一种新型CO2/原油助混剂CAA8-X的应用与助混机理

CO₂驱是一种具有广阔前景的提高油藏采收率的方法。其中,降低CO₂与原油的最低混相压力以实现混相驱是增强CO₂驱效果的重要手段。由此我们设计了由亲油基团十六烷基和亲CO₂基团全乙酰蔗糖酯基结合的新型“亲油-亲CO₂助混分子”十六酸全乙酰基蔗糖酯CAA8-X,研究发现,CAA8-X对超临界CO₂流体和不同油相的煤油、白油以及长庆原油有优异的助混效果,界面张力消失法和细管实验法测定结果表明,CAA8-X可以将超临界CO₂/长庆原油的最低混相压力降低20.5%。用分子动力学模拟计算了CO₂分子与全乙酰蔗糖酯基的亲和能力,研究了这类新型“亲油-亲CO₂助混分子”通过多酯头基降低与CO₂亲和势能而降低油/CO₂界面能的助混机理。     

新型类沸石金属-有机骨架材料用于天然气中CO2的分离

研究了在usf型类沸石金属-有机骨架材料(usf-ZMOF)中不同金属离子(Li⁺, Na⁺, K⁺, Rb⁺, Cs⁺, Mg²⁺, Ca²⁺, Sr²⁺, Al³⁺)对天然气分离(以CO₂/CH₄, CO₂/H₂, CO₂/N₂为研究对象)的不同影响. 结果表明, 此类材料对于3种体系的分离选择性均高于现有材料. 其中性能最好的是Al-usf-ZMOF, 其对CO₂/CH₄, CO₂/N₂和CO₂/H₂的分离选择性分别为290, 1700和16800. 同时, 对于经不同的离子交换后的usf-ZMOF, 吸附选择性随着离子电荷值的增加而增大; 对于同一主族的离子, 选择性随着原子序数的增加而减小. 而上述现象的产生是由阳离子和CO₂间的强静电作用所致.     

CuO-CoO-Cr2O3-K2O催化剂的表征及其低碳醇合成反应特性和本征动力学行为考察

本工作用TPR、TPD、XRD、TEM、SEM和物理吸附方法比较系统地表征了CuO-CoO-Cr₂O₃-K₂O催化剂的单组份、双组份及三组份及热失活催化剂的还原特性,热脱附特性、物理吸附特征、物相结构及其形貌特征,同时用考察宏观反应特性与本征动力学行为方法初步探讨了CO₂+H₂,CO+H₂和CO+CO₂+H₂体系反应特性和本征动力学特性,获得以下反应能被光催化、被p-DNB部分阻止及5的生成均表明反应经历了S_RN1机理。     

超临界二氧化碳偶合超声预处理强化玉米秸秆酶水解(英)

提出了一个木质纤维素生物质预处理的全绿色加工过程.以玉米秸秆和玉米芯为原料,以超临界CO₂和超声偶合法对木质纤维素进行预处理.超临界CO₂预处理条件为:压力15-25 MPa,温度120₁70℃,含水量50%,反应时间0.5₄ h.超声场功率600W,温度80℃,作用时间2-8 h.用纤维素酶水解反应获得的还原糖总量来评价预处理效果.结果表明,单纯超临界CO₂和超临界CO₂偶合超声预处理都能够提高生物质水解反应还原糖产量.对于玉米芯,超临界CO₂预处理（170℃,20 MPa,3 0min）后,还原糖产率为62%（未预处理的为12%）.对于玉米秸秆（170℃,20 MPa,2.5 h）,还原糖产率为46.4%.对于玉米芯,超临界CO₂偶合超声预处理（600 W,80℃下超声处理6 h,然后用170℃,20 MPa超临界CO₂预处理30 min）后,还原糖产率为87%.对于玉米秸秆,超临界CO₂偶合超声预处理（600 W,80℃下超声处理8 h,然后用170℃,20 MPa超临界CO₂预处理1 h）后,还原糖产率为25.5%.与未处理生物质相比,X射线衍射结果表明玉米秸秆和玉米芯在超临界CO₂和超声预处理后其结晶度没有明显变化.扫描电镜分析则发现木质纤维素的表面积显著增加.     

均相体系可见光催化还原CO2研究进展和面临挑战

利用太阳能将CO₂还原成可以利用的燃料或者有机物,是洁净新能源的重要研究方向,具有很大的挑战性。均相体系作为光催化还原CO₂最早研究的体系,对于CO₂还原的分子机理研究、新型催化剂设计以及体系优化方面具有重要指导意义。近五年来,均相体系光催化还原CO₂的研究取得了显著进展。本综述将对近五年来均相体系中光催化还原CO₂取得的重要研究进展进行综述,并对均相光催化体系发展面临的挑战进行了总结。     

CO2在非质子溶剂与铁基离子液体复合体系中的吸收

选用非质子型有机溶剂聚乙二醇二甲醚(NHD)与N, N-二甲基乙酰胺(DMAC), 分别与BmimFeCl₄复配, 构建了BmimFeCl₄/NHD和BmimFeCl₄/DMAC复合铁基离子液体体系. 考察了温度、 BmimFeCl₄/溶剂的质量 比以及压力对CO₂在复合铁基离子液体体系中溶解行为的影响. 结果表明, 高压低温的吸收条件更利于CO₂ 的溶解, 当BmimFeCl₄/DMAC质量比为7∶3时, CO₂在BmimFeCl₄/DMAC复合体系中的亨利系数为0.9181 MPa·L·mol^-1, 低于同等条件下BmimFeCl₄/NHD体系的亨利系数. 在常压、 363.2 K条件下进行再生, 经5次循环后, CO₂在BmimFeCl₄/NHD和BmimFeCl₄/DMAC中的溶解度分别为初次吸收量的92.53%和99.04%. 傅里叶变换红外光谱(FTIR)结果表明, 铁基离子液体复配体系吸收CO₂为物理吸收过程. 密度泛函理论(DFT)计算与IRI分析的结果表明, 在复配DMAC的体系中, CO₂更倾向与阳离子和溶剂分子作用, 而在复配NHD的体系中, CO₂则更容易与阴离子和溶剂分子作用.     

可见光驱动丰产金属卟啉类配合物催化的二氧化碳选择性还原反应

随着能源短缺和环境问题日益突出, 寻找清洁和可再生能源来替代化石燃料是本世纪科学家面临的最紧迫的任务之一. 为了实现我国“双碳”战略目标, 利用太阳能将二氧化碳(CO₂)转化为清洁燃料和化学品是实现社会可持续发展的途径之一. 催化剂是CO₂光还原技术的核心组成部分, 其可以吸附气态CO₂分子, 在可见光照射下将CO₂还原为一氧化碳(CO)、 甲酸(HCOOH)、 甲醇(CH₃OH)或甲烷(CH₄)等能源小分子. 目前, 新型CO₂还原光催化体系的开发取得了很好的进展. 本文综合评述了近年来均相及非均相丰产金属卟啉类催化剂在光催化CO₂还原中的研究进展, 并对在金属卟啉均相催化剂作用下, CO₂光还原为CO或CH₄的反应机理分别进行了介绍, 还讨论了金属卟啉基多孔有机聚合物与卟啉有机金属框架在光催化CO₂方面的重要应用. 最后, 对可见光驱动卟啉类金属配合物催化的CO₂还原的发展前景进行了展望.     

六硼化镧和六硼化铈与二氧化碳在高温下的作用

用热重法结合化学分析及X射线等固相鉴定的方法研究了LaB₆和CeB₆与CO₂在500—1000℃范围内的化学作用,实验表明六硼化物于700℃以下在CO₂中比较稳定,而700℃以上作用就渐为显著.在所研究的温度范围内,主要的反应可以式(1)表示:2LnB₆+21CO₂→Ln₂O₃·3B₂O₃+3B₂O₃+21CO(1) 其中Ln=La或Ce;少量的反应按式(2)进行 4LnBe₆+21CO₂→2Ln₂O₃·3B₂O₃+6B₂O₃+21C(2) 根据试样在反应过程中的增重按主要反应式(1)估算了各温度下的反应速度.计算结果表明,当作用量不太大时(即温度不高、或温度虽高而在反应初始阶段),作用分数R与时间t符合于式(3):1-(1-R)^1/3=k₁t(3) 而在较高温度反应进行一定时间后,R与t则有下列关系:[1-(1-R)^1/3]³=k₂t(4) 其中k₁及K₂在不同温度下为不同的常数.对上述结果提出了解释.     

丙烯酰胺多面体低聚倍半硅氧烷在超临界CO2中的RAFT聚合

以超临界CO₂为聚合介质, 硫代苯甲酰基特丁基硫酯(TTBT)为链转移剂, 通过可逆加成-断裂链转移(RAFT)聚合制备了聚丙烯酰胺多面体低聚倍半硅氧烷(PAMPOSS)均聚物及其与甲基丙烯酸甲酯(PMMA)的嵌段共聚物(PAMPOSS-b-PMMA). 对产物结构组成和分子量及其分布进行表征. 结果表明, 在TTBT的控制下, POSS的均聚物和嵌段共聚物具有高分子量及窄分子量分布. 含POSS单体在超临界CO₂中为均相聚合, POSS聚合物的结晶性在一定程度上影响其在超临界CO₂中溶解性.     

双中心多孔聚合物作为多相催化剂实现CO2在温和条件下高效转化

由于对化石燃料的高度依赖和二氧化碳(CO₂)的过度排放,大气中CO₂浓度从280 ppm上升到400 ppm左右,导致全球变暖和其他气候问题.在这种情况下,如何有效降低空气中的CO₂浓度成为近年来最迫切的研究领域之一.另一方面,作为一种无毒、廉价且丰富的C1资源,CO₂也可以转化为各种高附加值的工业产品,如甲酸、一氧化碳、甲烷、甲醇以及碳酸酯等.其中CO₂与环氧化物转化生成环碳酸酯的环加成反应具有良好原子经济性,在近年来引起了人们的广泛关注.尽管已有多种多相和均相催化剂应用于该反应,但已有的催化剂特别是多相催化剂往往具有反应条件苛刻、催化剂易损失以及需要可溶性的共催化剂等缺点,从而限制了它们的进一步实际应用.因此,发展多相催化剂实现在温和和无共催化剂条件下的CO₂环加成转化仍是一个挑战.本文通过自由基共聚的方法,以乙烯基功能化的金属卟啉和季膦盐作为单体制备了一种新型多孔有机聚合物(POP-PBnCl-TPPMg-x).考虑到金属卟啉和季膦盐常作为CO₂环加成反应中的Lewis酸和Lewis碱活性中心,我们通过自由基共聚实现了这两种活性中心在分子水平上的结合与协同.所得的催化剂的组成和结构通过固体核磁、X射线光电子能谱、氮气吸附、扫描电子显微镜、透射式电子显微镜等手段进行了表征.值得指出的是,所得多相催化剂具有良好的CO₂吸附与富集效应,十分有利于CO₂的催化转化.我们以温和(40℃和1 atm CO₂)并没有任何无可溶性共催化剂存在条件下,进行CO₂与环氧化物的环加成作为探针反应,测试了不同催化剂的催化活性.以催化剂POP-PBnCl-TPPMg-12为例,其催化活性远超过单组分的POP-PBnCl和POP-TPPMg多相催化剂,也超过了二者机械混合的POP-PBnCl+POP-TPPMg-12催化剂,接近均相催化剂PBnCl+TPPMg-12的水平.这表明通过共聚合方法所得到的催化剂可以实现Lewis酸和Lewis碱两种活性中心的分子水平的结合.本文进一步研究了多相催化剂POP-PBnCl-TPPMg-12和均相催化剂PBnCl+TPPMg-12在低浓度CO₂(15%N2 v/v,工业废气中CO₂的浓度)条件下的催化活性,发现在该条件下多相催化剂表现出比均相催化剂更为优异的催化转化性能,且展现出良好的稳定性和循环使用性能,在循环使用5次后仍无明显的活性损失.该催化剂所具有的多相特点和优良的催化性能,因而有望成为实现工业CO₂脱除并转化成高附加值产品的潜在高效催化剂.     

Study on Phase Equilibrium Properties for CO_(2+) Cosolvent Binary Systems

Recently, the application of supercritical fluid technology is very interested, and it is applied in many areas for its special properties. The performance of supercritical fluid (SCF) as a solvent can be greatly affected by addition of an entrainer to the system. An entrainer can be added to a supercritical fluid to enhance its solvent strength and/or selectivity. Critical point data for these dilute supercritical fluid-cosolvent systems are imperative for the design of efficient separation …     

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…     

Determination of Critical Parameters of Carbon Dioxide ＋ Butyraldehyde System with Different Compositions

Supercritical carbon dioxide（SC-CO2 ） is considered in green chemistry as a substitute for conventional solvents in chemical reactions due to its environmentally benign character. Recently we have reported the homogeneous hydroformylation of propylene in supercritical carbon dioxide（ SC-CO2 ） , which is an example of this kind of application of carbon dioxide. The determination for the critical parameters of carbon dioxide ＋ butyraldehyde mixtures is necessary for this reaction design which is the focus of the present paper. The critical parameters of the binary systems were determined via the static visual method at a constant volume with the molar fraction of butyraldehyde ranging from 1.0% to 2. 2% and the pressure ranging from 5 to 10 MPa. The experimental results show that the critical pressure and temperature increased with increasing the molar fraction of butyraldehyde. The bubble（dew） temperatures and the bubble （dew） pressures for the binary systems were also determined experimentally. The p-T Figures at different compositions of the binary systems were described. In addition, the critical compressibility factors Zc of the binary systems at different concentrations of n-butyraldehyde were calculated. It was found that the critical compressibility factor values of the binary systems decreased with increasing the molar fraction of n-butyraldehyde in the experimental range.     

Modified mass action law-based model to correlate the solubility of solids and liquids in entrained supercritical carbon dioxide

The solubility of solids and liquids in supercritical CO2 with added entrainers was modeled with a modified version of the equation of Chrastil to include the effect of entrainers. By considering the formation of the solute-entrainer-solvent complexes an equation is obtained which predicts an exponential increase of solubility with fluid density and/or entrainer concentration. The correlating model was tested by non-linear regression through a computerized iterative process for several systems where an entrainer was present. Four experimental parameters are easily regressed from experimental data, hence the corresponding properties of components such as chemical potentials or critical parameters are not needed. Instead of its simplicity, this thermodynamical model provided a good correlation of the solubility enhancement in the presence of entrainer effect.     

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.     

Enhancement of Structural fluctuation in the region connecting two kinds of critical points in temperature-pressure-composition three-dimensional phase diagram: Raman studies of benzene/CO2 binary systems up to supercritical region

Pressure dependence of Raman spectra of benzene/CO2 two-component systems was systematically studied at different temperatures and compositions. We estimated the magnitude of inhomogeneous component in Raman bandwidth to get information on the structural fluctuation in the system. It was found that the inhomogeneous bandwidth attains a maximum on an isothermal plane in the temperature-pressure-composition three-dimensional phase diagram when the state point crosses the line connecting the region where the density fluctuation is large (the vicinity of the critical point of neat CO2) and the region where the concentration fluctuation in a binary system is enhanced (the vicinity of the critical solution point). By accumulating such data, we found that the points of large structural fluctuation comprise a sheet that includes the extension line of the gas-liquid equilibrium line in the phase diagram of neat CO2 and the line connecting critical solution points of the two-component system at different temperatures. Interaction between benzene and CO2 molecules in the supercritical region is briefly discussed.     

How does the critical point change during a chemical reaction in supercritical fluids? A study of the hydroformylation of propene in supercritical CO(2).

An understanding of homogeneous catalysis in supercritical fluids requires a knowledge of the phase behavior and the variation in critical point as the reaction proceeds. In this paper, the critical temperatures, T(c) and pressures, P(c), have been measured for a considerable number of mixtures representing the various stages of the hydroformylation reaction of propene in supercritical CO(2) and different reactant concentrations. Critical point data have also been measured for all of the binary mixtures of the components (CO(2), H(2), CO, propene, n- and isobutyraldehyde) which are not available from the literature or can be deduced from published data. We use the stoichiometry of the reacting system to simplify greatly the phase behavior problem by defining a path through the otherwise multidimensional "phase space". Satisfactory modeling of the data (0.3% in T(c) and 3.0% in P(c)) has been achieved using the Peng-Robinson equation of state and ignoring all binary interactions which do not involve CO(2). The model is used to explore the strategies needed to avoid phase separation in continuous and batch reactions. At a given temperature, a batch reactor may need to be run under much higher pressures than a flow reactor if single-phase conditions are to be preserved throughout the course of the reaction. Most of the critical point data were measured acoustically, but a selection of points were validated using more traditional view-cell procedures.     

Theoretical Studies on Critical Properties of Binary System with Supercritical Carbon Dioxide

A new expression of mixing rule is suggested according to the Mayson‘s mixing rule in this paper,which adopts the Redlich-Kwong cubic equation of state and the modifed Chueh-Prausnitz method to calculate the experiment critical points of six binary mixtures CO2 toluene,CO2 cyclohexane,CO2 n-butanal,CO2 i-butanal,CO2 methanol,CO2 ethanol.The coefficients of interaction parameter in the expression of mixing rule were optimized from experimental data.The calculated results of critical temperature and critical pressure meet the experiment data well.The maximum relative errore of temperature and pressure between the calculation results and experiment data are 1.493% and 5.2236% respectively,indicating that the proposed expression of mixing rule is reasonable.This may provide a fundamental method for studying and predicting the properties of supercritical fluids.     

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.     

Entrainer effect on photochirogenesis in near- and supercritical carbon dioxide: dramatic enhancement of enantioselectivity

Diethyl ether added as an entrainer (cosolvent) to near- and supercritical CO2 significantly enhanced the enantioselectivity of photocyclization of 5,5-diphenyl-4-penten-1-ol sensitized by saccharide naphthalenedicarboxylate to give a cyclization product in enantiomeric excesses much larger than those obtained in conventional organic solvents, revealing the unique features of nc- and sc-CO2 as well as the critical role of entrainer clustering to the intervening diastereomeric exciplex pair.