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。     

沉淀剂对CuZnAl催化剂糠醛气相加氢制糠醇选择性的影响

采用共沉淀法制得分别以NaOH、Na_2CO_3和Na_2CO_3/NaOH为沉淀剂的CuZnAl-1、CuZnAl-2和CuZnAl-3催化剂,采用X射线衍射(XRD)、N2吸附-脱附、H_2-程序升温还原(H_2-TPR)、热重和NH_3-程序升温脱附(NH3-TPD)等方法对催化剂进行了表征,并在固定床反应器上研究了沉淀剂对CuZnAl催化剂糠醛气相加氢制糠醇选择性的影响。结果表明,糠醛加氢在三种催化剂上均有较高转化率,而CuZnAl-3催化剂对糠醇有较高选择性。沉淀剂对CuZnAl催化剂的物相结构、比表面积、酸性和氧化还原性均有较大影响。以Na_2CO_3/NaOH为沉淀剂得到的CuZnAl-3催化剂具有适宜的比表面积、CuO晶相、较弱的酸性位,且表面CuO易于还原,这些因素有利于催化反应生成糠醇。CuZnAl-3催化剂上糠醛气相加氢制糠醇优化工艺参数为:常压、反应温度180℃、氢醛物质的量比为5∶1、糠醛体积空速0.3h~(-1);糠醛转化率为99.4%,糠醇选择性为98.3%。     

Cu/ZnO催化糠醛气相加氢制2-甲基呋喃的研究

通过共沉淀法制备一系列铜锌催化剂,用于固定床上糠醛气相加氢制2-甲基呋喃的研究。采用X射线衍射仪(XRD)、N_2吸附-脱附、扫描电子显微镜(SEM)、H_2-程序升温还原(H_2-TPR)、NH_3-程序升温脱附(NH_3-TPD)表征,分析催化剂中Cu0和ZnO在催化反应中的作用。结果表明,Cu~0是糠醛加氢的活性中心,氧化锌的加入减小了催化剂晶粒粒径、增大了催化剂比表面积、利于催化剂还原和增加催化剂表面弱酸性位。当Cu/Zn物质的量比为1∶2时,Cu_1Zn_2催化剂具有适宜氧化还原活性中心及弱酸位数量,对2-甲基呋喃表现出较高的选择性。Cu_1Zn_2催化剂在常压、反应温度为200℃、氢醛物质的量比为4∶1、糠醛体积空速为0.3 h-1条件下,糠醛转化率100.0%,2-甲基呋喃选择性最高为93.6%。反应稳定运行200 h后,糠醛转化率仍为100.0%,2-甲基呋喃选择性为80.0%,糠醇选择性为11.4%。     

Pd/Cu(111)双金属表面催化糠醛脱碳及加氢的反应机理

采用密度泛函理论(DFT)研究糠醛在最稳定Pd/Cu(111)双金属表面上的吸附构型和糠醛脱碳及加氢的反应机理。结果表明,当糠醛初始吸附于O_3-Pd-top、O_7-Cu-hcp位时,吸附构型最稳定,其吸附能为73.4 kJ/mol。糠醛在Pd/Cu(111)双金属表面上更易发生脱碳反应。对于糠醛脱碳反应,所需活化能较低,各个基元反应均为放热反应,糠醛更易先失去支链上的H形成(C_4H_3O)CO,然后中间体脱碳加氢得到呋喃,其中,C_4H_3O加氢生成呋喃所需活化能(72.6 kJ/mol)最高,是反应的控速步骤。对于加氢反应,糠醛与首个氢原子的反应需要最大的活化能(290.4 kJ/mol),是反应的限速步骤。     

廉价离子液体体系中玉米芯生成糠醛优化

采用廉价绿色离子液体[TEA][HSO4]作为溶剂,利用微波加热法辅助玉米芯水解并脱水制备糠醛.通过响应面法优化糠醛生成反应条件,有效转换玉米芯中的木糖,并得到82.2％糠醛收率.利用2-丁醇作为萃取剂对糠醛进行回收.重复4次萃取实验,从[TEA][HSO4]中回收99.7％糠醛.在2次[TEA][HSO4]的回收实验...     

介孔Ni/MgO催化剂催化水蒸气重整生物质油制氢

采用水热法制备了介孔MgO作为催化剂的载体,并制备了介孔Ni/MgO催化剂。利用N_2吸附-脱附、XRD、H_2-TPR等对样品进行表征,并考察了介孔Ni/MgO催化水蒸气重整糠醛、生物质油模型物和两种商用生物质油制氢的活性。结果表明,在介孔Ni/MgO催化剂催化水蒸气重整糠醛制氢反应中,随着反应温度的提高,水蒸气重整糠醛中糠醛的转化率、氢气的产率和氢气的选择性,都呈现递增的趋势。在反应温度提高到600℃时,糠醛的转化率和氢气的产率分别达到94.9%和83.2%。Ni/MgO催化水蒸气重整二组分模拟生物质油,糠醛/乙酸、糠醛/羟基丙酮制氢的反应中,氢气的产率分别达到87.3%和86.8%,均高于水蒸气重整糠醛反应中氢气的产率。由此表明,乙酸或羟基丙酮的存在,提高了模拟生物质油中主要有机物组分糠醛的转化率,并相应地提高了氢气的产率。在水蒸气重整商用生物质油制氢反应中,随着反应物水碳比(S/C(molar ratio)=5、10、15、20、25)的提高,主要有机物的转化率、氢气的产率和选择性呈现出增加的趋势。在水碳比为20时,两种生物质油的主要有机物组分(糠醛、乙酸和羟基丙酮)的转化率均可达90%以上,氢气的产率也达到81.0%以上。由此可知,Ni催化剂对于水蒸气重整商用生物质油也具有较高的催化活性。     

糠醛渣热解特性的研究

以糠醛渣为研究对象,应用热重分析法,以高纯氮气为载气对其进行了详细的热重分析试验。结果表明糠醛渣热解随温度升高经历五个不同阶段,表现了糠醛渣热解的复杂性。通过对5 ℃/min、20 ℃/min、50 ℃/min和80 ℃/min的升温速率及不同粒径下的失重曲线进行的对比表明,随着升温速率和粒径的增大,糠醛渣热解的初始温度增大,热解向高温侧移动。最后根据实验数据建立了热解动力学模型,并对数学模型进行了求解,得到了糠醛渣热解反应的动力学参数,表明糠醛渣热解属三级反应。     

糠醛液相加氢用Mo改性Ni-B/TiO2-Al2O3(S)非晶态合金催化剂

以溶胶-凝胶法制备复合载体TiO2-Al2O3(S)负载非晶态Ni-B合金用于催化糠醛液相加氢反应, 并研究了Mo对催化剂的改性作用. 采用ICP(等离子发射光谱)、DSC(差示扫描量热)、N2吸附、TPR(程序升温还原)和TPD(程序升温脱附)等技术对催化剂进行了表征. 研究结果表明, 与单一氧化铝载体相比, 复合载体负载的Ni-B合金催化性能明显提高, 这是由于在同样的制备条件下, 复合载体负载的Ni-B中Ni含量更高, 同时TiO2分散到了γ-Al2O3的孔中, 堵住了部分细孔, 有利于产物糠醇扩散出来, 防止深度加氢. Mo能提高Ni-B/TiO2-Al2O3(S)的热稳定性, 增大Ni的负载量, 使部分氧化态物种变得易于被还原, 表面出现新的加氢活性中心, 并增加化学吸附中心数, 减弱吸氢强度, 因而显著提高了Ni-B/TiO2-Al2O3(S)的活性; Mo添加使Ni-B/TiO2-Al2O3(S)的平均孔径及总孔容均增大, 有利于产物糠醇扩散出来, 还能使糠醇更易从催化剂的表面脱附, 防止其深度加氢, 因而提高了糠醇的选择性. 当Mo含量为1.25%时, 糠醛转化率、糠醇选择性都达到了100%.     

糠醛在Pt(111)表面的吸附和脱碳反应

采用广义梯度近似的密度泛函理论并结合平板模型的方法, 优化了糠醛分子在Pt(111)面的吸附模型,并探究了糠醛脱碳反应形成呋喃的机理. 结果表明: 吸附后糠醛分子环上的C―H(O)键及支链―CHO相对于金属表面倾斜上翘, 分子平面被扭曲, 易于呋喃的形成; 同时, 糠醛分子向Pt表面转移电子0.765e, 环中的大π键与Pt(111)表面的d轨道发生较强的相互作用, 使得糠醛的芳香性被破坏, 环上的碳原子呈现准sp³杂化. 此外, 对糠醛脱碳反应中的各反应步骤进行过渡态搜索, 通过比较各步骤的活化能, 得出糠醛更易先失去支链上的H形成酰基中间体(C₄H₃O)CO, 中间体继续脱碳加氢形成产物呋喃. 该过程的控速步骤为(C₄H₃O)CO^*+^*→C₄H₃O^*+CO^* (^*为吸附位),活化能为127.65 kJ·mol^-1.     

Rapid determination of furfural in biomass hydrolysate by full evaporation headspace gas chromatography

This paper reports a full evaporation (FE) headspace gas chromatographic (HS-GC) method for rapid determination of furfural in the biomass hydrolysate. The data show that a near-complete mass transfer of furfural in the sample from biomass hydrolysate to the vapor phase (headspace) was achieved within 3 min at 105°C when a very small (<40 μL) sample was added to a 20 mL headspace sample vial. The acid-catalyzed furfural decomposition under these conditions was negligible. The furfural in the vapor phase was then determined by HS-GC using a flame ionization detector. The results showed that the method has an excellent measurement precision (RSD<0.5%) and accuracy (recovery=100.2±1.7%) for furfural quantification in carbohydrate hydrolysate samples. The method requires no sample pretreatment, so it is simple, rapid and accurate, and suitable for applications in lignocellulosic biomass conversion to fuel ethanol or other high value-added products.     

NanoTiO2-CNT复合膜电极在DMF溶液中对糠醛的异相电催化还原

通过在乙醇中电化学溶解Ti金属阳极合成前驱体Ti(OEt)4和溶胶-凝胶法在Ti表面修饰一层纳米TiO2-碳纳米管(nanoTiO2-CNT)复合膜, 采用循环伏安和电解合成法研究了nanoTiO2-CNT复合膜电极在N, N-二甲基甲酰胺(DMF)中的氧化还原行为以及对糠醛(furfural)还原的电催化活性. 结果发现, nanoTiO2-CNT电极在阴极扫描时有两对氧化还原峰, 可逆半波电位E r1/2 分别为－1.27 V和－2.44 V(vs SCE, 扫描速度100 mV•s-1), 分别对应于TiO2/Ti2O3氧化还原电对的可逆电极过程和TiO2/Ti(OH)3电对的准可逆电极过程；在DMF电解液中nanoTiO2-CNT复合膜中的Ti(IV)/Ti(III)氧化还原电对作为媒质间接电还原糠醛为糠醇, 反应机理为电化学偶联随后化学催化反应(EC′)机理.     

Determination of furfural in an oscillating chemical reaction using an analyte pulse perturbation technique

A rapid and convenient method for the determination of furfural is presented that is based upon sequential perturbation of the Mn(II)-catalyzed B-Z oscillating system with different amounts of furfural using a continuous-flow stirred tank reactor (CSTR). When the sample was injected, the change in the amplitude and/or period was linearly proportional to the logarithm of the concentration of furfural over the range 3×10⁻⁸∼1×10⁻⁵ mol L⁻¹. This method gave a detection limit of 3×10⁻⁹ mol L⁻¹ under optimum conditions. Finally, the possible mechanism of furfural perturbation in the oscillating reaction is discussed. When the furfural was injected into the Mn(II)-catalyzed B-Z oscillating system, the change in the amplitude and/or period was linearly proportional to the logarithm of the concentration of furfural over the range 3×10⁻⁸~1×10⁻⁵ mol L⁻¹, with a detection limit of 3×10⁻⁹ mol L⁻¹ under optimum conditions.      

水/二甲基亚砜体系中无机盐高效催化木糖脱水制备糠醛(英)

提出了一种高效的均相催化木糖制备糠醛的方法,探讨了水/二甲基亚砜（DMSO）均相体系中不同类型的无机盐对催化木糖制备糠醛的影响.结果表明,氯盐较硫酸盐和硝酸盐表现出较高的催化活性,其中以SnCl₄的催化效果最高.且它与LiCl复配时催化性能更高.当SnCl₄的摩尔分数为0.8时,催化效果最好,糠醛收率达56.9%.反应条件优化实验发现,当催化剂与木糖的摩尔比为0.5:1,固液比为1:20,水与DMSO体积比为5:5时,于130℃下反应6h,糠醛收率达63%.     

Zur Colorimetrie des Furfurols

Summary A review is given of the colour reaction of phenols of the resorcinol type with furfural (RTR) and of its qualitative and quantitative analytical applications.It was found that not only resorcinols but also m-methylsubstituted phenols can give the typical RTR. Paperchromatography of the RTR product of orcinol with furfural showed the complexity of the product.A number of factors, which influence the use of the RTR for the colorimetric determination of furfural in Tollens-distillates have been studied for about 10 phenols of the resorcinol type. In most cases spectral overlapping by the reaction product with 5-hydroxymethylfurfural (HMF) makes the phenols inapplicable. The use of a reductive medium for the colour reaction of furfural with these phenols eliminates this defect but by the result of extreme deviation from Beers law.Orcinol was found to be suitable as furfural reagent for Tollens-distillates. It is fairly unsensitive to HMF and formaldehyde both in spectral overlapping and reactive influence. The RTR of orcinol with furfural does not follow Beers law, the form of its deviation is dependent on Fe³⁺ or Cu²⁺ addition but in each case reproducible. Its optimal sample concentration of furfural from the colorimetric view-point is 200 mg/l.

---

---

I. Mitteilung: diese Z. 161, 324 (1958).     

Enhanced three-dimensional electrochemical process using magnetic recoverable of Fe3O4@GAC towards furfural degradation and mineralization

Furfural is as one of the major environmental pollutants in different industrial effluents such as refinery and petrochemical, paper, cardboard and oil refining. This toxic chemical is irritant and causes allergy for skin, eyes and mucous membranes. This study was developed to investigate the efficiency of a three-dimensional electrochemical process in the presence of granular activated carbon magnetized with Fe₃O₄ (Fe₃O₄@GAC) particle electrodes for removal of furfural from aqueous solution. The particle electrodes structural and morphological featured were determined via BET, VSM, XRD, FE-SEM and FTIR techniques. The experiments were performed based on central composite design (CCD) and the role of influencing factors including reaction time, pH, voltage and initial furfural concentrations at five levels were evaluated. The Quadratic model with high correlation coefficient = 0.9872 (R² and (R²_Adj = 0.9724)) was suggested for experimental data analysis. The performance of electrochemical oxidation towards furfural degradation was enhanced substantially after adding Fe₃O₄@GAC. The highest furfural removal efficiency (98.2%) was achieved under optimal conditions (furfural: 201 mg/L, electrolysis time: 69 min, voltage: 19 V, and pH: 5.0). Besides, over 78 and 74 % of COD and TOC were removed by Fe₃O₄@GAC-based three-dimensional process, respectively. Based on the COD/TOC ratio and average oxidation state (AOS) index, a significant increase was observed in the biodegradability of intermediates of furfural after treatment. Results showed that three-dimensional electrochemical process with particle electrodes is a promising technology for efficient removal of furfural, even at high concentrations. Results of Liquid chromatography–mass spectrometry (LC-MS) analysis and degradation pathway showed that furfural could be oxidized to compounds with smaller molecular masses, which eventually converted to carbon dioxide and water.     

焙烧温度对CuMgAl催化剂催化糠醛气相加氢制糠醇性能的影响

采用分步沉淀过程制得质量比m(CuO)∶m(MgO)∶m(Al_2O_3)为25∶26∶49的CuMgAl类水滑石前驱体,经过不同温度焙烧制得CuMgAl-t催化剂。通过BET、热重、XRD、H_2-TPR和CO_2-TPD对催化剂进行表征,在固定床中考察CuMgAl-t催化剂催化糠醛气相加氢制糠醇的性能。结果表明,焙烧温度影响催化剂活性、稳定性及对产物的选择性,低温焙烧的催化剂经还原后可获得较多活性中心,高温焙烧的催化剂表面具有更多的碱性位,CuMgAl催化剂经450℃焙烧表面存在适宜的活性中心和碱性位。在常压、反应温度180℃、氢醛物质的量比5∶1、糠醛体积空速0.3h~(-1)的条件下,CuMgAl-450催化剂上糠醛的转化率和糠醇的选择性分别达到98.64%和97.66%。     

MgO/NaY催化糠醛和丙酮合成航空燃料中间体的性能研究

采用"机械混合-焙烧"方法制备了负载型固体碱催化剂MgO/NaY,研究了糠醛与丙酮在水-乙醇体系中的羟醛缩合反应,考察了催化剂负载量、原料配比、反应温度、反应时间等因素对催化剂性能的影响。结果表明,20%MgO/NaY催化剂表现出最佳的催化性能,在85℃条件下反应8 h后,糠醛转化率达到99.6%,亚糠基丙酮(FA)和二亚糠基丙酮(F₂A)选择性分别达到42.2%和57.1%,缩合产物的总收率为98.6%。高温促进反应中间体向产物的转化,有利于提高产物的总选择性。改变糠醛/丙酮的摩尔比可调控两种缩合产物的选择性,较高的糠醛/丙酮摩尔比有利于提高F₂A的选择性,但会降低整体反应速率。重复性评价表明,催化剂具有较好的再生性能。     

Catalytic Conversion of Xylose to Furfural by p-Toluenesulfonic Acid (pTSA) and Chlorides: Process Optimization and Kinetic Modeling

Furfural is one of the most promising precursor chemicals with an extended range of downstream derivatives. In this work, conversion of xylose to produce furfural was performed by employing p-toluenesulfonic acid (pTSA) as a catalyst in DMSO medium at moderate temperature and atmospheric pressure. The production process was optimized based on kinetic modeling of xylose conversion to furfural alongwith simultaneous formation of humin from xylose and furfural. The synergetic effects of organic acids and Lewis acids were investigated. Results showed that the catalyst pTSA-CrCl₃·6H₂O was a promising combined catalyst due to the high furfural yield (53.10%) at a moderate temperature of 120 °C. Observed kinetic modeling illustrated that the condensation of furfural in the DMSO solvent medium actually could be neglected. The established model was found to be satisfactory and could be well applied for process simulation and optimization with adequate accuracy. The estimated values of activation energies for xylose dehydration, condensation of xylose, and furfural to humin were 81.80, 66.50, and 93.02 kJ/mol, respectively.     

Effect of acetic acid and furfural on cellulase production of Trichoderma reesei RUT C30

Because of the high temperature applied in the steam pretreatment of lignocellulosic materials, different types of inhibiting degradation products of saccharides and lignin, such as acetic acid and furfural, are formed. The main objective of the present study was to examine the effect of acetic acid and furfural on the cellulase production of a filamentous fungus Trichoderma reesei RUT C30, which is known to be one of the best cellulase-producing strains. Mandels’s mineral medium, supplemented with steam-pretreated willow as the carbon source at a concentration corresponding to 10 g/L of carbohydrate, was used. Four different concentration levels of acetic acid (0–3.0 g/L) and furfural (0–1.2 g/L) were applied alone as well as in certain combinations. Two enzyme activities, cellulase and β-glucosidase, were measured. The highest cellulase activity obtained after a 7-d incubation was 1.55 FPU/mL with 1.0 g/L of acetic acid and 0.8 g/L of furfural added to the medium. This was 17% higher than that obtained without acetic acid and furfural. Furthermore, the results showed that acetic acid alone did not influence the cellulase activity even at the highest concentration. However, β-glucosidase activity was increased with increasing acetic acid concentration. Furfural proved to be an inhibiting agent causing a significant decrease in both cellulase and β-glucosidase production.     

Differential spectroscopy features of furfural in the 320–400 nm region

Application of differential spectrophotometry to furfural enables the presence in it of foreign compounds, especially the products of its autoxidation, and also their nature to be established by a spectral comparison of the sample investigated with pure furfural. The special feature of the spectrum is that the position of the characteristic maximum formed in the presence of various substances changes according to the thickness of the layer investigated: _max=15.9 log l + ₀. The establishment of these properties enables the method to be usedfor the study of different amounts of impurities in furfural by varying the layer thickness. The method is simple in use and possesses a high sensitivity.