果糖低温快速热解制备糠醛的机理研究

果糖低温快速热解制备5-羟甲基糠醛(HMF)的过程中,糠醛(FF)是一种重要的副产物。通过Py-GC/MS(快速热解-气相色谱/质谱联用)实验考察果糖低温快速热解过程中FF的形成特性。结果表明,FF的产率和相对含量都随着热解温度的提高先增大后减小,并在350℃时达到最大值,最高相对峰面积含量达到11.6%。此外,通过密度泛函理论计算,研究果糖热解形成FF的四条可能途径,计算结果表明,果糖热解形成FF的最优途径为路径2,即果糖首先经历一个协同的六元环过渡态,C5-C6键断裂的同时C6位羟基上的氢与C4位的羟基发生脱水反应,脱出一分子甲醛和一分子水,生成含C4=C5双键的二氢呋喃中间体,随后C2位上的羟基与C1位上的氢通过一个四元环过渡态又脱出一分子水,生成的烯醇中间体中烯醇氢与C3位的羟基最后经历一个六元环的过渡态再脱出一分子水,最终形成FF。     

Phosphorylation of Furfural by Secondary Phosphine Oxides

Nucleophilic addition of secondary phosphine oxides to furfural takes place under mild conditions and gives quantitative yields of 2-(diorganylphosphorylhydroxymethyl)furans, which are polyfunctional building blocks for organic synthesis and prospective amphiphilic ligands for the design of metal complex catalysts.     

Catalytic oxidation of furan and hydrofuran compounds 8. Synthesis of 5-ethoxycarbonyl-4-hydroxy-3-oxo-2(3H)-furanone by the oxidation of furfural in the system aqueous H2O2-VOSO4-ethanol

The special features of the oxidation of furfural by aqueous hydrogen peroxide in the presence of vanadyl sulfate and ethanol has been studied for the first time. It has been established that this reaction proceeds with the formation of previously unknown oxidation products of furan compounds, one of which was isolated from the reaction mixture as the ethyl ester. It was established by spectral methods and qualitative reactions that this product is 5-ethoxycarbonyl-4-hydroxy-3-oxo-2(3H)-furanone. __________ Translated from Khimiya Geterotsiklicheskikh Soedinenii, No. 3, pp. 386–392, March, 2008.     

On the Role of Protonic Acid Sites in Cu Loaded FAU31 Zeolite as a Catalyst for the Catalytic Transformation of Furfural to Furan

The aim of the present paper is to study the speciation and the role of different active site types (copper species and Brønsted acid sites) in the direct synthesis of furan from furfural catalyzed by copper-exchanged FAU31 zeolite. Four series of samples were prepared by using different conditions of post-synthesis treatment, which exhibit none, one or two types of active sites. The catalysts were characterized by XRD, low-temperature sorption of nitrogen, SEM, H₂-TPR, NMR and by means of IR spectroscopy with ammonia and CO sorption as probe molecules to assess the types of active sites. All catalyst underwent catalytic tests. The performed experiments allowed to propose the relation between the kind of active centers (Cu or Brønsted acid sites) and the type of detected products (2-metylfuran and furan) obtained in the studied reaction. It was found that the production of 2-methylfuran (in trace amounts) is determined by the presence of the redox-type centers, while the protonic acid sites are mainly responsible for the furan production and catalytic activity in the whole temperature range. All studied catalysts revealed very high susceptibility to coking due to polymerization of furfural.     

Mesoporous Porphyrin-Silica Nanocomposite as Solid Acid Catalyst for High Yield Synthesis of HMF in Water

Solid acid catalysts occupy a special class in heterogeneous catalysis for their efficiency in eco-friendly conversion of biomass into demanding chemicals. We synthesized porphyrin containing porous organic polymers (PorPOPs) using colloidal silica as a support. Post-modification with chlorosulfonic acid enabled sulfonic acid functionalization, and the resulting material (PorPOPS) showed excellent activity and durability for the conversion of fructose to 5-hydroxymethyl furfural (HMF) in green solvent water. PorPOPS composite was characterized by N₂ sorption, FTIR, TGA, CHNS, FESEM, TEM and XPS techniques, justifying the successful synthesis of organic networks and the grafting of sulfonic acid sites (5 wt%). Furthermore, a high surface area (260 m²/g) and the presence of distinct mesopores of ~15 nm were distinctly different from the porphyrin containing sulfonated porous organic polymer (FePOP-1S). Surprisingly the hybrid PorPOPS showed an excellent yield of HMF (85%) and high selectivity (>90%) in water as compared to microporous pristine-FePOP-1S (yield of HMF = 35%). This research demonstrates the requirement of organic modification on silica surfaces to tailor the activity and selectivity of the catalysts. We foresee that this research may inspire further applications of biomass conversion in water in future environmental research.     

Nb-P/SBA-15催化剂的制备及其对果糖水解制5-羟甲基糠醛的催化性能

果糖催化脱水制5-羟甲基糠醛（5-HMF）是生物质转化制高附加值化合物过程中的一个重要反应。采用自制的介孔SBA-15,浸渍法制备了Nb/SBA-15催化剂,再经磷酸化处理制得Nb-P/SBA-15催化剂,研究了该催化剂在果糖脱水制5-HMF反应中的性能。SEM、TEM、BET和XRD表征结果表明,Nb/SBA-15和Nb-P/SBA-15完好地保留了SBA-15的微观结构,其内孔道直径为10 nm,铌酸在孔内表面分布均匀;负载铌和磷酸化后,孔壁变薄。NH₃-TPD结果显示,Nb/SBA-15经磷酸预处理后,不仅弱酸性位有所增加,而且产生了中强酸和强酸性位,使得在含水两相体系果糖脱水反应中,Nb-P/SBA-15比Nb/SBA-15具有更高的催化活性和5-HMF选择性。同时考察了反应温度、溶剂比例、反应时间对果糖脱水的影响,结果表明,以水/MIBK（V/V=1/2）为溶剂时,160 ℃下反应1.5 h,果糖转化率和5-HMF收率分别高达96.1%和92.6%。Nb-P/SBA-15经循环使用四次后仍具有较好的催化活性,表明该催化剂具有较高的耐水稳定性。     

Simultaneous determination of furfural and its degradation products,furoic acid and maleic acid,in transformer oil by the reversed‐phase vortex‐assisted liquid–liquid microextraction followed by high‐performance liquid chromatography

To explore why the use of furfural as a transformer oil‐paper insulation aging characteristic is problematic in real world application, we developed a method for the simultaneous determination of furfural, furoic acid, and maleic acid in transformer oil by reversed‐phase vortex‐assisted liquid–liquid microextraction combined with high‐performance liquid chromatography. The conditions for the proposed method were optimized, and the obtained extract can be directly analyzed by high‐performance liquid chromatography. The detection limits (signal‐to‐noise ratio = 3) of the method ranged from 1.0 to 4.6 μg/L, the enrichment factors for furfural, furoic acid, maleic acid, and fumaric acid were 4.6, 25.1, 15.6, and 17.5, respectively, and the recovery rates for three analytes (fumaric acid was undetected) range from 82.1 to 106.2%. The contents of furfural, furoic acid, and maleic acid resulted from accelerated aging of transformer insulation oil‐paper were measured using the present method for the first time, and the aging samples were analyzed by liquid chromatography with mass spectrometry for the identification of furoic acid and maleic acid in the aging transformer oil samples. Using the optimal method, the target products of samples at different aging time were tracked and measured.     

Furfural Hydrogenation on Nickel‐promoted Cu‐containing Catalysts Prepared from Hydrotalcite‐Like Precursors

The nickel‐promoted Cu‐containing catalysts (Cu_xNi_y‐MgAlO) for furfural (FFR) hydrogenation were prepared from the hydrotalcite‐like precursors, and characterized by X‐ray powder diffraction, inductively‐coupled plasma atomic emission spectroscopy, N₂ adsorption‐desorption, UV‐Vis diffuse reflectance spectra and temperature‐programmed reduction with H₂ in the present work. The obtained catalysts were observed to exhibit a better catalytic property than the corresponding Cu‐MgAlO or Ni‐MgAlO samples in FFR hydrogenation, and the CuNi‐MgAlO catalyst with the actual Cu and Ni loadings of 12.5 wt% and 4.5 wt%, respectively, could give the highest FFR conversion (93.2%) and furfuryl alcohol selectivity (89.2%). At the same time, Cu⁰ species from the reduction of Cu²⁺ ions in spinel phases were deduced to be more active for FFR hydrogenation.     

时间域曲线拟合求取糠醛加氢反应的传递,吸附与动力学参数

利用脉冲-应答技术,测定了糠醛在BHK-1催化剂上的传递与吸附系数和加氢反应速率常数。依据修正过的Kubin-Kucera气固相传质一维扩散模型,用单纯形法进行多维搜索的最优化方法来完成富里埃分析和时间域曲线拟合的计算。求得了六个参数:E、D_e、k_f、k_a、K_a、k_r,并对富里埃分析法和时间域曲线拟合法作了比较。     

Synthesis of g-butyrolactone and 2-methylfuran through the coupling of dehydrogenation and hydrogenation over copper-chromite catalyst

The new coupling process of the dehydrogenation of 1,4-butanediol (BDO) and the hydrogenation of furfural (FFA) over a copper-chromite catalyst was carried out in a continuous fixed-bed reactor. The effects of the reaction conditions on the coupling process were investigated in detail. The results show that the coupling process has some advantages over the individual dehydrogenation and hydrogenation ones, such as optimal hydrogen utilization, good energy efficiency, improved yield and mild reaction condition. This revised version was published online in August 2006 with corrections to the Cover Date.