超临界CO2+EtOH+CO+H2四元体系压力和温度变化规律及超临界性质的研究

在5～11MPa的范围内,利用恒容静态平衡法详细考察了CO2密度在0.542～0.590g/cm3范围的不同组成的超临界CO2+EtOH+CO+H2四元体系的压力和温度的变化规律,并测定了相应的临界温度和临界压力.模拟了超临界丙烯氢甲酰反应体系的相行为.结果发现,CO+H2加入量的增多可明显改变超临界CO2+EtOH+CO+H2四元体系的超临界性质,主要表现为该体系的临界温度随着CO和H2摩尔分数的增加而线性降低,临界压力随着CO和H2摩尔分数的增加而线性增加.在相同的CO和H2组成下,超临界四元体系的压力随着体系温度的增加而线性增加,并且p-T线的斜率基本相同.在相同温度下超临界四元体系的压力随着体系中CO和H2摩尔分数的增加线性增加,并且不同温度时的变化率基本相同.     

超临界CO_2诱导相转化法制备聚苯乙烯膜及膜体系的相图计算

以甲苯为溶剂,利用超临界CO_2诱导相转化法制备了多孔非对称聚苯乙烯膜.通过扫描电镜对膜结构进行了表征,探讨了不同温度、压力和铸膜液中聚苯乙烯浓度对膜形态、孔径分布及膜孔隙率的影响;同时,基于Tompa扩展的Flory-Huggins聚合物溶液理论计算了聚苯乙烯/超临界CO_2/甲苯铸膜体系的三元相图.研究表明,在温度为35~65℃、压力为8~16 MPa及聚合物质量分数为15%~35%条件下,制备的聚苯乙烯膜截面呈胞腔状孔结构,孔隙率为53.54%~84.67%,且孔隙率随温度、压力和聚苯乙烯浓度均呈现出先增大后减小的趋势.相图计算结果表明,温度对体系双节线位置的改变影响较小,而压力对其影响相对较大.     

分散红60在超临界CO2中的溶解度实验研究

有关分散染料与超临界CO2二元体系的相平衡数据(溶解度)实验测定及模型关联,对超临界流体染色工艺基础研究及工业化至关重要。本文建立了高压溶解度测试实验装置,在温度353～393K、压力15～30MPa条件下,对分散红60在超临界CO2中的溶解度进行了测定。并利用zcan经验公式对实验结果进行关联,关联结果和实验结果吻合较好,最大误差为9.3%。结果表明:体系的压力、温度和混合物密度是影响分散染料在超临界CO2中溶解度的重要因素;可利用zcan经验公式对染料等固体物质在超临界CO2中的溶解度进行关联计算。     

PEBAX®2533/PSf中空纤维复合膜制备及阻力性能

采用浸渍涂层法制备了聚醚共聚酰胺(PEBAX®2533)/聚砜(PSf)中空纤维复合膜. 考察了涂层液浓度、 温度和基膜预处理对复合膜结构、 阻力及渗透性能的影响, 并考察了操作压力对膜渗透性能的影响. 实验结果表明, 随着涂层液浓度的增加, 复合膜致密层厚度及阻力增大, 复合膜总阻力及支撑层阻力先增大后减小, CO2渗透速率先减小后增大, 分离系数增大. 随着涂层温度升高, 复合膜致密层厚度及阻力减小, 支撑层阻力增大, 复合膜总阻力先减小后增大, 分离系数和渗透速率先增大后减小. 经过预处理, 复合膜致密层厚度减小、 阻力大幅度减小, CO2渗透速率增大58%, 分离系数略有下降. 复合膜支撑层阻力过大, 尤其是支撑层的致密结构影响复合膜的塑化行为.     

Study on the syngas methanation of nickel-based catalyst

实验基于工业用镍基甲烷化催化剂,分别考察了操作温度、原料气CO浓度、操作压力、空速等对合成气(CO浓度5％～25％)甲烷化反应的影响,并分析了造成催化剂失活的因素.结果表明,在300～500℃CH4的生成速率随着温度的升高、压力的增大、CO浓度的增加而增大.但CO的浓度不能过高,当H2/CO≤3时催化剂的催化活性会逐步下降.通过XRD、EDS等分析结果得知,催化剂表面存在积炭,催化剂的失活跟积炭有关,通过进一步的对照实验和BET分析表明,积炭的速率与反应温度有关,温度越高积炭速率越快.     

CO2/离子液体体系热力学性质的分子动力学模拟

超临界CO2和离子液体(ILs)是两种绿色溶剂. 离子液体可以溶解超临界CO2, 而超临界CO2不能溶解离子液体. 由此设计构成的CO2/IL二元系统, 同时具备了超临界CO2和离子液体的许多优点: 既可以降低离子液体的粘度, 还便于相分离, 是新型的耦合绿色溶剂. 其物理化学性质对于设计反应、分离等过程非常重要. 因此, 本文以CO2/IL二元系统为研究对象, 通过选择合适的分子力场和系综, 运用分子动力学(MD)模拟方法研究了CO2/[bmim][PF6]、CO2/[bmim][NO3]等体系的热力学性质. 结果表明, CO2对ILs膨胀度的影响非常小, 当CO2摩尔分数为0.5时, ILs膨胀仅为15%. CO2/ILs的扩散系数远小于CO2膨胀甲醇、乙醇溶液的扩散系数. 随着CO2含量的增加, ILs的扩散系数提高, 粘度显著下降, 表明CO2能有效地改善ILs扩散性, 减小其粘度. 因此CO2可用以改善离子液体溶剂体系的传递特性, 增强反应分离过程在其中的进行.     

近/超临界水条件下生物质气化的研究进展

回顾了近/超临界水条件下生物质气化的研究进展。由于超临界水的特殊性能,同其他热化学气化相比,湿生物质不必干燥就可以直接与超临界水作用,生成的气体产物主要是H2、CO2、CO、CH4以及少量的C2H4和C2H6。讨论了温度、压力、停留时间、生物质浓度等影响因素对超临界水生物质气化的影响。高温、低生物质浓度有利于气化反应进行;与温度相比,压力对反应的影响要小得多。产气量随着停留时间或反应时间的增加而增加,到一定值后保持不变。催化剂和盐类的加入有利于气化,而酚类、蛋白质、氨基酸、硫对反应有抑制作用。文中,针对近临界和超临界水的特点,提出先对生物质进行近临界水气化,再进行超临界水气化,实现生物质高效气化的研究思路。     

二氧化碳从它溶胀后的聚合物中的解吸

研究了经过40℃,8.0～14.0MPa的超临界二氧化碳溶胀后的6种聚合物LDPE、PP、PA6、EVA、PS和PU中的CO2解吸情况,模拟了聚合物中CO2的解吸规律,即以时间的自然指数递减规律,并根据Fick扩散定理从理论上推导出CO2在聚合物中的解吸方程,由解吸方程计算解吸扩散系数,结果表明CO2的解吸扩散系数数量级达10-7cm2/s,解吸扩散系数与CO2在聚合物中的浓度和温度以及解吸前聚合物在超临界二氧化碳中的压力有关。     

超临界二氧化碳中布洛芬响应因子的研究

应用高压紫外检测器在线测定了布洛芬在超临界二氧化碳中的响应因子。 考察了温度、压力和CO2密度等参数对它的影响。在温度298-333K、压力9-17MPa范围内超临界CO2中布洛芬的响应因子随CO2密度的增加而线性递减。建立了布洛芬在超临界CO2中响应因子的经验计算式(回归系数r=0．97)，其理论计算结果与实验数据吻合良好，最大误差≤10％。     

低温高活性熔铁催化剂上的超临界相费托合成反应

在固定床反应器中超临界相条件下研究了熔铁催化剂上的费托合成反应,发现在超临界介质中反应物和产物更容易扩散,较好地抑制了催化剂表面非活性碳的沉积,从而提高了费托合成反应中的CO转化率和烯烃选择性,增加了链增长因子,降低了甲烷选择性.同时,考察了超临界介质、反应温度、压力、H2/CO比和空速等条件对费托合成反应的影响.结果表明,C5-8正构烷烃在催化剂活性温度下都是适宜的超临界介质.当温度和压力都在介质的临界点以上时,介质表现出较好的传质与传热性能,可改善费托合成反应性能.     

A catalyst-free novel synthesis of diethyl carbonate from ethyl carbamate in supercritical ethanol

Diethyl carbonate has been synthesized via the alcoholysis of ethyl carbamate in supercritical ethanol under catalyst-free conditions.The influences of various parameters such as reaction temperature,reaction time,reaction pressure,ethanol/ethyl molar ratios and reaction loading volume on the yield of DEC were studied systematically.The experimental results indicated that the alcoholysis of ethyl carbamate was greatly improved in supercritical ethanol.The optimal reaction conditions were as follows：a reaction temperature of 573 K,a reaction time of 30 min,a reaction pressure of 13.2 MPa,an ethanol/ethyl carbamate molar ratio of 10 and a reactor loading volume of 285 μL respectively.The optimal yield of DEC was 22.9%.     

Relationship between the density of supercritical CO_2 + ethanol binary system and its critical properties

The solvent strength and selectivity of supercritical fluids (SCF) can be greatly enhanced by addition of one or two entrainers into the system. The amount of entrainer added is usually less than 5% (mole fraction). However, even with such slight amount, solubility of organic solutes has been observed to increase by several orders magnitude[1]. Therefore, critical pressure and tem-perature data of these supercritical fluid + cosolvent systems are imperative for the reasonable design of effici…     

Relationship between the density of supercritical CO<Subscript>2</Subscript> + ethanol binary system and its critical properties

The dependent relation between temperature and pressure of supercritical CO₂+ ethanol binary system under the pressure range from 5 to 10 MPa with the variety of densities and mole fractions of ethanol that range from 0 to 2% was investigated by the static visual method in a constant volume. The critical temperature and pressure were experimentally determined simultaneously. The PTρ figures at different ethanol contents were described based on the determined pressure and temperature data, from which pressure of supercritical CO₂ + ethanol binary system was found to increase linearly with the increasing temperature. P-T lines show certain convergent feature in a specific concentration of ethanol and the convergent points shift to the region of higher temperature and pressure with the increasing ethanol compositions. Furthermore, the effect of density and ethanol concentration on the critical point of CO₂ + ethanol binary system was discussed in details. Critical points increase linearly with the increasing mole fraction of ethanol in specific density and critical points change at different densities. The critical compressibility factors Z_c of supercritical CO₂ + ethanol binary systems at different compositions of ethanol were calculated and Z _c -ρ figure was obtained accordingly. It was found from Z _c -ρ figure that critical compressibility factors of supercritical CO₂ unitary or binary systems decline linearly with the increasing density, by which the critical point can be predicted precisely.     

Supercritical fluid chromatography with a slurry-packed capillary column

A versatile system with a slurry-packed capillary column was developed for supercritical fluid chromatography, which is capable of programming both inlet and outlet pressure independently, as well as using a restrictor to apply back pressure. This system revealed the relationships between pressure drop, flow rate, and linear velocity in pressure-programmed supercritical fluid chromatography. In the restrictor system, both the pressure drop and the flow rate increased almost linearly with inlet pressure, while under conditions of constant pressure drop characteristic behavior was observed which depended on the density-viscosity relationships of supercritical fluid. Resolution in the separation of polysiloxane oligomers was found to be increased by increasing the ratio of pressure drop to pressure-programming rate, although the sensitivity decreased due to the increase in peak volume. The system controlling both inlet and outlet pressure has distinct advantages over the restrictor system controlling both inlet and outlet pressure has distinct advantages over the restrictor system in practical in practical operations.     

Solubilities of caffeine and theophylline in supercritical ammonia

The solubilities of caffeine and theophylline in supercritical ammonia at 140°C have been determined. Both compounds exhibited substantial solubility in the ammonia, with caffeine showing the greatest increase in solubility near the critical pressure where density increases most rapidly. However, theophylline showed an appreciable solubility at pressures substantially below the critical pressure. Possible chemical reactions of supercritical ammonia with these solutes at this temperature were found to be unimportant in the present study. The role of supercritical ammonia as a solvent for polar organic molecules is discussed.     

Study on depolymerization of polycarbonate in supercritical ethanol

The characteristics of depolymerization of PC in supercritical ethanol were investigated in the range of 483-563 K by using a high-pressure batch autoclave reactor. Based on the qualitative and quantitative analyses of the products, a depolymerization-reaction model was proposed to explain the reaction mechanism, i.e. random scission and ester exchange reaction occurred simultaneously during the process of depolymerizaition of PC. It was suggested that the process of depolymerization consisted of subcritical region, transitional region and supercritical region. It was indicated that PC degraded with slow decrease of molecular weight determined by GPC and with the conversion of 7.5% at 513 K in subcritical region. While in the supercritical region, the molecular weight of PC decreased quickly and degraded completely in 30 min at 563 K. Continuous-distribution kinetics could be used to describe the mechanism of polymer degradation and the energy of activation for the random scission of PC in the supercritical region was 97.2 kJ/mol. Moreover, PC could be degraded completely into diethyl carbonate (DEC) and bisphenol A (BPA) with the yields of 89% and 90%, respectively, in supercritical region.     

高温煤焦油的超临界萃取分馏研究

采用正戊烷溶剂,在超临界状态下,于220℃和5MPa~15MPa循序升压条件下,将高温煤焦油萃取分馏为10个液相窄馏分和1个固相沥青产物;切割深度达78.36%,萃余沥青收率为21.64%,明显低于常规蒸馏沥青收率。研究发现,所用高温煤焦油的初馏分萃取收率最高,随着萃取压力的增加,较低压力段一次萃取液相馏分的收率迅速减少;压力达到10 MPa,液相馏分总收率趋于峰值。元素分析和色质联用分析数据表明,随着萃取压力的增加,一次萃取获得窄馏分的碳氢原子比逐渐增加,平均环数和相对分子质量均逐渐增大,萃取馏分逐渐变重。     

Investigation of carbon dioxide modified supercritical and near supercritical carrier streams for flow injection systems

Since flow injection (FI) is a dilution technique, efforts have been undertaken to minimize online dilution or dispersion. Solutes in supercritical fluids exhibit increased diffusion coefficients which have been shown to decrease dispersion of the sample zone. This work investigates the use of supercritical fluids (or CO₂ modified fluids) as carrier streams for FI. Both a non-reacting tracer and an online chemical reaction were employed to investigate the behavior of solutes in supercritical and near critical systems. Further, these results are compared to those obtained in the system studied with a conventional carrier stream. Plots of peak response vs% CO₂ modifier increase with a sharp break at moderate modifier composition (20–30%). Plots of peak variance vs% CO₂ modifier show decreased variance with increasing % modifier. The system was also optimized with regards to temperature and pressure. The optimized system displayed improved limits of detection and decreased variance relative to 0% CO₂ modifier carrier streams.     

Van der Waals supercritical fluid: exact formulas for special lines

In the framework of the van der Waals model, analytical expressions for the locus of extrema (ridges) for heat capacity, thermal expansion coefficient, compressibility, density fluctuation, and sound velocity in the supercritical region have been obtained. It was found that the ridges for different thermodynamic values virtually merge into single Widom line only at T < 1.07T(c), P < 1.25P(c) and become smeared at T < 2T(c), P < 5P(c), where T(c) and P(c) are the critical temperature and pressure. The behavior of the Batschinski lines and the pseudo-Gruneisen parameter γ of a van der Waals fluid were analyzed. In the critical point, the van der Waals fluid has γ = 8/3, corresponding to a soft sphere particle system with exponent n = 14.