镁铝类水滑石/阳离子淀粉分散体系流变学振荡行为研究

采用稳态剪切和小振幅振荡剪切实验研究了镁铝类水滑石化合物(Mg-Al HTlc)/阳离子淀粉(CS)分散体系(HTlc与CS质量之比R分别为0, 0.02, 0.05和0.08)的流变学性质．实验结果表明: 上述体系在实验pH值(5～11)范围内均为剪切稀释非牛顿流体, 其中, Mg-Al HTlc/CS (R＝0, 0.02和0.05)分散体系的流变曲线符合幂律模型, 而Mg-Al HTlc/CS (R＝0.08)体系符合Herschel-Bulkley模型. 上述体系先于1000 s^－1剪切180 s, 再于1 s^－1(或者3 s^－1)低速剪切时均表观出粘度随时间周期变化的振荡现象. 振荡现象缘于CS分子结构的周期变化. pH值、剪切速率和HTlc含量的变化可以改变振荡周期(频率)和振幅. 低pH值条件下, Mg-Al HTlc/CS (R＝0.08)体系先于1000 s^－1剪切180 s, 再于小振幅振荡剪切(剪切应力0.03 Pa, 频率0.5 Hz)时储能模量G?和损耗模量G?也表现出随时间周期变化的振荡现象.     

Thixotropy of Aqueous Suspensions Containing Mg‐Al Hydrotalcite‐like Compound and Low‐substituted Cationic Starch: Comparison between Oscillatory Shear and Thixotropic Loop Measurements

The rheological properties of aqueous suspensions consisting of positively charged aluminum magnesium hydrotalcite‐like compound (HTlc) and low‐substituted cationic starch (LCS) were investigated. Special emphasis was placed on the thixotropic phenomenon. Thixotropic behavior was investigated by two thixotropic methods: thixotropic loop and oscillatory shear measurements. LCS molecules could be adsorbed onto HTlc particles due to the hydrogen bonding between ether groups or hydroxyl groups of LCS and hydroxyl groups of HTlc. The elastic dynamic response of the HTlc/LCS suspension increased with increasing mass ratio (R) of HTlc and a three‐dimensional network structure could be formed in the suspension with higher R value. The thixotropic type of the HTlc/LCS suspension transformed from negative to positive and then to complex thixotropy when R changed from 0 to 0.5. By comparing between the thixotropic results obtained by thixotropic loop and oscillatory shear measurements, it was validated that the thixotropic loop for the suspension showing complex thixotropy had a crossover point.     

胶含量、pH值及电解质对Mg-Fe-HTlc/高岭土分散体系流变性的影响

胶含量、pH值及电解质对Mg-Fe-HTlc/高岭土分散体系流变性的影响;类水滑石化合物;高岭土;剪切应力;分散体系;流变性     

Effects of Temperature and Catalyst to Oil Weight Ratio on the Catalytic Conversion of Heavy Oil to Propylene Using ZSM-5 and USY Catalysts

It is useful for practical operation to study the rules of production of propylene by the catalytic conversion of heavy oil in FCC (fluid catalytic cracking). The effects of temperature and C/O ratio (catalyst to oil weight ratio) on the distribution of the product and the yield of propylene were investigated on a micro reactor unit with two model catalysts, namely ZSM-5/Al2O3 and USY/Al2O3, and Fushun vacuum gas oil (VGO) was used as the feedstock. The conversion of heavy oil over ZSM-5 catalyst can be comparable to that of USY catalyst at high temperature and high C/O ratio. The rate of conversion of heavy oil using the ZSM-5 equilibrium catalyst is lower compared with the USY equilibrium catalyst under the general FCC conditions and this can be attributed to the poor steam ability of the ZSM-5 equilibrium catalyst. The difference in pore topologies of USY and ZSM-5 is the reason why the principal products for the above two catalysts is different, namely gasoline and liquid petroleum gas (LPG), repspectively. So the LPG selectivity, especially the propylene selectivity, may decline if USY is added into the FCC catalyst for maximizing the production of propylene. Increasing the C/O ratio is the most economical method for the increase of LPG yield than the increase of the temperature of the two model catalysts, because the loss of light oil is less in the former case. There is an inverse correlation between HTC (hydrogen transfer coefficient) and the yield of propylene, and restricting the hydrogen transfer reaction is the more important measure in increasing the yield of propylene of the ZSM-5 catalyst. The ethylene yield of ZSM-5/Al2O3 is higher, but the gaseous side products with low value are not enhanced when ZSM-5 catalyst is used. Moreover, for LPG and the end products, dry gas and coke, their ranges of reaction conditions to which their yields are dependent are different, and that of end products is more severe than that of LPG. So it is clear that maximizing LPG and propylene and restricting dry gas and coke can be both achieved via increasing the severity of reaction conditions among the range of reaction conditions which LPG yield is sensitive to.     

顶空固相微萃取-气相色谱/质谱法分析鉴定畜禽粪便中的挥发性有机化合物

采用顶空固相微萃取(HS-SPME)-气相色谱/质谱法(GC/MS)测定了牛粪、猪粪以及鸡粪中的挥发性有机化合物(VOCs)。在优化HS-SPME条件的基础上,通过GC/MS分析,从牛粪中分离鉴定出44种VOCs,从猪粪中分离鉴定出40种VOCs,从鸡粪中分离鉴定出41种VOCs。HS-SPME-GC/MS具有简单、快速、无需有机溶剂等特点,适合于畜禽粪便中挥发性有机化合物的分析与鉴定。同时,该研究揭示了畜禽养殖场臭味物质的来源,为治理其环境污染提供了科学依据。     

The hydrogenphosphate complex of (1,5-cyclooctadiene)iridium(I), {[Bu4N][(1,5-COD)Ir · HPO4]}n: synthesis, spectroscopic characterization, and ES-MS of a new, preferred precursor to HPO4 and Bu4N stabilized Ir(0)n nanoclusters

The synthesis and characterization of a previously unknown, rare organometallic-phosphate complex, {[Bu₄N][(1,5-COD)Ir · HPO₄]}_n (1), is described. Characterization of 1 was accomplished by elemental analysis, electrospray mass spectrometry (ES-MS), and ¹H and ¹³C NMR which established the symmetry of the product as at least C₂ or C_s. The ES-MS reveals an interesting, Ir(I) to Ir(III) oxidative process with intense peaks displaying the ¹⁹¹Ir/¹⁹³Ir isotopic distribution patterns expected for the fragments [(1,5-COD)Ir^III(HPO₄)₂]⁻, [(C₈H₁₁)₂(Ir^III)₂(PO₄)(HPO₄)(H₂O)]⁻, and [(C₈H₁₁)₂(Ir^III)₂(PO₄)(HPO₄)(H₂O)₂]⁻. These fragments, in turn, provide evidence for a structure with two HPO₄²⁻ groups attached to a single Ir, for example ring structures (of at least such C₂ or C_s symmetry) such as {[Bu₄N][(1,5-COD)Ir · HPO₄]}₂. Complex 1 is significant since it is known to be the preferred, compositionally precise precursor to the prototype example of a recently discovered class of novel, HPO₄²⁻ and Bu₄N⁺ stabilized nanoclusters, (Bu₄N)_2n²ⁿ⁺[Ir(0)_n · (HPO₄)_n]²ⁿ⁻. Such nanoclusters are being extended, via their analogous hydrogenphosphate-organometallic precursors (1,5-COD)M^{+ or 2+}/HPO₄²⁻ (M=Rh(I), Ru(II), Pt(II)) to their corresponding, catalytically active [M(0)_n · (HPO₄)_n]²ⁿ⁻ nanoclusters.     

分子筛硅铝比及晶粒粒径对 Cu-ZnO-Al2O3/HZSM-5催化剂直接合成二甲醚反应性能的影响

采用水热晶化法合成了硅铝比(SiO₂/Al₂O₃)为60、120、200和晶粒粒径分别为1.00和0.25 μm的HZSM-5分子筛,并以其为甲醇脱水活性组分与铜基甲醇合成活性组分(Cu-ZnO-Al₂O₃)组成双功能催化剂(Cu-ZnO-Al₂O₃/HZSM-5),在连续流动加压固定床反应器上考察了Cu-ZnO-Al₂O₃/HZSM-5对合成气直接制二甲醚反应的催化性能。结果表明,随着分子筛硅铝比的提高,二氧化碳副产物的生成量逐渐减少,从而使目的产物二甲醚的选择性逐渐增大。与常规分子筛相比,小晶粒分子筛的反应活性接近,但二氧化碳和烃类副产物的选择性较低。     

Molar Mass,Radius of Gyration and Second Virial Coefficient from new Static Light Scattering Equations for Dilute Solutions: Application to 21 (Macro)molecules

New equations for static light scattering of dilute binary solutions allow molar mass determination of macromolecules from measurements of scattered intensity ratios between solution and solvent (I_r). In contrast to the standard Carr–Zimm equations, they do not rely on the experimental absolute value of the Rayleigh ratio of a reference liquid. The picture shows a typical plot for the surfactant BRIJ72 in CH₂Cl₂ (M_Supplier=0.359 kg mol^?1).

     

Effects on the Reactivity by Changing the Electrophilic Center from CO to CS: Contrasting Reactivity of Hydroxide,p‐Chlorophenoxide,and Butan‐2,3‐dione Monoximate in DMSO/H2O Mixtures

Second‐order rate constants have been measured spectrophotometrically for the reactions of O‐p‐nitrophenyl thionobenzoate ( 1 , PNPTB) with HO^?, butan‐2,3‐dione monoximate (Ox^?, α‐nucleophile), and p‐chlorophenoxide (p‐ClPhO^?, normal nucleophile) in DMSO/H₂O of varying mixtures at (25.0±0.1) °C. Reactivity of these nucleophiles significantly increases with increasing DMSO content. HO^? is less reactive than p‐ClPhO^? toward 1 up to 70 mol % DMSO although HO^? is over six pK_a units more basic in these media. Ox^? is more reactive than p‐ClPhO^? in all media studied, indicating that the α‐effect is in effect. The magnitude of the α‐effect (i.e., k/k_p) increases with the DMSO content up to 50 mol % DMSO and decreases beyond that point. However, the dependency of the α‐effect profile on the solvent for reactions of 1 contrasts to that reported previously for the corresponding reactions of p‐nitrophenyl benzoate ( 2 , PNPB); reactions of 1 result in much smaller α‐effects than those of 2 . Breakdown of the α‐effect into ground‐state (GS) and transition‐state (TS) effects shows that the GS effect is not responsible for the α‐effect across the solvent mixtures. The role of the solvent has been discussed on the basis of the bell‐shaped α‐effect profiles found in the current study as well as in our previous studies, that is, a GS effect in the H₂O‐rich region through H‐bonding interactions and a TS effect in the DMSO‐rich media through mutual polarizability interactions.