利用FTIR光谱仪研究PU／PMMA IPN初期反应动力学

本文用FTIR光谱仪研完聚醚聚氨酯/聚甲基丙烯酸甲酯(PU/PMMA)互穿聚合物网络(IPN)的初期反应动力学.实验结果表明:该体系IPN在生成过程中动力学不同步是造成相容性较差的原因之一,提高反应温度和增加PMMA的引发剂用量有利于反应同步进行.增加PMMA的含量,使PU反应速度加快是PMMA"溶剂效应”的结果;增加PU含量,使PMMA反应速度减慢是PU的“笼壁效应”结果.聚醚聚氨酯及聚甲基丙烯酸甲酯初期反应均属一级反应动力学.     

生物质型煤在固硫剂条件下的燃烧特性研究

本文研究了生物质型煤在不同Ca/S比和不同生物质加入量下的燃烧特性,并进行了动力学分析.结果表明,固硫型煤的TG,DTG曲线变化趋势相似,都出现两个明显的失重峰挥发分析出阶段和煤焦燃烧阶段.一般在310-320℃范围内挥发分析出达到最大,在520-530℃范围内,煤焦燃烧失重速率最大.由于固硫反应的增重和型煤燃烧的失重的相对变化,导致第二个失重峰变化比较平缓,且失重温度范围较宽.不同Ca/S比的样品试验结果相比,Ca/S=2样品的最大失重点温度要比Ca/S=1.5样品的最大失重点温度要低;同一Ca/S比下,随着生物质量的增加,相应失重峰的峰值增加,最终失重百分比增加.通过动力学分析,生物质型煤在固硫剂条件下的燃烧反应服从燃烧动力学的基本方程表征的规律,对于不同的温度阶段可用不同的一级反应来描述.     

SH15树脂吸附胞二磷胆碱的热力学及动力学研究

静态条件下,研究了SH15树脂吸附水溶液中胞二磷胆碱(CDPC)的热力学和动力学特性.测定了不同温度下,热力学性质的变化.实验结果表明,SH15树脂对CDPC吸附平衡数据符合Langmmuir吸附等温方程,吸附过程为自发的物理吸附过程.考察了温度、溶液浓度、树脂粒径和搅拌速率对吸附过程的影响.运用动边界模型(MBM)描述了SH15树脂吸附CDPC的动力学过程,确定在实验条件范围内,SH15树脂吸附CDPC的吸附速度受颗粒扩散控制,并计算出吸附过程的表观活化能为9.73kJ/mol,反应级数为0.47,速率常数为0.0744,并推导出CDPC:在SH15树脂上的动力学总方程.     

Ni/PDC催化甲醇气相羰基化的动力学数学分析

研究了Ni/聚合物衍生碳(Ni/PDC)催化甲醇气相羰基化过程的动力学行为.Langmuir-Hinshelwood反应机制用于建立动力学数学模型,在此模型基础上导出反应速率的表达式以及反应速率与碘甲烷、一氧化碳和甲醇等反应物分压之间的数学关系.这些关系得到了实验数据的证实.反应速率对反应温度的依赖性以Arrhenius曲线给出,升高反应温度会导致反应控制机制从动力学控制模式转化为扩散控制模式,同时反应的有效速率表达式和表观活化能都有相应的变化.     

环氧基笼型倍半硅氧烷/4,4''-二氨基二苯砜体系的等温固化动力学

应用等温差示扫描量热法研究了4,4'-二氨基二苯砜(DDS)固化笼型倍半硅氧烷环氧树脂(POSSER)体系的反应动力学,测定了固化反应热,得出了不同温度下固化反应程度与反应时间、固化反应速率与反应时间的关系曲线,通过非线性拟合得到固化反应速率与反应程度的关系曲线.结果表明,固化反应在体系的玻璃化转变温度以上进行,等温固化反应遵从自催化反应机理,用Kamal方程可很好地描述不同温度下固化反应的自催化过程,拟合得到其反应动力学参数k1、k2、m、n,k1和k2对应的固化反应的表观活化能分别为79.67和59.84 kJ/mol.     

巯基/乙烯基硅氮烷紫外光固化的研究

利用原位红外跟踪技术和光-示差扫描量热技术研究了不同类型多官能巯基化合物与乙烯基硅氮烷的紫外光聚合动力学过程.结果表明,巯基化合物官能度越高,聚合反应速率越高,但最终转化率越低.巯基丙酸酯类化合物比烷基硫醇类化合物更易与乙烯基硅氮烷反应.在较低温度下,反应温度对聚合反应的影响较弱,反应活化能约为2.3kJ/mol,而较高反应温度下反应速率偏离Arrhenius方程.     

燃烧反应机理构建的双参数速率常数方法

采用Arrhenius方程的双参数形式描述反应的速率常数对温度的依赖关系, 解决了三参数(A, n, E)过拟合造成的复杂燃烧机理参数缺乏通用性等问题. 在不改变物种数和基元反应数条件下, 将UCSD核心机理进行双参数处理, 并应用于小分子体系的动力学模拟, 得到的模拟结果与三参数机理基本相符. 双参数机理恢复了Arrhenius活化能的物理意义, 可实现机理的参数比较和迁移, 缩小了机理整体优化的变量空间, 为燃烧机理参数的统一奠定了基础.     

热辐射通量对沥青改性PMMA燃烧特性的影响

采用本体聚合法制备沥青改性聚甲基丙烯酸甲酯(PMMA)块体,研究了热辐射通量对其热释放速率平均值、质量损失速率平均值、点燃时间、CO及CO_2产率的影响。结果表明,添加沥青的PMMA点燃后300 s内平均热释放速率由569 kW/m~2降低到了525 kW/m~2,沥青使其燃烧更加平稳;沥青改性PMMA的平均热释放速率、质量损失速率和CO产率与热辐射通量成线性递增关系;点燃时间随着辐射通量的增加而呈指数衰减趋势;CO_2产率在热辐射通量低于40 kW/m~2时基本不变,高于40 kW/m~2时呈线性递增。添加沥青之后PMMA能够平稳燃烧使其可以作为锥形量热仪标准物质候选物,得到的燃烧特性与热辐射通量的函数关系式为其不确定度评估提供了依据。     

Mn-Fe_2O_3载氧体作用下CO化学链燃烧特性及动力学研究

采用共沉淀法制备不同物质的量比Mn掺杂的铁基载氧体(Mn-Fe2O3),并进行XRD、BET和TEM表征。开展不同温度下Mn-Fe2O3与CO的化学链燃烧实验,研究载氧体的反应特性,确定较优的掺杂量和反应温度。结果表明,适量的Mn掺杂有助于改善铁基载氧体的反应活性,Fe∶Mn物质的量为50∶1时燃烧反应转化率最高。多循环化学链燃烧实验证实了载氧体稳定性较好。不同升温速率(30、40、50℃/min)下反应动力学分析表明,Mn-Fe2O3与CO的化学链燃烧还原反应均属于随机成核和随后生长的Avrami-Erofeev方程模型,并依据模型分别计算出了该模型的活化能和频率因子。     

铜离子在合金硫化镍矿浸出过程的化学动力学

建立了在常压氧化硫酸浸出合金硫化镍矿过程中通氧反应结束后铜离子浸出镍的动力学方程,反应的表观活化能为129.88 kJ.K-1.mol-1.根据该动力学方程,可以进一步对硫酸氧化浸出合金硫化镍矿过程中镍的浸出速率进行推导.     

Development of an automated digestion and droplet deposition microfluidic chip for MALDI-TOF MS

An automated proteolytic digestion bioreactor and droplet deposition system was constructed with a plastic microfluidic device for off-line interfacing to matrix assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOF MS). The microfluidic chips were fabricated in poly(methyl methacrylate) (PMMA), using a micromilling machine and incorporated a bioreactor, which was 100 microm wide, 100 microm deep, and possessed a 4 cm effective channel length (400 nL volume). The chip was operated by pressure-driven flow and mounted on a robotic fraction collector system. The PMMA bioreactor contained surface immobilized trypsin, which was covalently attached to the UV-modified PMMA surface using coupling reagents N-(3-dimethylaminopropyl)-N'-ethylcarbodiimide hydrochloride (EDC) and hydroxysulfosuccinimide (sulfo-NHS). The digested peptides were mixed with a MALDI matrix on-chip and deposited as discrete spots on MALDI targets. The bioreactor provided efficient digestion of a test protein, cytochrome c, at a flow rate of 1 microL/min, producing a reaction time of approximately 24 s to give adequate sequence coverage for protein identification. Other proteins were also evaluated using this solid-phase bioreactor. The efficiency of digestion was evaluated by monitoring the sequence coverage, which was 64%, 35%, 58%, and 47% for cytochrome c, bovine serum albumin (BSA), myoglobin, and phosphorylase b, respectively.     

PP/EVA/OMMT纳米复合材料及其阻燃材料的动态燃烧行为

利用锥形量热仪(CONE)在35kW/m2热辐照条件下,并结合极限氧指数(LOI)和UL-94垂直燃烧测试方法对聚丙烯(PP)/乙烯-醋酸乙烯酯共聚物(EVA)/有机蒙脱土(OMMT)纳米复合材料和加入无卤复配阻燃剂制备的PP/EVA/OMMT/氢氧化铝(ATH)/三氧化二锑(AO)纳米复合阻燃材料的热释放速率、烟释放及材料在燃烧时的质量损失行为进行了研究。结果表明,添加5%(质量分数)OMMT可以提高PP/EVA复合材料的阻燃性能,燃烧时的热释放速率、质量损失率以及烟释放量减少,且OMMT与无卤复配阻燃剂之间可产生阻燃协同作用,使纳米复合阻燃材料的阻燃性能、热稳定性和抑烟性进一步增强。     

聚甲基丙烯酸甲酯热氧化降解的化学动力学研究

使用质谱、热分析手段研究了PMMA热解反应.结果表明,在氮气中,PMMA-CH=CH2有两个失重阶段,分别对应于主链末端双键引发的断链和主链无规则断链反应,转折点的失重率约为26%.其中,第一阶段的失重速率受扩散过程控制,平均表观活化能E为158.5 kJ/mol, lnA为27.69;第二失重阶段为1.5级化学反应,平均表观活化能E为214.79 kJ/mol, lnA为40.46.在空气中, PMMA也有两个失重阶段,反应机理为1级化学反应,转折点处的失重率约为70%.其中在第一失重阶段平均表观活化能E为130.32 kJ/mol, lnA为24.81,在此阶段中, 过氧化基团的分解反应对PMMA的失重速率有重要影响; 在空气中第二失重阶段平均表观活化能E为 78.25 kJ/mol, lnA为13.97.     

Characteristics of steady burning over inclined polymethyl methacrylate surface in different pressure environments

This paper aims to examine the characteristics of steady burning of inclined polymethyl methacrylate (PMMA) slabs under different ambient pressures. A sequence of experiments concerning steady burning intensity and combustion efficiency of the sample were conducted under both normal pressure (Hefei: altitude 30 m, 100 kPa) and reduced pressure (Lhasa: altitude 3650 m, 64 kPa). An in situ calorimeter based on oxygen consumption method was employed to measure the heat release rate of materials. A semi-theoretical model based on convective heat feedback from the flame was proposed and fitted well with laminar-dominated flame over the inclined PMMA surface. The critical maximum side length of sample for laminar-dominated flame in Hefei is lower than Lhasa. The trend of combustion efficiency with increasing inclination angle shows a great difference under different pressure environments.

     

Poly(methyl methacrylate) Membrane: Dynamic Measurement of Concentrations During Water-Induced Phase Separation

The properties of membranes produced by nonsolvent-induced phase separation (NIPS) depend on the rate of mass transfer of mobile components. This paper reports the use of Fourier transform infrared-attenuated total reflectance (FTIR-ATR) using principle component regression (PCR) analysis to study the compositional change of polymer solution immersed into the water prior to the phase demixing. To correlate the compositional change with the macroscopic structure, the observation on the dynamics of NIPS is made by a low magnification optical microscope equipped with a video camera. The morphology of the films was also examined by scanning electron microscope. Acetone and N, N-dimethylformamide were chosen as solvents to present different behavior of poly (methyl methacrylate) (PMMA) solutions during the NIPS process. The ratio of solvent and nonsolvent exchange, flux ratio shows the mass transfer in the homogeneous polymer solution after immersion in a nonsolvent bath. The results show that the flux ratio ( ) is affected by solvents which probably affects the ultimate structures of the precipitated polymer.     

Reverse Atom Transfer Radical Polymerization of MMA in the Presence of CaCO3/SiO2 Two-Component Composite Particles

Summary: We previously discovered that structurally well-defined polymer/inorganic composite particles, i.e., poly(methyl methacrylate) (PMMA)/CaCO₃/SiO₂ three-component composite particles, can be achieved via reverse atom transfer radical polymerization (ATRP), using 2,2′-azo-bis-isobutyronitrile as initiator and Cu^II bromide as catalyst. In the present study, the influence of the mass ratio of CaCO₃/SiO₂ two-component composite particles to methyl methacrylate (MMA) on the rate and behavior of the polymerization was studied in detail. The results illustrate that increasing the mass ratio of CaCO₃/SiO₂ two-component composite particles will decrease the overall rate of polymerization of MMA under standard reverse ATRP conditions. Thermal properties of the obtained well-defined particles were characterized and determined by thermogravimetric analysis (TGA). The results indicate that well-defined PMMA chains grafted on the surface of CaCO₃/SiO₂ particles were only degraded by random chain scission of C C linkages within the PMMA chain, which is different from the degradation of PMMA chains prepared via traditional radical polymerization. This difference is reasonably ascribed to the difference between the end groups of PMMA prepared via reverse ATRP and that via traditional radical polymerization, which has been confirmed by end group analysis measured by ¹H–NMR spectroscopy.     

Thermogravimetric studies on poly(methyl methacrylate), poly(tetrahydrofuran) and their blends

TG studies are given for PMMA prepared by radical polymerization, PTHF prepared by cationic polymerization, and their blends. A procedure is proposed for determining the activation energy, frequency factor, and the order of events corresponding to the respective stages of the multistage TG curves. The order of the initial event of PMMA is not the 1st. It is shown for this discussion that the relationship between mass loss and time of the 2nd order reaction is similar to that of the depolymerization including the vaporization process at the earlier times. Some of TG curves of PTHF are not dependent on the heating rate. This independence depends on the size of sample. The order of event of PTHF, which is obtained from TG curves dependent on the heating rate, is the 0th. The event order equal to the 0th reflects major contribution of vaporization in the event. The TG behaviors shown by the procedure mentioned above for the PMMA/PTHF blends with the smaller PMMA or PTHF contents cancel those of PMMA or PTHF. This revised version was published online in July 2006 with corrections to the Cover Date.     

Gaseous and Particle‐bound VOC Products of Combustion Extracted by Needle Trap Samplers

Gaseous benzene, toluene, ethylbenzene and o‐xylene (BTEX) were extracted by using the divinylbenzene (DVB) particles (mesh sizes 60–80, 80–100 and 100–120) as sorbents packed in passive needle trap samplers (NTS). This study performed feasibility tests of these self‐designed DVB‐NTS as diffusive time‐weighted average (TWA) samplers and compared extraction efficiency with that of 100 mm polydimethylsiloxane‐solid phase microextration (PDMS‐SPME) fiber for sampling gaseous and particle‐bound volatile organic compounds (VOCs) from burning mosquito coils. Experimental results indicated that extraction rate of NTS is a reliable index in extracting VOCs. Additionally, comparisons of the NTS in extracting BTEX mass showed the NTS packed with the smallest diameters of adsorbent particles (100–120 mesh DVB) were the most effective. The mass of gaseous BTEX extracted by 100 μm PDMS‐SPME fiber were substantially lower than that extracted by DVB‐NTS of all meshes for the 30‐min TWA sampling of burning mosquito coils, and NTS packed with 100–120 mesh DVB adsorbed BTEX 50–120 ng BTEX. Particles clogging inside the packed phase of NTS inhibited VOC extraction performance after 3–5 samplings of burning particles, especially NTS packed with small‐diameter adsorbents.     

Block balance in hydrogenated polybutadiene‐b‐polymethylmethacrylate diblock copolymer for efficient interfacial activity in low‐density polyethylene/polymethylmethacrylate blend: Phase morphology development

The objective of the present study was to determine the best molecular balance between the two hydrogenated polybutadiene (HPB) and polymethylmethacrylate (PMMA) blocks that promotes an HPB‐b‐PMMA diblock copolymer with efficient compatibilization activity in a low‐density polyethylene (LDPE)/PMMA immiscible blend. The model blend selected, LDPE/PMMA, is “more immiscible” than the LDPE/polystyrene pair largely reported in open literature. The blends having a composition of 80LDPE/20PMMA exhibit a droplet‐in‐matrix phase morphology whereas in 20LDPE/80PMMA a co‐continuous phase morphology was developed. In the droplet‐in‐matrix phase morphology, the emulsifying efficiency of the copolymer was evaluated based on the maximum reduction of the PMMA droplet size it is able to promote. Whereas, in the co‐continuous phase morphology, the copolymer was evaluated based on its ability to stabilize the maximum phase co‐continuity. The sequences of the best emulsifying copolymer revealed are not symmetrical. An HPB‐b‐PMMA where the ratio of molar mass of the blocks, _HPB/ _PMMA, is within 1.8–1.95 exhibits a much better interfacial activity in LDPE/PMMA blends than a copolymer of much lower ratio (longer PMMA block). This is ascribed to the much higher interactions (cohesive energy density) encountered in PMMA (PMMA of the copolymer and PMMA phase of the blend) compared with the LDPE side (HPB of the copolymer and LDPE phase of the blend). © 2005 Wiley Periodicals, Inc. J Polym Sci Part B: Polym Phys 43: 837–848, 2005