for different alkane/thiophene mixtures decrease with increase of carbon number in the alkanes. Corresponding activation energies of permeation for alkanes in PDMS membrane increase with increase of carbon number in the alkanes. Differences of molecular size and structure of the alkanes lead to various selectivities thereof within PDMS membrane. In addition, the permeability and activation energy of thiophene in various systems differ from each other due to coupling effect which should be taken into consideration when dealing with multicomponent systems. Pervaporation results of ternary systems indicated that, the increase of content of lighter alkane in feed would result in a larger total flux, but a smaller selectivity to thiophene simultaneously. A quaternary system, the mixture of n-heptane, n-octane, n-nonane and thiophene, was employed to simulate the desulfurization process of gasoline. With the membrane having a PDMS layer of 11 μm, the total flux was measured to be about 1.65 kg/m² h, with the corresponding enrichment factor of thiophene 3.9 at 30 °C.     

Pervaporation performance of crosslinked polyethylene glycol membranes for deep desulfurization of FCC gasoline

An crosslinked polyethylene glycol (PEG) membrane was prepared for fluid catalytic cracking (FCC) gasoline desulfurization. Sulfur enrichment factor come to 4.75 and 3.51 for typical FCC gasoline feed with sulfur content of 238.28 and 1227.24 μg/g, respectively. Pervaporation performance of membranes kept stable within the long time run of 500 h, which indicated that crosslinked PEG membranes had the property of resisting pollution. Judging from chromatographic analysis, the membranes were more efficient for thiophene species. Effects of operation conditions including permeate pressure, feed temperature, feed flow rate and feed sulfur content level on the pervaporation performance were investigated. Permeation flux decreased with increasing permeate pressure while increased with the operating temperature increase. Sulfur enrichment factor increased firstly and decreased then when permeate pressure and temperature rose. The peak value occurred at 10.5 mm Hg and 358 K for model compounds feed (378 K for FCC gasoline feed). Arrhenius relationship existed between flux and operating temperature. Both sulfur enrichment factor and flux were shown to increase with increasing feed flow rate. Permeation flux increased while sulfur enrichment factor decreased as the feed sulfur content increased, but the influence of increasing sulfur content on pervaporation performance weakened when sulfur content come to 600 μg/g.     

裂解汽油中噻吩硫在Co-Mo/Al2O3上的催化加氢宏观动力学

采用绝热管式固定床积分反应器，在2.5MPa~3.9MPa、513K~655K、氢/裂解汽油摩尔比1.8~3.5和裂解汽油中噻吩、单甲基噻吩和双甲基噻吩质量分数为838×10－6、137×10－6~723×10－6和192×10－6~723×10－6下，对Co-Mo/Al2O3催化剂上裂解汽油催化加氢脱硫的宏观动力学进行了研究。以Powell优化法和Merson迭代法对动力学实验数据进行非线性参数估值，建立了良好吻合实验数据的、裂解汽油催化加氢脱硫的幂函数型宏观动力学模型。噻吩、单甲基噻吩和双甲基噻吩的反应级数分别为0.721、0.735和0.87，对应的加氢反应宏观活化能依次为70.0kJ·mol－1、67.9kJ·mol－1和59.9kJ·mol－1。各噻吩基硫的转化率均随反应压力的提高而增加，3.5MPa以上时，增加的趋势减缓；反应温度的提高有利于噻吩基硫转化率的增加；593K以上时，各硫化物的转化率随温度的增加呈现线性增加的趋势。     

TS-1/H2O2催化模拟汽油中噻吩的选择氧化研究

随着环境法规的日益严格,世界各国对于燃料中硫质量分数做了新的规定,要求车用燃料的硫控制在10×10-6~50×10-6,燃料电池硫的质量分数控制为(1×10-6。要达到这样高的脱硫深度,传统的脱硫方法面临着极大的挑战[1]。因此,其他非HDS脱硫方法受到研究者关注,其中氧化萃取深度脱硫     

Sorption and transport behavior of gasoline components in polyethylene glycol membranes

Desulphurization mechanism of polyethylene glycol (PEG) membranes has been investigated by the study of solubility and diffusion behavior of typical gasoline components through PEG membranes with various crosslinking degrees. The sorption, diffusion and permeation coefficients were calculated by the systematic studies of dynamic sorption curves of gasoline components such as thiophene, n-heptane, cyclohexane, cyclohexene and toluene in PEG membranes. Furthermore, the temperature dependence of diffusion and solubility coefficients and the influence of crosslinking degree on sorption and diffusion behaviors were conducted to elucidate the mass-transfer mechanism. According to the discussions on dynamic sorption curves, transport mode, activation energy and thermodynamic parameters, thiophene species were the preferential permeation components. Crosslinking is an effective modification way to improve the overall performance of PEG membranes applied in gasoline desulphurization. The pervaporation (PV) and gas chromatography (GC) experiments results corresponded to the conclusions. All these investigations will provide helpful suggestions for the newly emerged membrane desulphurization technology and complex organic mixture separation by pervaporation.     

碱酸改性ZSM-5分子筛催化剂的噻吩烷基化反应性能研究

以SiO_2/Al_2O_3物质的量比为50的HZSM-5分子筛为原粉,经过一定浓度的NaOH溶液处理后再使用柠檬酸溶液进行酸洗以制备微孔-介孔多级孔HZSM-5催化剂,并研究其在模拟油中的噻吩烷基化反应性能。结果表明,使用柠檬酸溶液进行酸洗可以清除碱处理后孔道内残余的杂质。当柠檬酸溶液浓度为0.5 mol/L时,此时得到的HZ(AC-0.5)催化剂具有适宜的孔径和酸性,因而噻吩烷基化转化率最高,达到95.6%。在HZ(AC-0.5)催化剂上以苯并噻吩作为噻吩衍生物模型化合物,异戊二烯作为烯烃模型化合物,苯作为芳烃模型化合物,分别考察噻吩烷基化反应性能,并分析不同组分的模拟油对噻吩烷基化反应转化率和选择性的影响。结果表明,噻吩烷基化的最佳反应温度是120℃,在该温度下苯并噻吩烷基化的转化率高于噻吩烷基化的转化率,当异戊二烯作为烯烃模型化合物后噻吩的转化率会升高,当苯作为芳烃模型化合物后噻吩的转化率会降低。     

Study of Carbon Nanotube Supported Co-Mo Selective Hydrodesulphurization Catalysts for Fluid Catalytic Cracking Gasoline

In this paper, carbon nanotube supported Co-Mo catalysts for selective hydrodesulphurization （HDS） of fluid catalytic cracking （FCC） gasoline were studied, using di-isobutylene, cyclohexene, 1-octene and thiophene as model compounds to simulate FCC gasoline. The results show that the Co-Mo/CNT has very high HDS activity and HDS/hydrogenation selectivity comparing with the Co-Mo/γ-Al2O3 and Co-Mo/AC catalyst systems. The saturation ratio of cyclohexene was lower than 50%, and the saturation ratio of 1,3-di-isobutylene lower than 60% for the Co-Mo/CNT catalysts. Co/Mo atomic ratio was found to be one of the most important key factors in influencing the hydrogenation selectivity and HDS activity, and the most suitable Co/Mo atomic ratio was 0.4. Co/CNT and Mo/CNT mono-metallic catalysts showed lower HDS activity and selectivity than the Co-Mo/CNT bi-metallic catalysts.