Effect of pressure on the selectivity for the esterification of ethylene glycol with propionic acid in supercritical CO2

The esterification of ethylene glycol with propionic acid was investigated in supercritical CO2 at 50.0 degrees C. The effect of pressure on equilibrium conversion and selectivity of ethylene glycol monopropionate (monoester) and ethylene glycol dipropinonate (diester) was studied systematically. It was shown that the equilibrium conversion and selectivity was nearly independent of pressure as pressure was lower than 9 MPa. At higher pressure, however, the yield and selectivity of the diester increased considerably, while those of the monoester decreased with increasing pressure. The main reason was that reactants and products distributed between the vapor phase and liquid phase at higher pressures. The solvent power of CO2 for the diester is stronger than that for the monoester. More diester molecules in the liquid phase were extracted into the vapor at higher pressures, which shifted equilibrium of the consecutive reversible reactions.     

硅对铁基费-托合成催化剂的影响

用共沉淀法制备了一系列不同硅含量的铁基催化剂,采用N2吸附和原位X射线衍射对催化剂进行了表征,在固定床反应器中考察了催化剂的费-托合成反应活性、选择性和稳定性.结果表明,含硅的催化剂具有较大的比表面积和较小的平均孔径,在CO还原及费-托合成反应中生成的碳化铁物种的稳定性比不含硅的催化剂高.在费-托合成反应中,不含硅的催化剂具有较高的初始活性,但易失活;含硅的催化剂具有较低的初始活性,但稳定性较高.Fe7C3是活性最高的碳化铁物种.随着硅含量的增加,催化剂的费-托合成反应更易生成低碳数产物.     

Sorption equilibria of CO2/CH4 mixture on activated carbon in presence of water

The sorption isotherms of CO2 + CH4 mixtures on an activated carbon were collected in the presence of water at a temperature suitable for hydrate formation. The equilibrium composition of both phases was determined. The initial concentration of CO2 in mixtures was set at 33, 38 and 42%, and the total pressure was up to 10 MPa. CO2 hydrates were firstly formed following the increase of total pressure, and CO2 dominates the sorbed phase composition. CO2 concentration in the sorbed phase begins to decrease when the partial pressure of methane allows for the formation of methane hydrates. Competition for hydrate cavities was observed between CO2 and CH4 as reflected in the isotherm shape and phase composition at equilibrium. The formation pressure of hydrates is lower for mixtures than for pure gases, and the highest sorption capacity of each gas decreased in the mixture sorption either.     

Study on the phase behaviors,viscosities, and thermodynamic properties of CO2/[C(4)mim][PF(6)]/methanol system at elevated pressures

An apparatus to determine the vapor-liquid equilibria of CO(2)/ionic liquid (IL)/organic solvent multisystems and the viscosity of the liquid phase at elevated pressures has been constructed. The solubility of CO(2) in 3-butyl-1-methyl-imidazolium hexafluorophosphate ([C(4)mim][PF(6)]) and the viscosity of CO(2)-saturated [C(4)mim][PF(6)] have been studied at 313.15, 323.15, and 333.15 K and at pressures up to 12.5 MPa. The phase behavior of CO(2)/[C(4)mim][PF(6)]/methanol ternary mixture and the viscosity of the liquid phases at equilibrium condition have also been determined at 313.15 K and at 7.15 and 10.00 MPa. The partition coefficients of the components in the ternary system are calculated. Peng-Robinson equation of state and some thermodynamic functions are combined to calculate the fugacity coefficients of the components in the system. It demonstrates that the viscosity of the IL-rich phase decreases significantly with increasing pressure of CO(2), and the effect of temperature on the viscosity of CO(2)/IL mixture is not noticeable at high pressure, although the viscosity of the CO(2)-free IL decreases dramatically with increasing temperature. Compressed CO(2) may become an attractive reagent for reducing the viscosity of ILs in many applications. The mole fraction of methanol in the CO(2)-rich phase is much lower than that in the IL-rich phase; this indicates that the interaction between the IL and methanol is stronger than that between CO(2) and methanol. The fugacity coefficient of CO(2) in IL-rich phase is larger than unity, while that of methanol is much small than unity, which further suggests that methanol-IL interaction is much stronger than CO(2)-IL interaction. However, the CO(2)-IL interaction is stronger than the CO(2)-methanol interaction.     

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。     

压缩CO2中Co-N-C催化3-硝基苯乙烯选择性加氢反应动力学及相行为

对于苯环上含有各种可还原基团(如–C=C,–CN,–C≡C)的硝基芳烃,通过选择性加氢来制备芳香胺类化合物依然充满挑战.负载型纳米催化剂通常存在过度加氢的缺陷,虽然通过覆盖部分金属位点等方法可改善其选择性,但多是以牺牲催化活性为代价.得益于较高的原子利用率以及孤立的活性位结构,单原子催化剂在硝基芳烃选择性加氢反应中崭露头角.例如Pt1/FeOx单原子催化剂在3-硝基苯乙烯加氢反应中对目标产物的选择性高于99％,且转化频率(TOF)是Pt纳米催化剂的20倍以上.然而,已报道的单原子催化体系中,活性组分多为Pt族贵金属,且以有机溶剂为反应介质,不符合绿色化学理念.本文以环境友好型溶剂——压缩CO2为反应介质,以氮掺杂碳负载非贵金属Co单原子(Co-N-C)为催化剂,实现了3-硝基苯乙烯的选择性加氢,且反应体系中无任何有机溶剂和助剂.在温和(60 oC,3 MPa H2(RT),总压8.1 MPa)的反应条件下,3-硝基苯乙烯可完全转化,目标产物3-乙烯基苯胺的选择性达到>99％,且产物可通过简单卸压直接分离.Co-N-C单原子催化剂表现出较高的稳定性,循环使用4次以后活性并无明显降低.HAADF-STEM表征发现反应后的催化剂中,Co仍然呈单原子分散.研究发现,通过改变CO2压力(即CO2相行为)可调变H2在其中的溶解度以及在加氢反应中的反应级数,进而调变反应速率.通常认为,催化活性会随CO2压力增大呈线性增加,而本文中转化率却随CO2压力增加呈现"倒V型"曲线关系,即当体系总压为8.1 MPa(PCO2=5.0 MPa)时,转化率达到最大值(100％),而升高或降低CO2压力均会显著降低催化活性.为解释"倒V型"曲线的成因,通过含可视窗的高压釜研究了3-硝基苯乙烯/CO2/H2三元体系的相行为.发现当总压为13.4 MPa时,体系为均匀的一相(即3-硝基苯乙烯完全溶解在CO2中);而当总压为8.1 MPa时,却形成了气-液两相.用激光笔照射高压釜上部的气相时,出现了明显的丁达尔现象,说明其中溶解有少量的3-硝基苯乙烯,呈胶体分散;底部为CO2膨胀的3-硝基苯乙烯液相,且该膨胀行为通过硝基苯-CO2二元相行为研究得到证实(即在一定CO2压力下,6 mL硝基苯可被CO2膨胀至充满整个高压釜(容积为29.3 mL)).动力学研究发现,在不含CO2以及总压为11.2 MPa时,H2的反应级数为～0.5;而当总压为8.1 MPa(CO2压力为5.0 MPa)时,H2的级数降为0,说明该压力下H2的溶解度显著增加.通过Peng-Robinson方程计算了不同CO2压力下H2的溶解度,发现H2溶解度与CO2压力也呈"倒V型"曲线关系,且最高点对应的CO2压力与上述转化率-PCO2曲线一致.因此,当总压为8.1 MPa,CO2分压为5.0 MPa时形成了CO2膨胀的3-硝基苯乙烯液体,溶解入该膨胀液体的CO2促进了H2的溶解,进而使H2的反应级数降为0,从而促进了加氢反应的进行.综上,本文以压缩CO2为溶剂,以非贵金属基Co-N-C为催化剂,发展了一种3-硝基苯乙烯绿色选择性加氢途径.同时发现,改变CO2压力可调变反应体系的相行为及反应动力学行为,进而调变催化性能.该研究结果可为调变压缩CO2介质中进行的其它催化转化反应性能提供借鉴.     

CO在超临界水中的转化以及碱性钾盐的影响

构建了CO高压溶解的进气系统,在连续式反应系统中对超临界水条件下CO的转化规律进行了研究;针对生物质超临界水气化中钾盐的多样性,选择KHCO₃、K₂CO₃和KOH等三种钾盐成分,研究了它们在不同工艺条件（450-600℃、23-29 MPa、停留时间3-6 s）下对超临界水中水煤气转化过程的影响。结果表明,在无催化条件下,提高反应温度、延长停留时间均提高了CO的转化率,而压力对其影响在低压下（23-25 MPa）比较大,高压下（25-29 MPa）比较小,水煤气转化的反应动力学方程为k=10^3.75×exp（-0.66×10⁵/RT）（s^-1）。碱性钾盐均能显著提高CO转化率,其催化促进程度从大到小依次为：KHCO₃>K₂CO₃>KOH。添加碱性钾盐时,提高反应温度、延长停留时间均提高CO转化率,而压力的影响比较复杂。碱性盐对水煤气转化反应的催化是通过草酸盐（HC₂O₄^-）和甲酸盐（HCOO^-）作为中间产物进行的。     

超临界相CO加氢合成甲醇,异丁醇的研究

以正十一～十三烷的混合物为超临界介质,在反应温度３６０～４１０℃、合成气压力７５ＭＰａ、进气空速１７００ｈ－１、介质压力１７８ＭＰａ、总压９３ＭＰａ的实验条件下,研究了固定床反应器中Ｚｎ－Ｃｒ、Ｃｕ－Ｚｎ－Ｃｒ催化剂在超临界相和气相条件下合成甲醇、异丁醇的性能。结果表明,超临界相反应的ＣＯ转化率高于气相反应。在超临界条件下反应,醇类选择性随着温度升高下降较慢,而气相反应醇类选择性随着温度升高下降较快。气相反应产物以甲醇、异丁醇为主,含少量乙醇和正丙醇,超临界相反应的产物分布与气相反应的明显不同,甲醇含量减少,乙醇、正丙醇和异丁醇都有不同程度增加。超临界流体的存在对合成醇链增长有影响,在不同催化剂上的产物分布有较大差异     

工业固定床Fe-Cu-K催化剂浆态床F-T合成适应性研究

采用连续搅拌釜式反应器,在接近F-T合成实际工况下考察了工业固定床Fe-Cu-K催化剂浆态床F-T合成反应性能,研究反应温度、压力、原料气空速和氢碳摩尔比等操作参数对催化剂反应活性、产物选择性和稳定性的影响,实验总运转时间达2 500 h;同时采用扫描电镜技术（SEM）对催化剂的抗磨损性能进行了研究,结果表明,操作参数对催化剂的活性、选择性和目标产物产率有较大的影响,工业固定床Fe-Cu-K催化剂具有一定的抗磨损性能,F-T合成烃产物分布合理;催化剂具有较高的稳定性,在589 h的稳定条件运行内,催化剂的失活速率为0.23%/d（以CO转化率的降低计）;在整个运行期间CH4选择性维持在较低的水平。     

Thermodynamic calculations in the system CH4-H2O and methane hydrate phase equilibria

Using the Gibbs function of reaction, equilibrium pressure, temperature conditions for the formation of methane clathrate hydrate have been calculated from the thermodynamic properties of phases in the system CH4-H2O. The thermodynamic model accurately reproduces the published phase-equilibria data to within +/-2 K of the observed equilibrium boundaries in the range 0.08-117 MPa and 190-307 K. The model also provides an estimate of the third-law entropy of methane hydrate at 273.15 K, 0.1 MPa of 56.2 J mol(-1) K(-1) for 1/nCH4.H2O, where n is the hydrate number. Agreement between the calculated and published phase-equilibria data is optimized when the hydrate composition is fixed and independent of the pressure and temperature for the conditions modeled.     

The Differential Relationships of Thermodynamic Variables for the Equilibrium of Heterogeneous Substances

For the system without adiabatic walls, rigid walls or semi-permeable walls and without chemical reactions or without other restrictions except restrictions of phase equilibrium conditions, if the number of components of the system is k and the number of phases is φ, the degree of freedom of the system at equilibrium is f=k-φ+2. Because the degree of freedom is incapable of being negative, f=k-φ+2≥0, viz.φ≤k+2. For the heterogeneous equilibrium, the number of phases is at least 2, so φ=k+2-f≥2, viz. f≤k. Hence the range of change of φ and f is 2≤φ≤k+2,0≤f≤k, respectitvely. If φ=k+2, there are no independent variables in the system at equilibrium. If φ=k+1, there is one independent variable; if the temperature is selected as the independent variable, the other dependent variables can be expressed as the function of the temperature. If φ=k, there are two independent variables; if the temperature and pressure are selected as the independent variables, the other dependent variables can be expressed as the function of the temperature and pressure. If 2≤φ≤k-1, there are more than two independent variables; if the temperature, pressure and some concentrations are selected as independent variables, the other dependent variables can be expressed as the function of the temperature, pressure and these concentrations. The differential relationships of dependent variables and independent variables are educed out according to the principle of phase equilibriums for 2≤φ≤k-1. In any phase the number of the variables is(k+1), viz. temperature T, pressure p and (k-1) mole fractions x1, x2,…, xk-1. The temperature and pressure are common variables of every phase. The number of independent variables is at best k for the heterogeneous equilibriums of k components. The temperature, pressure and (k-2) concentrations are selected as independent variables. The independent concentration variables are selected entirely from the first phase and the concentration variables of the other phases all act as dependent variables. There is at least one dependent concentration variable in the first phase.     

高压下CO_2-乙醇二元系统的气液平衡

在带有可视石英窗的可变体积高压釜内 ,在 60－ 180℃温度范围、 4.0－ 14.5 MPa压力范围下测定了 CO2和乙醇二元系统的相平衡数据 .根据实验结果预测了 pc,Tc,xc.用 Peng-Robinson方程和 Wong-Sandler混合规则进行了拟合 ,所得结果与实验数据基本相符 .     

高压下CO2-乙醇二元系统的气液平衡

在带有可视石英窗的可变体积高压釜内,在60－180 ℃温度范围、 4.0－14.5 MPa压力范围下测定了CO2和乙醇二元系统的相平衡数据.根据实验结果预测了pc,Tc,xc.用Peng Robinson方程和Wong Sandler混合规则进行了拟合,所得结果与实验数据基本相符.     

合成气直接转化制低碳烯烃催化剂设计及反应条件优化

采用水热法合成了相同粒径、不同硅铝比的ZSM-5分子筛,并通过浸渍法将Fe基（Fe-Cu-K）催化剂负载于ZSM-5上,系统考察了分子筛硅铝比变化对合成气制烯烃（FTO）反应的影响。结果表明,反应条件、分子筛酸性对CO转化率和低碳烯烃选择性有显著影响。当ZSM-5分子筛硅铝比为50时负载型催化剂有着最高的CO转化率（84.71%）和低碳烯烃选择性（32.08%）。H₂-TPR结果表明,硅铝比为50的Z50/FeCuK中Fe物相的还原度最高。原位漫反射红外光谱（DRIFTS）、热重差热分析（TG-DTA）、X射线粉末衍射（XRD）等结果表明,Z50/FeCuK催化剂表面吸附的碳酸盐和烃类吸附物种最多,且其反应后形成了较多的FeC_x晶相。最后对反应条件进行了优化,结果表明,温度为310 ℃,H₂/CO （volume ratio）=2和压力为1.0 MPa时FTO的催化性能最优。     

Co-Generation of C2 Hydrocarbons and Synthesis Gases from Methane and Carbon Dioxide： a Thermodynamic Analysis

This paper deals with thermodynamic chemical equilibrium analysis using the method of direct minimization of Gibbs free energy for all possible CH4 and CO2 reactions. The effects of CO2/CH4 feed ratio, reaction temperature, and system pressure on equilibrium composition, conversion, selectivity and yield were studied. In addition, carbon and no carbon formation regions were also considered at various reaction temperatures and CO2/CH4 feed ratios in the reaction system at equilibrium. It was found that the reaction temperature above 1100 K and CO2/CH4 ratio=1 were favourable for synthesis gas production with H2/CO ratio unity, while carbon dioxide oxidative coupling of methane （CO2 OCM） reaction to produce ethane and ethylene is less favourable thermodynamically. Numerical results indicated that the no carbon formation region was at temperatures above 1000 K and CO2/CH4 ratio larger than 1.     

超临界CO2+碳酸二乙酯二元体系高压气-液相平衡

在带有石英视窗的可变体积高压釜内,于333,353,373和393K等4个温度下,测定了3.0～15.0MPa范围内超临界CO2与碳酸二乙酯(DEC)二元体系的气-液平衡数据.结果表明,当温度恒定时,随着压力的增大,液相中超临界CO2的浓度急剧增大,气相中碳酸二乙酯的浓度缓慢增加.根据实验结果推测出了体系的pc,Tc,xc和Vc等临界性质.     

Liposome fluidization and melting point depression by pressurized CO2 determined by fluorescence anisotropy

The influence of CO2 on the bilayer fluidity of liposomes, which are representative of model cellular membranes, was examined for the first time at the elevated pressures (up to 13.9 MPa) associated with CO2-based processing of liposomes and microbial sterilization. Fluidization and melting point depression of aqueous dipalmitoylphosphatidylcholine (DPPC) liposomes by pressurized CO2 (present as an excess phase) were studied by steady-state fluorescence anisotropy using the membrane probe 1,6-diphenyl-1,3,5-hexatriene (DPH). Isothermal experiments revealed reversible, pressure-dependent fluidization of DPPC bilayers at temperatures corresponding to near-gel (295 K) and fluid (333 K) phases at atmospheric pressure, where the gel-to-fluid phase transition (Tm) occurs at approximately 315 K. Isobaric measurements (PCO2 =1.8, 7.0, and 13.9 MPa) of DPH anisotropy demonstrate substantial melting point depression (DeltaTm = -4.8 to -18.5 K) and a large broadening of the gel-fluid phase transition region, which were interpreted using conventional theories of melting point depression. Liposome fluidity is influenced by CO2 accumulation in the hydrocarbon core and polar headgroup region, as well as the formation of carbonic acid and/or the presence of buffering species under elevated CO2 pressure.     

Metastable Equilibrium in Quaternary System Li2SO4 ＋ K2SO4＋Li2CO3 ＋ K2CO3 ＋ H2O at 288 K

IntroductionThe Zhabuye salt lake, Tibet in China, is famousfor the high concentrations of lithium, boron, andpotassium in the world. The main components areLi , K , Na , B4O72 -, CO32 -, Cl-, SO42 -, andH2O, including rare elements such as Rb and Cs .The…     

氯化钴/邻菲罗啉催化氯苄双羰化合成苯丙酮酸的研究

双羰化是制备α-酮酸及其衍生物的重要反应 ,因其反应途径简捷且收率高而倍受青睐 ,国内外有不少关于氯苄双羰化合成苯丙酮酸的报道 .1 982年发现的钯配合物主要用于催化芳基卤代物的双羰化 [1] ;金子林等[2 ] 进行了八羰基二钴催化氯苄双羰化合成苯丙酮酸的研究 ,李光兴等[3 ] 近期也报道了吡啶 - 2 -羧酸钴的催化氯苄高效合成苯丙酮酸 .受前期吡啶 - 2 -羧酸钴催化双羰化研究成果的启发 ,我们进一步探讨了不同的席夫碱与氯化钴组成的催化体系的双羰化性能 .实验发现 ,采用“一锅煮”的方式 ,将氯化钴和邻菲罗啉 ( Phen)按一定比例加入到…     

Kinetics of the CO oxidation reaction on Pt(111) studied by in situ high-resolution x-ray photoelectron spectroscopy

High-resolution x-ray photoelectron spectroscopy has been used to study the kinetics of the CO oxidation reaction on a Pt(111) surface in situ. The study focuses on the interaction of a preadsorbed p(2x2) layer of atomic oxygen with CO dosed using a supersonic molecular beam. Measurements of O 1s and C 1s spectra at 120 K show that CO adsorbs on the oxygen precovered substrate, but no reaction occurs. A maximum CO coverage of 0.23 ML (monolayer) is observed, with CO exclusively bound on on-top sites. In accordance with the literature, bridge sites are blocked by the presence of atomic oxygen. The reaction of CO with preadsorbed O to CO(2) is studied isothermally in a temperature range between 275 and 305 K. The reaction rate initially increases with CO pressure, but saturates at 9x10(-7) mbar. The data indicate that a certain amount of disordered oxygen within the p(2x2) layer acts as a starting point of the reaction and for a given temperature reacts with a higher rate than O in the well-ordered oxygen p(2x2) phase. For the reaction of CO with this ordered phase, the results confirm the assumption of a reaction mechanism, which is restricted to the edges of compact oxygen islands. The activation energy of the reaction is determined to (0.53+/-0.04) eV, with a prefactor of 4.7x10(6+/-0.7) s(-1).