磺酸官能化的磁性核壳结构的纳米材料用于果糖脱水制备5-羟甲基糠醛(英)

通过反相微乳液法制备了以Fe₃O₄为核,磺酸官能化的硅基材料为壳层的磁性酸性催化剂.首先制备纳米Fe₃O₄磁核,然后涂层包覆苯基修饰的纳米级硅层,最后进行苯基磺化修饰,制得固体酸催化剂Fe₃O₄@Si/Ph-SO₃H.在果糖脱水制备5-羟甲基糠醛反应中,该催化剂表现出较好的催化活性,优于传统催化剂A-15,且与均相无机酸催化活性相当.当采用二甲基亚砜作溶剂,在110℃下反应3 h,果糖转化率达到99%,5-羟甲基糠醛收率为82%.另外,该催化剂经磁法回收后可多次重复使用.     

介孔磷酸铌一锅法高效催化木糖制备糠醛

木糖转化到糠醛一般包括两步: 首先在酶、碱或路易斯(L)酸的催化作用下异构化木糖到木酮糖, 接下来木酮糖在酸的作用下脱水得到糠醛. 针对木糖水相脱水一步制备糠醛, 利用十六烷基三甲基溴化铵(CTAB)为模板剂, 借助软模板合作策略制备了一种抗水的新型固体酸催化剂, 介孔磷酸铌, 并利用X射线衍射(XRD)、N₂吸脱附、透射电镜(TEM)、氨气程序升温脱附(NH₃-TPD)和吡啶吸附傅里叶变换红外(Py-FTIR)光谱对材料的结构和酸性质进行了表征. 研究发现介孔磷酸铌不仅具有很高的比表面积(>200 m²·g^-1), 比较窄的孔径分布(3.5nm), 同时还具有很强的L酸性和布朗斯特(B)酸性. 通过L酸催化的木糖异构化为木酮糖/来苏糖和B酸催化的木酮糖/来苏糖进一步脱水得到糠醛, 实现了一步由木糖到糠醛的高效转化. 为了优化反应条件, 考察了水溶液中反应温度、投料质量比及反应时间对木糖转化率和糠醛收率的影响, 在最佳的反应条件下, 木糖的转化率为96.5%, 糠醛的收率达49.8%. 进一步地, 为了提高收率且易于分离, 利用4-甲基-2-戊酮(MIBK)/NaCl水溶液(体积比为7:3)作为反应混合溶剂, 使糠醛收率提高到68.4%.     

以NiAl-NO3-LDH为前驱体制备Ni-Al2O3催化剂及其催化乙酰丙酸加氢性能

以NO₃^-插层类水滑石（NiAl-NO₃-LDH）为前驱体制备了一系列不同Ni/Al摩尔比的Ni-Al₂O₃催化剂,考察了其催化乙酰丙酸液相加氢性能.表征结果表明,随着Ni/Al摩尔比的增加,类水滑石层板结构中存在的游离态γ-AlOOH物种逐步演变为游离的Ni（OH）₂物种,制备的催化剂中金属-载体相互作用逐渐减弱,Ni物种分散度逐渐降低,表面酸性中心数量先增多后减少;当Ni/Al摩尔比为3时,所制备的催化剂表面具有最丰富的酸性中心和加氢中心.在酸性中心和加氢中心的协同作用下,该催化剂表现出优异的催化乙酰丙酸加氢合成γ-戊内酯性能及良好的使用稳定性.在160℃,4 MPa氢气条件下反应5 h时,γ-戊内酯的收率最高可达92.7%.     

固定床催化及气相中和法转化木糖制备糠醛

采用固定床催化及气相中和的方法优化了糠醛的洁净生产工艺.在固定床催化阶段主要考察了催化剂硫酸的浓度、原料木糖溶液的浓度及添加助催化剂对糠醛收率的影响;气相中和阶段主要考察了不同金属阳离子及阴离子对糠醛收率及糠醛液酸度的影响.实验结果表明,当固定床催化条件选定为2 mol/L硫酸,木糖溶液质量分数为10%,助催化剂Na Cl添加量80 g时,糠醛收率最高可达到74. 12%;在气相中和阶段,阴离子对提高糠醛收率的影响顺序为SO_4~(2-)Cl-CO_3~(2-)OH~-,而不同金属阳离子的影响不大.经过气相中和制备的糠醛液的酸度均符合国家标准GB/T1926.1-2009.     

SO42-/SnO2-硅藻土型固体酸的制备及其对正丁酸与异戊醇的催化酯化

采用质量比为1∶3的SnCl₄·5H₂O和硅藻土制备的硅藻土Sn(OH)₄溶胶,70 ℃老化12 h,90 ℃干燥12 h、3.0 mol/L硫酸浸渍3 h、550 ℃焙烧3.5 h,制备了SO₄^2-/SnO₂硅藻土型固体酸催化剂。 利用IR、 XRD、TG测试技术表征了催化剂的理化性质。 用于催化正丁酸与异戊醇的酯化反应,当n（异戊醇）∶n（正丁酸）=1.4∶1、催化剂用量为反应物总质量的2.5%、10 mL苯、反应时间70 min时,酯收率为97.7％。 结果表明,该催化剂兼具多元氧化物型固体酸和硫酸酸化改性天然粘土固体酸催化剂的优点,催化活性高,成本低廉、制备方法简单并可适当回收循环使用。     

过渡金属甲基磺酸盐催化醇的四氢吡喃化反应

以过渡金属甲基磺酸盐［Mn(CH₃SO₃)₂·2H₂O, Cu(CH₃SO₃)₂·4H₂O, Co(CH₃SO₃)₂·4H₂O和Zn(CH₃SO₃)₂·4H₂O］为催化剂,在室温条件下催化醇的四氢吡喃化反应,并对反应条件进行了优化。结果表明：当醇用量为30 mmol,醇和3,4-二氢吡喃摩尔比为1.0 ：1.1,甲基磺酸盐用量为1 mmol,二氯甲烷20 mL时,可高效催化醇的四氢吡喃化反应。与路易斯酸催化活性相比,过渡金属甲基磺酸盐催化醇的四氢吡喃化反应效果最好,催化酚的效果较差。用Mn(CH₃SO₃)₂·2H₂O和Cu(CH₃SO₃)₂·4H₂O催化正丁醇的四氢吡喃化反应,重复使用5次,收率分别为89%和92%。     

稻壳碳基固体酸催化剂的制备及在木糖脱水制备糠醛反应中的催化性能

以工业生产中碱法溶硅剩余的稻壳残渣为碳源,采用硫酸磺化法制备稻壳碳基固体酸催化剂,考察了其催化木糖脱水制备糠醛的性能.采用红外光谱、元素分析及表面酸浓度测定等手段对催化剂进行了表征.对固体酸催化剂的制备条件进行了优化,所得催化剂的表面酸浓度可达1.03 mmol/g.以木糖脱水制备糠醛为模型反应,考察了溶剂类别、反应温度和反应时间对固体酸催化剂催化性能的影响.实验结果表明,以二甲基亚砜(DMSO)为反应溶剂效果优于水,并且随着反应温度的升高和反应时间的延长,反应产率逐渐增加,最高可达75.8%.此外,还对催化剂的循环性能进行了研究,探讨了其失活原因和再生方法.     

不同酸解聚麦秸产物分析及其动力学

以麦秸为研究对象,解聚剂为HCl、HNO₃和H₃PO₄,对解聚产物进行定性和定量分析,并利用动力学模型描述木糖及糠醛的产生过程。 结果表明,解聚液中的产物有葡萄糖、木糖、阿拉伯糖、纤维二糖、乙酸、糠醛、5-羟甲基糠醛。 通过引入变量(α,木糖/木聚糖的比值)利用Saeman动力学模型获得了不同温度下,木聚糖的水解速率常数、木糖的转化速率常数以及糠醛的生成速率常数。 HCl、HNO₃和H₃PO₄解聚麦秸,木糖的生成活化能分别为55.5、46.3和59.8 kJ/mol。 结合反应温度、反应时间、反应速率以及木糖和糠醛的浓度,确定最佳解聚条件为:硝酸作解聚剂,在130 ℃下水解95 min。     

柱层析硅胶固载K2CO3催化合成生物柴油的研究

研究了柱层析硅胶-K₂CO₃固体碱催化剂的制备条件,并对其进行XRD、FT-IR和SEM表征分析。结果表明,部分K₂CO₃吸收空气中的CO₂生成KHCO₃,K₂CO₃与 KHCO₃分散到硅胶表面,增强了催化效果。并考查了催化剂用量、醇油摩尔比、反应时间对生物柴油制备的影响。研究表明,催化剂的制备温度为120℃,催化剂用量为原料油质量的5%,醇油摩尔比为12∶1,反应温度70℃,反应时间2h,生物柴油收率可达95.2%。     

钴铝复合氧化物同时催化去除碳烟和氮氧化物

以稳态共沉淀法合成的含Co类水滑石为前驱物, 制备了具有介孔结构的复合氧化物催化剂(CAO), 采用程序升温反应技术评价了催化剂同时去除碳烟和氮氧化物的性能, 并用ICP, BET, SEM和XPS等手段分析了材料结构和催化性能的关联. 结果表明, 催化剂呈现钴尖晶石相, 材料表面除了存在与金属键合的晶格氧外, 还有大量的吸附氧. Co/Al摩尔比和焙烧温度影响催化剂的活性, 当Co/Al摩尔比为4和焙烧温度为800 ℃时制备的4CAO-800是一种综合性能良好的催化剂, 具有较低的起燃温度(t_i=290 ℃), 生成N₂的选择性较高(S_N2/C=3.5%). 在同时去除碳烟和NO_x反应中, 碳烟的催化燃烧过程可能存在溢流机理和氧化还原机理协同作用.     

Microwave-assisted hydrothermal treatment of corncob using tin(IV) chloride as catalyst for furfural production

The hydrothermal treatment of pentose-rich corncob under microwave irradiation was performed using SnCl₄ as catalyst for furfural production in this study. The influences of the catalyst amount, reaction temperature and reaction time on the compositions of the hydrolysate and solid residue were discussed comparatively. The solid residue obtained was characterized by FTIR, XRD and SEM. The results showed that the cell wall structure of the treated corncob was destroyed to a certain extent under the function of catalysts during the treatment, and most of the hemicelluloses were released from the cell wall and entered the hydrolysate as hemicellulose-derived sugars, followed by the selective dehydration to furfural. When the temperature reached the preset value of 190 °C under microwave irradiation, the highest furfural yield of 9.0 wt% (based on the dry weight of corncob) was achieved from the one-step conversion of corncob under the microwave-assisted hydrothermal treatment with a 1 % amount of SnCl₄ (based on the dry weight of corncob) and a solid-to-liquor ratio of 1:20.     

Nanosized cobalt-based catalyst prepared by supercritical phase condition for Fischer-Tropsch synthesis

A series of nanosized Co/Zn/Mn/K composite catalysts for Fischer-Tropsch synthesis (FTS) were prepared by supercritical fluid drying (SCFD) method and common drying (CD) method. The nanosized cobalt-based catalysts were characterized by XRD, TEM and BET techniques. Their catalytic performances were tested in a slurry-bed reactor under FTS reaction conditions. The drying and crystallization were carried out simultaneously during SCFD, therefore, the catalysts prepared by SCFD method have ideal structure and show the FTS performance superior to the others prepared by CD method. The FTS activity and selectivity were improved via adding Zn, Mn and K promoters, and less CH₄ and CO₂ as well as higher yield of C₅₊ products were achieved. The optimal performance of a 92% CO conversion and a 65% C₅₊ product yield was obtained over a catalyst with the component of Co/Zn/Mn/K = 100/50/10/7. Furthermore, the catalytic performance was studied under the conditions of liquid-phase and supercritical phase slurry-bed, and C₅₊ product yield were 57.4% and 65.4%, respectively. In summary, better catalytic performance was obtained using the nanosized catalyst prepared by SCFD method under supercritical reaction conditions, resulting in higher conversion of CO, less CO₂ byproduct, and higher yield of C₅₊ products.     

Highly stable and selective Ru/NiFe_2O_4 catalysts for transfer hydrogenation of biomass-derived furfural to 2-methylfuran

Spinel ferrites NiFe_2O_4 supported Ru catalysts have been prepared via a simple sol–gel route and applied for converting biomass-derived furfural to 2-methylfuran. The as-prepared catalysts were characterized by thermogravimetric analysis(TG), N_2 adsorption–desorption, X-ray diffraction(XRD), scanning electronic microscopy(SEM), and X-ray photoelectron spectroscopy(XPS). Results showed that the catalysts had well-dispersed Ru active sites and large surface area for calcination temperature ranging from 300 to 500 ℃. The conversion of biomass-derived furfural into 2-methylfuran was conducted over Ru/NiFe_2O_4 through catalytic transfer hydrogenation in liquid-phase with 2-propanol as the hydrogen source. A significantly enhanced activity and increased 2-methylfuran yield have been achieved in this study. Under mild conditions(180 ℃ and 2.1 MPa N_2), the conversion of furfural exceeds 97% and 2-methylfuran yield was up to 83% over the catalyst containing 8 wt% Ru. After five repeated uses, the catalytic activity and the corresponding product yield remained almost unchanged. The excellent catalytic activity and recycling performance provide a broad prospects for various practical applications.     

CO2-Enhanced Production and Synthesis of 2,5- Furandicarboxylic Acid under CO2 Flow through Henkel Reaction

The present study investigated the preparation of 2,5-furandicarboxylic acid (FDCA) via the Henkel reaction between furoic acid alkali metal salts and zinc chloride under a continuous CO₂ flow at atmospheric pressure. The results obtained were compared with those of previous studies that used high-pressure conditions or toxic cadmium catalysts. The pathways and rate-determining steps of the reaction are revealed for the first time. Furthermore, the enhanced formation of FDCA through the promotion of carboxyl exchange and rearrangement during the reaction under a CO₂ flow was examined. The CO₂-rich environment afforded a high FDCA yield of 86.30 %, which is the highest yield obtained to date using the Henkel reaction. The findings of this study offer economically improved conditions for large-scale FDCA production.     

Soluble polymer-supported catalysts containing pendant quaternary onium salts for the addition reaction of oxiranes with carbon dioxide

The addition reaction of oxiranes ( 15a-d ) with carbon dioxide (CO₂) was carried out using 1 mol % of soluble polymer-supported quaternary onium salts as catalysts under atmospheric pressure. The reaction of 15a-d with CO₂ proceeded very smoothly to give the corresponding five-membered cyclic carbonates ( 16a-d ) in high yields at 90-100°C. The catalytic activity of the soluble polymer-supported quaternary onium salts was strongly affected by the following factors: kind of reaction solvent, degree of introduction of the pendant onium salt residues in the polymer chain, and type of alkyl group on the onium salts due to the balance between lipophilicity and steric hindrance of the onium salt residue. Furthermore, these soluble polymer-supported quaternary onium salts were found ordinarily to have higher catalytic activity than low molecular weight quaternary onium salts under the same reaction conditions. It was also found that the rate of reaction was proportional both to catalyst concentration and to oxirane concentration. © 1995 John Wiley & Sons, Inc.     

Efficient dehydration of carbohydrates to 5-hydroxymethylfurfural in ionic liquids catalyzed by tin(Ⅳ) phosphonate and zirconium phosphonate

In this work,we synthesized tin(IV)phosphonate(SnBPMA)and zirconium phosphonate(ZrBPMA)by the reaction of SnCl4·5H2O or ZrOCl2·8H2O with N,N-bis(phosphonomethyl)aminoacetic acid,which was synthesized from a biomaterial glycine through a Mannich-type reaction.The SnBPMA and ZrBPMA were very efficient heterogeneous catalysts for the dehydration of fructose to produce 5-hydroxymethylfurfural(HMF),and the SnBPMA had higher activity than the ZrBPMA.The effects of solvents,temperature,reaction time,and reactant/solvent weight ratio on the reaction catalyzed by SnBPMA were investigated.It was demonstrated that the yield of HMF could reach 86.5%with 1-ethyl-3-methylimidazolium bromide([Emim]Br)as solvent,and the SnBPMA and SnBPMA/[Emim]Br catalytic system could be reused five times without considerable reduction in catalytic efficiency.Further study indicated that the SnBPMA and ZrBPMA in[Emim]Br were also effective for the dehydration of sucrose and inulin to produce HMF with satisfactory yields.     

Efficient and Reusable Sn(II)‐containing Imidazolium‐based Ionic Liquid as a Catalyst for the Oxidation of Benzyl Alcohol

A simple and efficient catalytic system [BBIM]Br–SnCl₂ for the oxidation of benzyl alcohol using hydrogen peroxide as the oxidant has been developed. Reaction conditions such as the catalyst dose, the solvents, reaction temperature, reaction time, and the amount of hydrogen peroxide were investigated. The optimum reaction conditions identified were 0.11 g of catalyst, no solvent, 65°C, 15 min, and 2 mmol of hydrogen peroxide. Oxidation of various alcohols was also investigated under the optimized conditions. The catalyst [BBIM]Br–SnCl₂ can be easily recovered and reused for six reaction runs without significant loss of catalytic activity, because the Sn species of the catalyst can be coordinated with the imidazole ring of the ionic liquid. The reused catalyst was further characterized by Fourier transform infrared spectroscopy to evaluate its chemical properties. The results proved that the [BBIM]Br–SnCl₂ catalyst was stable and reusable for the oxidation reactions. A possible mechanism for the oxidation of benzyl alcohol to benzaldehyde is proposed.     

二次法(同晶取代)快速合成Sn-β沸石用于葡萄糖异构制果糖

采用二次法快速合成了Sn-β沸石.该方法包含杂原子脱除和与SnCl₄的同晶取代两个步骤,合成时间从水热法的约40 d缩短为少于1 d,Sn含量更高.将该沸石用于水相催化葡萄糖异构化制果糖反应,详细考察了反应温度、时间、催化剂用量、溶剂以及卤盐添加物对反应性能的影响.在优化的反应条件下,果糖收率最高可达约43%.催化剂可以通过焙烧再生.     

Oxidative carbonylation of phenol to diphenyl carbonate catalyzed by palladium complexes bridged with N,N‐ligands over functionalized silica

Heterogeneous palladium catalysts anchored on functionalized silica were prepared by sol–gel methods and their catalytic properties for the oxidative carbonylation of phenol to diphenyl carbonate (DPC) were investigated. The catalysts were characterized by means of IR, XPS, EA and BET. The Pd loading in the heterogeneous catalysts and leaching in solution were detected by atomic absorption. The effects of different reaction parameters such as temperature, solvent and inorganic cocatalyst on the yield of DPC and Pd leaching were also studied. It was found that Cu₂O and tetrahydrofuran (THF) were the best partners with these heterogeneous catalysts. In the presence of 3 Å molecular sieves as dehydrating agent, the heterogeneous palladium catalyst prepared from 2‐acylpyridine revealed excellent catalytic performance and stability at 110 °C for 5 h, giving 13.7% yield of DPC based on phenol and 4.0% Pd loss in solution. The heterogeneous catalyst was more active and stable compared with traditional supported Pd? C catalyst under the same reaction conditions. Copyright © 2005 John Wiley & Sons, Ltd.     

Rapid SnCl2 catalyzed phenylselenoetherification of (Z)- and (E)-hex-4-en-1-ols

A fast and efficient method for intramolecular heterocyclization of (Z)- and (E)-hex-4-en-1-ols was developed. The method does not cause side reactions of the substrates and provides the cyclic phenylselenoethers in high yields after only few minutes. A catalytic amount of SnCl₂ increased the yield, but in the presence of an equimolar amount of SnCl₂, formation of corresponding cyclic ethers were almost quantitative and reaction occurred instantaneously under extremely mild experimental conditions.