Oxidative chemisorption of SO_2 on γ - Al_2O_3 and deposition of H_2-permselective SiO_2 films

The interaction of SO_2 with γ - Al_2O_3 and the deposition of H_2 permselective SiO_2 films have been investigated. The adsorption and oxidative adsorption of SO_2 on γ - Al_2O_3 have been examined at temperatures 500-700°C by Fourier transform infrared spectroscopy (FTIR) and thermogravimetric analysis (TGA). At temperatures above 500°C most of SO_2 adsorbed on the strong sites on alumina. The adsorbed SO_2 species was characterized by an IR band at 1065 cm^(-1). The equilibrium coverage and initial rate of adsorption decreased with temperature suggesting a two-step adsorption. When γ - Al_2O_3 was contacted with a mixture of SO_2 and O_2, adsorption of SO_2 and oxidation of the adsorbed SO_2 to a surface sulfate characterized by broad IR bands at 1070 cm^(-1), 1390 cm^(-1) took place. The results of a series of TGA experiments under different atmospheres strongly suggest that surface SO_2 and surface sulfate involve the same active sites such that SO_2 adsorption is inhibited by already formed sulfate. The results also indicate a broad range of site strengths.

The desorption of adsorbed SO_2 and the reductive desorption of oxidatively adsorbed SO_2 have been investigated by microreactor experiments and thermogravimetric analysis (TGA). Temperature programmed reduction (TPR) of adsorbed SO_2 showed that SO_2 was desorbed without significant reaction with H_2 when H_2 concentration was low while considerable reaction occurred when 100% H_2 was used. SO_2 adsorbed on the strong sites on alumina was reduced to sulfur and H_2S. The isothermal reduction experiments of oxidatively adsorbed SO_2 reveal that the rate of reduction is very slow below 550°C even with 100% H_2. The reduction product is mainly composed of SO_2. TPR experiments of oxidatively adsorbed SO_2 showed that H_2S arose from a sulfate strongly chemisorbed on the surface.

Films of amorphous SiO_2 were deposited within the walls of porous Vycor tubes by SiH_4 oxidation in an opposing reactants geometry : SiH_4 was passed inside the tube while O_2 was passed outside the tube. The two reactants diffused opposite to each other and reacted within a narrow front inside the tube wall to form a thin SiO_2 film. Once the pores were plugged the reactants could not reach each other and the reaction stopped. At 450°C and 0.1 and 0.33 atm of SiH_4 and O_2, the reaction was complete within 15 minutes. The thickness of the SiO_2 film was estimated to be about 0.1 µm. Measurements of H_2 and N_2 permeation rates showed that the SiO_2 film was highly selective to H_2 permeation. The H_2:N_2 flux at 450°C varied between 2000-3000.

Thin SiO_2 films were heat treated in different gas mixtures to determine their stability in functioning as high-temperature hydrogen-permselective membranes. The films were heat-treated at 450-700°C in dry N_2, dry O_2, N_2-H_2O, and O_2-H_2O mixtures. The permeation rates of H_2 and N_2 changed depending on the original conditions of film formation as well as on the heat treatment. Heating in dry N_2 slowly reduced the permeation rates of both H_2 and N_2. Heating in a N_2-H_2O atmosphere led to a steeper decline of H_2 permeability. But the permeation rate of N_2 increased or decreased according to whether the film deposition had been carried out in the absence or presence of H_2O vapor, respectively. Thermal treatment in O_2 caused rapid decline of the permeation rates of H_2 and N_2 in films that were deposited under dry conditions. The decline was moderate in films deposited under wet conditions.

Neural network design for switching network control

A neural network is a highly interconnected set of simple processors. The many connections allow information to travel rapidly through the network, and due to their simplicity, many processors in one network are feasible. Together these properties imply that we can build efficient massively parallel machines using neural networks. The primary problem is how do we specify the interconnections in a neural network. The various approaches developed so far such as outer product, learning algorithm, or energy function suffer from the following deficiencies: long training/ specification times; not guaranteed to work on all inputs; requires full connectivity.

Alternatively we discuss methods of using the topology and constraints of the problems themselves to design the topology and connections of the neural solution. We define several useful circuits-generalizations of the Winner-Take-All circuitthat allows us to incorporate constraints using feedback in a controlled manner. These circuits are proven to be stable, and to only converge on valid states. We use the Hopfield electronic model since this is close to an actual implementation. We also discuss methods for incorporating these circuits into larger systems, neural and nonneural. By exploiting regularities in our definition, we can construct efficient networks. To demonstrate the methods, we look to three problems from communications. We first discuss two applications to problems from circuit switching; finding routes in large multistage switches, and the call rearrangement problem. These show both, how we can use many neurons to build massively parallel machines, and how the Winner-Take-All circuits can simplify our designs.

Next we develop a solution to the contention arbitration problem of high-speed packet switches. We define a useful class of switching networks and then design a neural network to solve the contention arbitration problem for this class. Various aspects of the neural network/switch system are analyzed to measure the queueing performance of this method. Using the basic design, a feasible architecture for a large (1024-input) ATM packet switch is presented. Using the massive parallelism of neural networks, we can consider algorithms that were previously computationally unattainable. These now viable algorithms lead us to new perspectives on switch design.

Experimental and theoretical studies of the electrothermal instability in a nonequilibrium plasma

Experimental and theoretical studies have been made of the electrothermal waves occurring in a nonequilibrium MHD plasma. These waves are caused by an instability that occurs when a plasma having a dependence of conductivity on current density is subjected to crossed electric and magnetic fields. Theoretically, these waves were studied by developing and solving the equations of a steady, one-dimensional nonuniformity in electron density. From these nonlinear equations, predictions of the maximum amplitude and of the half width of steady waves could be obtained. Experimentally, the waves were studied in a nonequilibrium discharge produced in a potassium-seeded argon plasma at 2000°K and 1 atm. pressure. The behavior of such a discharge with four different configurations of electrodes was determined from photographs, photomultiplier measurements, and voltage probes. These four configurations were chosen to produce steady waves, to check the stability of steady waves, and to observe the manifestation of the waves in a MHD generator or accelerator configuration.

Steady, one-dimensional waves were found to exist in a number of situations, and where they existed, their characteristics agreed with the predictions of the steady theory. Some extensions of this theory were necessary, however, to describe the transient phenomena occurring in the inlet region of a discharge transverse to the gas flow. It was also found that in a discharge away from the stabilizing effect of the electrodes, steady waves became unstable for large Hall parameters. Methods of prediction of the effective electrical conductivity and Hall parameter of a plasma with nonuniformities caused by the electrothermal waves were also studied. Using these methods and the values of amplitude predicted by the steady theory, it was found that the measured decrease in transverse conductivity of a MHD device, 50 per cent at a Hall parameter of 5, could be accounted for in terms of the electrothermal instability.

Desarrollo de catalizadores de Co3o4 nanocristalinos para la oxidación de compuestos clorados

La contaminación atmosférica se presenta como uno de los problemas más importantes de las últimas décadas. Los efectos negativos de esta problemática son de carácter tanto global como local y ha n desencadenado una serie de daños que afectan al medio ambiente y a la salud de los seres vivos, entre ellos los seres humanos. El origen de la contaminación atmosféri ca se sitúa en los procesos que se derivan del aumento de la población, del desarrollo industrial, de la urbanización y del transporte. En la actualidad las industrias emplean una gran cantidad de sustancias químicas que son nocivas para el me dio ambiente. E ntre ellas destacan los compuestos orgánicos volátile s (COV) , los cuales se emiten a la atmó sfera cada vez en mayor medida. La creciente contaminación ha supuesto la implantación de una legislación medioambiental cada vez más severa. Como consecuencia, l as compañías están estudiando varias alternativas con el fin de cumplir las restricciones y de continuar con su marcha económica. Entre las posibles soluciones destacan los procesos catalíticos, los cuales representan más del 90% de entre los métodos lleva dos a cabo para el tratamiento químico.

Estudio comparativo de tecnologías comerciales de valorización de residuos solidos urbanos

Debido al incremento en la demand a de combustibles, y al consiguiente aumento en el precio del petróleo, se plantea el uso de la biomasa como sustituto de los combustibles fósiles. La biomasa está considerada como una fuente de energía renovable y c ada vez s e está apostando más por su uso ya que contribuye a la reducción de l CO 2 de la atmó sfera. Como la biomasa proviene de fuentes naturales, se supone que todo el CO 2 que ha absorbido durante su c iclo de vida para desarrollarse es igual a la cantidad de CO 2 que se emite al utilizar la bi omasa como combustible, por lo que el ciclo de carbono es neutro. Por otro lado, la biomasa contiene un bajo contenido , casi despreciable, de sulfuros, nitrógeno y cenizas, por lo que las emisiones producidas son menores. El termino biomasa involucra toda la materia orgánica existente en la naturaleza, por lo que utilizar ésta como combustible para la obtención de electricidad es una opción muy atractiva. Ahora bien, dado que el uso masivo de la biomasa para fines energéticos puede acarrear serios problemas medioambientales, hay que tener sumo cuidado a la hora de utilizarla , como por ejemplo en las calderas de pellets. Desde el punto de vista de la contaminación obtener calor a partir de esta fuente renovable es más ecológico, pero puede llegar a originar s erios problemas de deforestación. O tro ejemplo sería el uso de cultivos energéticos para la obtención de biocombustibles. El us o de éstos supondría su escasez debido al aumento de la demanda de éstos para fines energéticos, por lo que el precio de dichos cultivos aumentaría. Por lo tanto, la solución ideal consistiría en buscar un equilibrio o el tipo de biomasa que menos repercusión tenga sobre el medio ambiente. Entre esta última opción se encuentran los residuos sólidos urbanos (RSU) . Según la ley 22/2 011, de l 28 de Julio, de residuos y suelos contaminados, l os residuos sólidos urbanos son aquellos que son generados en los hogares como consecuencia de las actividades domésticas . Debido a que aproximadamente un 60% de su composición es materia orgánica , se pueden clasificar como biomasa, por lo que s e puede decir que los residuos sólidos urbanos son un “tipo de biomasa” a los que sería interesa nte dar uso . Debido a que l os residuos constituyen un gran problema ambiental, social y económico, se requiere mayor esfuerzo para su reducción y prevención. El aumento de la calidad de vida de la población ha hecho que cada vez se generen más residuos , por lo que es necesario un si stema eficaz para la gestión de éstos

Solubility and Diffusivity of Water in Lunar Basalt, and Chemical Zonation in Olivine-Hosted Melt Inclusions

I report the solubility and diffusivity of water in lunar basalt and an iron-free basaltic analogue at 1 atm and 1350 °C. Such parameters are critical for understanding the degassing histories of lunar pyroclastic glasses. Solubility experiments have been conducted over a range of fO₂ conditions from three log units below to five log units above the iron-wüstite buffer (IW) and over a range of pH₂/pH₂O from 0.03 to 24. Quenched experimental glasses were analyzed by Fourier transform infrared spectroscopy (FTIR) and secondary ionization mass spectrometry (SIMS) and were found to contain up to ~420 ppm water. Results demonstrate that, under the conditions of our experiments: (1) hydroxyl is the only H-bearing species detected by FTIR; (2) the solubility of water is proportional to the square root of pH₂O in the furnace atmosphere and is independent of fO₂ and pH₂/pH₂O; (3) the solubility of water is very similar in both melt compositions; (4) the concentration of H₂ in our iron-free experiments is <3 ppm, even at oxygen fugacities as low as IW-2.3 and pH₂/pH₂O as high as 24; and (5) SIMS analyses of water in iron-rich glasses equilibrated under variable fO₂ conditions can be strongly influenced by matrix effects, even when the concentrations of water in the glasses are low. Our results can be used to constrain the entrapment pressure of the lunar melt inclusions of Hauri et al. (2011).

Diffusion experiments were conducted over a range of fO₂ conditions from IW-2.2 to IW+6.7 and over a range of pH₂/pH₂O from nominally zero to ~10. The water concentrations measured in our quenched experimental glasses by SIMS and FTIR vary from a few ppm to ~430 ppm. Water concentration gradients are well described by models in which the diffusivity of water (D^*_water) is assumed to be constant. The relationship between D^*_water and water concentration is well described by a modified speciation model (Ni et al. 2012) in which both molecular water and hydroxyl are allowed to diffuse. The success of this modified speciation model for describing our results suggests that we have resolved the diffusivity of hydroxyl in basaltic melt for the first time. Best-fit values of D^*_water for our experiments on lunar basalt vary within a factor of ~2 over a range of pH₂/pH₂O from 0.007 to 9.7, a range of fO₂ from IW-2.2 to IW+4.9, and a water concentration range from ~80 ppm to ~280 ppm. The relative insensitivity of our best-fit values of D^*_water to variations in pH₂ suggests that H₂ diffusion was not significant during degassing of the lunar glasses of Saal et al. (2008). D^*_water during dehydration and hydration in H₂/CO₂ gas mixtures are approximately the same, which supports an equilibrium boundary condition for these experiments. However, dehydration experiments into CO₂ and CO/CO₂ gas mixtures leave some scope for the importance of kinetics during dehydration into H-free environments. The value of D^*_water chosen by Saal et al. (2008) for modeling the diffusive degassing of the lunar volcanic glasses is within a factor of three of our measured value in our lunar basaltic melt at 1350 °C.

In Chapter 4 of this thesis, I document significant zonation in major, minor, trace, and volatile elements in naturally glassy olivine-hosted melt inclusions from the Siqueiros Fracture Zone and the Galapagos Islands. Components with a higher concentration in the host olivine than in the melt (MgO, FeO, Cr₂O₃, and MnO) are depleted at the edges of the zoned melt inclusions relative to their centers, whereas except for CaO, H₂O, and F, components with a lower concentration in the host olivine than in the melt (Al₂O₃, SiO₂, Na₂O, K₂O, TiO₂, S, and Cl) are enriched near the melt inclusion edges. This zonation is due to formation of an olivine-depleted boundary layer in the adjacent melt in response to cooling and crystallization of olivine on the walls of the melt inclusions concurrent with diffusive propagation of the boundary layer toward the inclusion center.

Concentration profiles of some components in the melt inclusions exhibit multicomponent diffusion effects such as uphill diffusion (CaO, FeO) or slowing of the diffusion of typically rapidly diffusing components (Na₂O, K₂O) by coupling to slow diffusing components such as SiO₂ and Al₂O₃. Concentrations of H2O and F decrease towards the edges of some of the Siqueiros melt inclusions, suggesting either that these components have been lost from the inclusions into the host olivine late in their cooling histories and/or that these components are exhibiting multicomponent diffusion effects.

A model has been developed of the time-dependent evolution of MgO concentration profiles in melt inclusions due to simultaneous depletion of MgO at the inclusion walls due to olivine growth and diffusion of MgO in the melt inclusions in response to this depletion. Observed concentration profiles were fit to this model to constrain their thermal histories. Cooling rates determined by a single-stage linear cooling model are 150–13,000 °C hr^-1 from the liquidus down to ~1000 °C, consistent with previously determined cooling rates for basaltic glasses; compositional trends with melt inclusion size observed in the Siqueiros melt inclusions are described well by this simple single-stage linear cooling model. Despite the overall success of the modeling of MgO concentration profiles using a single-stage cooling history, MgO concentration profiles in some melt inclusions are better fit by a two-stage cooling history with a slower-cooling first stage followed by a faster-cooling second stage; the inferred total duration of cooling from the liquidus down to ~1000 °C is 40 s to just over one hour.

Based on our observations and models, compositions of zoned melt inclusions (even if measured at the centers of the inclusions) will typically have been diffusively fractionated relative to the initially trapped melt; for such inclusions, the initial composition cannot be simply reconstructed based on olivine-addition calculations, so caution should be exercised in application of such reconstructions to correct for post-entrapment crystallization of olivine on inclusion walls. Off-center analyses of a melt inclusion can also give results significantly fractionated relative to simple olivine crystallization.

All melt inclusions from the Siqueiros and Galapagos sample suites exhibit zoning profiles, and this feature may be nearly universal in glassy, olivine-hosted inclusions. If so, zoning profiles in melt inclusions could be widely useful to constrain late-stage syneruptive processes and as natural diffusion experiments.

New measurements on the absolute cosmic ray ionization from sea level to 1540 kilometers altitude

An air filled ionization chamber has been constructed with a volume of 552 liters and a wall consisting of 12.7 mg/cm² of plastic wrapped over a rigid, lightweight aluminum frame. A calibration in absolute units, independent of previous Caltech ion chamber calibrations, was applied to a sealed Neher electrometer for use in this chamber. The new chamber was flown along with an older, argon filled, balloon type chamber in a C-135 aircraft from 1,000 to 40,000 feet altitude, and other measurements of sea level cosmic ray ionization were made, resulting in the value of 2.60 ± .03 ion pairs/cm³ sec atm) at sea level. The calibrations of the two instruments were found to agree within 1 percent, and the airplane data were consistent with previous balloon measurements in the upper atmosphere. Ionization due to radon gas in the atmosphere was investigated. Absolute ionization data in the lower atmosphere have been compared with results of other observers, and discrepancies have been discussed.

Data from a polar orbiting ion chamber on the OGO-II, IV spacecraft have been analyzed. The problem of radioactivity produced on the spacecraft during passes through high fluxes of trapped protons has been investigated, and some corrections determined. Quiet time ionization averages over the polar regions have been plotted as function of altitude, and an analytical fit is made to the data that gives a value of 10.4 ± 2.3 percent for the fractional part of the ionization at the top of the atmosphere due to splash albedo particles, although this result is shown to depend on an assumed angular distribution for the albedo particles. Comparisons with other albedo measurements are made. The data are shown to be consistent with balloon and interplanetary ionization measurements. The position of the cosmic ray knee is found to exhibit an altitude dependence, a North-South effect, and a small local time variation.

Transformação de metanol em olefinas leves catalisada por zeólitas HZSM-5

A reação de transformação de MeOH em olefinas leves foi investigada sobre zeólitas HZSM-5 com razões SiO2/Al2O3 (SAR) iguais a 30, 80 e 280. As propriedades ácidas e texturais da amostra com SAR 30 foram modificadas por impregnação com ácido fosfórico. A caracterização físico-química das amostras foi realizada empregando-se as técnicas de FRX, fisissorção de N2, DRX, DTP de NH3 e IV com adsorção de piridina. O desempenho catalítico das mesmas foi comparado tanto em condições reacionais similares (mesma T, pressão parcial de MeOH e WHSV) como em condições de isoconversão. Verificou-se, que quanto maior a SAR da zeólita, menor a densidade total e a força dos sítios ácidos presentes, sendo este efeito mais significativo para os sítios de Brönsted. O efeito do aumento da SAR favoreceu a estabilidade catalítica e a formação de olefinas leves, principalmente propeno. No caso das amostras contendo fósforo, foi observada uma redução linear na área específica BET e no volume de microporos com o aumento do teor de fósforo. Estes resultados, aliados aos obtidos por DRX, sugerem que a redução mais significativa na área específica e no volume de microporos pode ser associada à redução na cristalinidade e à formação de espécies amorfas contendo fósforo, que bloqueariam a estrutura porosa da zeólita. Não se observou alteração significativa na força dos sítios fracos, enquanto a força dos sítios fortes diminuiu significativamente. As amostras apresentando menor SAR e menor teor de fósforo foram mais ativas. Por outro lado, em condições de isoconversão de 916%, a amostra mais seletiva à formação de olefinas foi aquela com maior SAR. Dentre as amostras impregnadas, aquela contendo 4% de fósforo foi a mais seletiva a propeno, enquanto a que continha 6% foi mais seletiva a eteno. A amostra com SAR igual a 280 foi investigada variando-se a temperatura de reação (400, 500 e 540C) e a pressão parcial de metanol (0,038; 0,083 e 0,123 atm), através de um planejamento experimental do tipo Box-Benhnken (32). O rendimento otimizado em olefinas leves foi alcançado a 480C e 0,08 atm. O modelo proposto descreveu bem os dados experimentais e evidenciou a existência de uma faixa ótima de temperatura para maximização do rendimento em propeno e eteno, o qual foi também afetado pela pressão parcial de MeOH na faixa estudada. Palavras-chave: ZSM-5, olefinas, propeno, eteno, processo MTO, fósforo.

Efecto antitumoral de la terfenadina, antagonista del receptor H1 de la histamina, mediado por el complejo I mitocondrial

180 p.

Injeção de sangue autógeno no tratamento da luxação recidivante da articulação temporomandibular

A articulação temporomandibular (ATM) é uma articulação complexa com características e funções únicas. Certamente é uma das articulações mais utilizadas e seu uso inadequado e excessivo consequentemente promove inúmeros transtornos. Dentre as alterações de hipermobilidade articular, o deslocamento mandibular refere-se ao posicionamento, geralmente anterior, do côndilo mandibular sobre a eminência articular, com completa separação das superfícies articulares e consequente travamento. Quando os episódios se tornam frequentes, algum método de tratamento, seja conservador ou cirúrgico, deve ser utilizado, devido ao grande transtorno funcional e social gerados. A injeção de sangue autógeno na articulação temporomandibular é uma técnica minimamente invasiva, com escassos relatos na literatura e que foi recentemente reintroduzida. Onze pacientes diagnosticados com luxação recidivante da articulação da cabeça mandibular receberam injeções bilaterais de sangue autógeno no compartimento articular superior e região pericapsular. Em acompanhamento, que variou de 24 a 35 meses (média de 29,6 meses), 3 (27,3%) pacientes apresentaram recidivas. O mesmo protocolo de tratamento foi repetido para estes três casos, porém sem sucesso, sendo então encaminhados para procedimento cirúrgico de eminectomia. Dessa forma, dos 11 pacientes inicialmente tratados, 8 (72,7%) não apresentaram episódios de deslocamento mandibular recorrente após o procedimento proposto. Trata-se de um procedimento simples, rápido, pouco invasivo, de baixo custo e com mínima possibilidade de complicações, sendo uma alternativa de tratamento viável, antes de se indicar procedimentos cirúrgicos.

Autoignition of alcohols and ethers in a rapid compression machine

The autoignition characteristics of methanol, ethanol and MTBE (methyl tert-butyl ether) have been investigated in a rapid compression machine at pressures in the range 20-40 atm and temperatures within 750-1000 K. All three oxygenated fuels tested show higher autoignition temperatures than paraffins, a trend consistent with the high octane number of these fuels. The autoignition delay time for methanol was slightly lower than predicted values using reported reaction mechanisms. However, the experimental and measured values for the activation energy are in very good agreement around 44 kcal/mol. The measured activation energy for ethanol autoignition is in good agreement with previous shock tube results (31 kcal/mol), although ignition times predicted by the shock tube correlation are a factor of three lower than the measured values. The measured activation energy for MTBE, 41.4 kcal/mol, was significantly higher than the value previously observed in shock tubes (28.1 kcal/mol). The onset of preignition, characterized by a slow energy release prior to early ignition was observed in some instances. Possible reasons for these ocurrences are discussed. © Copyright 1993 Society of Automotive engineers, Inc.

以用户为中心的场景设计方法研究

图形用户界面(GUI)的可用性在于给用户的任务提供了有用的图形表示和操作,以使用户无须分心于那些不必要的交互和领域特征.然而,当前的GUI设计通常反映了系统的状态和操作,迫使人们学习和适应预定义的系统任务.以用户为中心的GUI设计旨在提高系统可用性,但是众多的以用户为中心的设计研究只给出一些设计准则和经验性的方法,缺乏对实际软件设计的可操作指导.基于场景的设计是GUI设计的有效方法,然而,场景本身并没给出好的实现以用户为中心设计的方法.该文在研究以用户为中心的设计和基于场景的设计的基础上,提出一种以用户为中心的场景设计方法,力图给出一种提高GUI可用性的更有效的方法.该方法的核心是:用场景描述方式来体现用户为中心的设计思想,并将其贯穿到系统开发的各个阶段,真正实现从用户的角度设计系统.最后以ATM机的界面设计为例说明使用该方法进行设计的有效性.

糠醇和糠醇与三－（2－羟乙基）－异氰尿酸酯缩聚和磺化反应及结构性能表征

本工作对糠醇（FA）和FA与三－（2－羟乙基）异氰尿酸酯（THEIC）的缩聚和磺化反应以及产物的结构和抗氧，抗氯稳定性进行了系统的研究。对FA与THEIC表面聚合制备反渗透复合膜具有十分重要的指导意义。由热分析方法研究发现，FA和FA与THEIC共缩聚反应过程在DSC谱图上有四个放热反应峰。I、II峰（50～80 ℃）为FA头－尾及头－头醚化脱水线性缩聚反应。III峰（110～130 ℃）为FA缩聚物的端羟甲基与亚甲基脱水反应。IN峰（150～190 ℃）为高温下呋喃甲醚链脱出甲醛，甲醛与亚甲基发生交联反应。催化剂用量的增加有利于羟甲基间脱水醚化反应。FA与THEIC共缩聚反应在150 ℃左右有突变，THEIC参加反应的活性增加。体系中大量硫酸存在对THEIC参加反应不利，同时引起FA缩聚物裂解反应。THEIC的加入可改善FA缩聚物的耐热氧化裂解性能。空气下使起始热失重温度提高了60 ℃；氮气下，起始热失重温度提高80 ℃。FA缩聚物的磺化反应在低温下就开始进行，140 ℃时磺化程度最高。磺化度为0.067个SO_3H／重复单元，离子交换容量（电荷密度）为0.84 meg/g酸型。FA和甲基呋喃齐聚物和其磺化后的~(13)C-NMR分析表明，磺化反应容易发生在端呋喃环与H相连的α位，β位，中间呋喃环β位也可发生磺化反应。磺化反应速度较慢，磺化程度不高。H_2SO_4与FA重量之比大于四分之一时，磺化程度基本不变，H_2SO_4量过高时对产物有裂解作用，因此选择此比例比较适宜。由液体和固体~(13)C-NMR观察到FA缩聚反应过程中，羟甲基于100 ℃基本消失，而呋喃甲醚链生成。产生交联的主要原因是甲醛与亚甲基反应进行的。甲醛也可同呋喃环端αH位和β位发生反应生成羟甲基，羟甲基可继续参加反应使缩聚物产生交联。缩聚物中有明显的端甲基酮、醛和羧酸基的生成。产生的原因如下：FA缩聚物中呋喃环间在较高温度下可发生Diels-Alder反应，裂解色谱－质谱分析检出裂解产物中有CH_3和CH_3等芳香族化合物，证实发生了Diels-Alder反应。FA和甲基呋喃齐聚物在大量硫酸作用下，室温磺化交联产物的固体~(13)C-NMR表明有呋喃环上双键打开的反应。可能为Diels-Alder反应，也可能是环双键打开交联的反应。但形成的温度和反应速度还不十分清楚。FA和FA与THEIC缩聚物经过氧化氢氧化裂解产物裂解失重较大，主链发生了断裂反应红外光谱和固体~(13)C-NMR分析表明产生了大量的酮，醛和羧酸。反应过程可能如下：FA缩聚物经游离氯作用后，有少量缩聚物被裂解掉，共缩聚物中脂肪醚被裂解，生成醇，THEIC部分被裂解掉。于是可初步确定FA缩聚物和FA与TEHIC共缩聚物链中的亚甲基和脂肪醚键是易受氧化攻击的弱点。利用表面内反射红外光谱，电子能谱和电子显微镜等对PEC－1000复合膜和试剂复合膜进行了结构与组成剖析，发现PEC－1000膜分离功能层中含有较多伯醇化合物。膜表面含有较多的O, S, N等原子，因此制复合膜的溶液中，THEIC的含量较高，膜的流动电位随压力变化的速率为-4.67mV/atm，膜功能层中含有较多的极性SO_3~-基团。

盐和有机物对氨基酸热力学性质的影响-NaCl氨基酸-葡萄糖-水体系

在278.15-318.15范围内，本文测定了以下四个无液接电池的电动势：Pt,H_2(g, 1 atm)|HCl(m)、X Mass% Glucose-H_2O|Ag-AgCl (A) Pt,H_2 (g, 1 atm)|G(m_1), HGCl (m_2), X Mass% Glucose-H_2O|Ag-AgCl (B) Pt,H_2 (g, 1 atm) |HCl (m), NaCl (M-m), X Mass% Glucose-H_2O|Ag-AgCl (C) Pt,H_2 (g, 1 atm)|G(m_1), HGCl (m_2), NaCl (M-m), X Mass% Glucose-H_2O|Ag-AgCl (D) 其中G为中性甘氨酸，NH_3CH_2COO~-, HGClm为甘氨酸的盐酸盐，为相应电解质的质量摩尔浓度，X为葡萄糖在葡萄糖-水混合溶剂中的质量百分数，M为恒定的离子强度且M = 1.0mol/kg。并且测定了Glucose-H_2O的密度和介电常数。利用传统的D-H公式外推法和基于Pitzer理论的多项式逼近法分别确定了电池的标准电动势E°_3、E°_3，以及甘氨酸的一级热力学解离1.0mol/kg）-葡萄糖-水-HCl的HCl无限稀释溶液为参考态，并将两种方法得到的结果作了比较。甘氨酸的一级热力学解离常数符合Harned-Robinson方程：pK = A_1/T + A_2 + A+3 T 本文讨论了盐和有机物对pK_1的影响，并根据前人及我们的工作，指出在极性质子溶剂中和在极性非质子溶剂中的pK_1对1/D作图，分别得到直线和曲线。同时讨论了混合溶剂中甘氨酸的一级解离过程的各个热力学量ΔG°，ΔH°，ΔS°，ΔCp°，并讨论HCl的迁移性质和有机物葡萄糖、盐对它们的影响。最后将不同混合溶剂中甘氨酸解离过程的迁移能，迁移熵等作了比较。