纤维素超临界水预处理与水解研究

利用超临界水解工艺进行生物质废弃物(秸秆)能源转化, 使其主要成分纤维素在超临界水中快速水解为低聚糖, 为其进一步葡萄糖转化和乙醇发酵解决技术瓶颈. 其中纤维素在超临界水中的溶解是预处理与水解过程的限速步骤. 研究表明, 反应温度达到380 ℃及以上时, 纤维素可迅速溶解并进行水解, 液化比例可达100%; 在374～386 ℃范围内反应温度对纤维素的转化率有明显作用, 低聚糖和六碳糖的总产率在临界点附近出现最大值. 超临界条件下, 低聚糖和六碳糖转化率在较短反应时间内出现峰值, 而后随反应时间的延长快速下降, 固液比对于纤维素的低聚糖和六碳糖转化也有显著影响. 最优水解条件研究显示, 在380 ℃, 40 mg纤维素/2.5 mL水条件下反应16 s可获得最大的低聚糖产率, 为29.3%, 在380 ℃, 80 mg纤维素/2.5 mL水条件下反应18 s可获得最大的六碳糖产率, 为39.2%.     

Cu催化羟基自由基氧化断裂纤维二糖分子糖苷键反应及其在纤维素低温解聚中的应用

纤维素是葡萄糖通过β-1,4-糖苷键链接而成的高聚物,在木质纤维素中含量最高,结构稳定,较难水解.糖苷键的解聚主要有三种方式:酶水解、酸水解以及碱降解.酶解的优点是反应条件温和、副产物少,但存在成本高、活性低等缺点,限制了其大规模的工业化生产.碱水解纤维素的同时伴随着葡萄糖的peeling-off反应得到异变糖酸,需要消耗大量的碱,并且强碱也存在腐蚀性强和回收难等问题.酸水解是目前工业上常用的纤维素水解方法,在保持较高葡萄糖选择性的同时,通过对反应条件的控制(提高反应温度和酸浓度)来提高纤维素的水解效率,但是硫酸对设备的腐蚀性强,也难以回收,不符合绿色化学的发展要求.固体酸是近年来研究较多的纤维素水解催化剂.固体酸虽然腐蚀性弱、易回收,但是其活性低,水热稳定性较差,目前还不具备大规模生产的条件.本文发展了一种羟基自由基活化断裂糖苷键的方法,利用羟基自由基的高活性在低温下实现糖苷键的选择性断裂,同时羟基自由基与糖苷键作用后转化为无毒无害的水和氧气,将不会对环境造成污染.我们首先以纤维二糖作为纤维素的模型分子,通过羟基自由基能够优先与糖苷键反应得到葡萄糖和葡萄糖酸的实验证实所提出的方法的可行性.实验表明,来自H2O2的·OH自由基能够在铜基催化剂作用下选择性氧化断裂其糖苷键,生成葡萄糖和葡萄糖酸.比如:采用均相CuSO4体系,纤维二糖转化率约为20%时,葡萄糖和葡萄糖酸的选择性分别为28.5%和32.3%.采用多相CuO/SiO2(4 wt%CuO)体系,纤维二糖转化率约为20%时,葡萄糖和葡萄糖酸的选择性约分别为23.3%和25.7%,并且该催化剂具有良好的循环使用性能.与·OH类似,CuSO4催化过硫酸钾生成的·SO4-自由基也能够有效转化纤维二糖,在纤维二糖转化率为20%时,葡萄糖和葡萄糖酸的选择性分别为36.6%和39.9%.利用这种·OH和·SO4-自由基氧化的方法,也能够在较低温度下(333 K)解聚纤维素中的糖苷键.我们发展了H2O2浸渍预处理纤维浸渍预处理纤维素的方法,通过部分破坏纤维素糖苷键,提高了纤维素的水解活性.比如:处理后的纤维素在413 K条件下反应12 h,纤维素转化率和葡萄糖选择性分别达到约36.1%和42.5%.XRD结果表明,处理后的纤维素的晶体结构未发生明显的变化.FT-IR表征结果显示处理后的纤维素表面生成了大量的羧酸基团.     

纤维素在超临界水中的反应

纤维素是一种非常有价值的可再生资源,通过其反应可以获得多种有用的物质。对纤维素在超临界水中的反应进行了综述。在没有催化剂的情况下,纤维素在超临界水中水解生成葡萄糖、果糖、低聚物等;对纤维素水解的设备、产物分布以及纤维素水解反应机理进行了阐述。采用Ni,Pt,Ru,KOH等作催化剂,纤维素在超临界水中发生气化反应,生成的气体产物主要为H2,CO2和CH4;介绍了纤维素及其主要水解产物葡萄糖的制氢反应过程。对纤维素超临界水反应技术的发展前景进行了展望.     

酸洗预处理对纤维素热裂解的影响研究

为获得液体产量的最大化和提高产物中糖类的质量分数，采用盐酸（3%、5%、7%）、磷酸（7%）和硫酸（7%）对纤维素进行酸洗预处理。不同酸洗预处理下纤维素的微观结构和聚合度变化表明，酸处理损坏了纤维素的物理结构，并使聚合度大幅度降低。在“┣”形石英玻璃反应器的快速热裂解试验装置上进行了不同酸处理前后的纤维素热裂解试验，发现酸浸泡处理后，生物油产率下降，相应的气体和焦炭产率提高，并且随着酸浓度的提高，该趋势逐渐增强。与盐酸和磷酸相比，硫酸对生物油的生成具有更强的抑制作用，这表明，酸对纤维素交联和脱水反应的催化效果。通过GC-MS色质联机分析技术对生物油成分进行分析，发现酸的存在并没有改变生物油成分的种类，但使化合物之间的相对质量分数发生了变化。左旋葡聚糖的质量分数随稀酸溶液浓度的增加呈下降趋势，原因是残留在物料中的微量酸以催化脱水和交联反应的方式，对其生成起抑制作用。     

Cu催化羟基自由基氧化断裂纤维二糖分子糖苷键反应及其在纤维素低温解聚中的应用（英文）

纤维素是葡萄糖通过β-1,4-糖苷键链接而成的高聚物,在木质纤维素中含量最高,结构稳定,较难水解.糖苷键的解聚主要有三种方式:酶水解、酸水解以及碱降解.酶解的优点是反应条件温和、副产物少,但存在成本高、活性低等缺点,限制了其大规模的工业化生产.碱水解纤维素的同时伴随着葡萄糖的peeling-off反应得到异变糖酸,需要消耗大量的碱,并且强碱也存在腐蚀性强和回收难等问题.酸水解是目前工业上常用的纤维素水解方法,在保持较高葡萄糖选择性的同时,通过对反应条件的控制(提高反应温度和酸浓度)来提高纤维素的水解效率,但是硫酸对设备的腐蚀性强,也难以回收,不符合绿色化学的发展要求.固体酸是近年来研究较多的纤维素水解催化剂.固体酸虽然腐蚀性弱、易回收,但是其活性低,水热稳定性较差,目前还不具备大规模生产的条件.本文发展了一种羟基自由基活化断裂糖苷键的方法,利用羟基自由基的高活性在低温下实现糖苷键的选择性断裂,同时羟基自由基与糖苷键作用后转化为无毒无害的水和氧气,将不会对环境造成污染.我们首先以纤维二糖作为纤维素的模型分子,通过羟基自由基能够优先与糖苷键反应得到葡萄糖和葡萄糖酸的实验证实所提出的方法的可行性.实验表明,来自H_2O_2的·OH自由基能够在铜基催化剂作用下选择性氧化断裂其糖苷键,生成葡萄糖和葡萄糖酸.比如:采用均相Cu SO_4体系,纤维二糖转化率约为20%时,葡萄糖和葡萄糖酸的选择性分别为28.5%和32.3%.采用多相CuO/SiO_2(4 wt%CuO)体系,纤维二糖转化率约为20%时,葡萄糖和葡萄糖酸的选择性约分别为23.3%和25.7%,并且该催化剂具有良好的循环使用性能.与·OH类似,CuSO_4催化过硫酸钾生成的·SO_4~?自由基也能够有效转化纤维二糖,在纤维二糖转化率为20%时,葡萄糖和葡萄糖酸的选择性分别为36.6%和39.9%.利用这种·OH和·SO_4~?自由基氧化的方法,也能够在较低温度下(333 K)解聚纤维素中的糖苷键.我们发展了H_2O_2浸渍预处理纤维浸渍预处理纤维素的方法,通过部分破坏纤维素糖苷键,提高了纤维素的水解活性.比如:处理后的纤维素在413 K条件下反应12 h,纤维素转化率和葡萄糖选择性分别达到约36.1%和42.5%.XRD结果表明,处理后的纤维素的晶体结构未发生明显的变化.FT-IR表征结果显示处理后的纤维素表面生成了大量的羧酸基团.     

钾盐催化纤维素快速热裂解机理研究

在红外辐射机理试验装置上进行了钾盐催化纤维素快速热裂解机理研究。试验发现，钾盐在抑制生物油生成的同时，促进了炭和气体的生成。结合反应前后金属盐电镜图以及生物油和焦炭中金属离子质量分数的检测，证实钾盐的催化作用主要发生在固相中，以离子形式选择性催化了不同类别的反应，加速了分子断键过程中的裂变和歧化反应。在抑制左旋葡聚糖生成的同时，促进了糖类以外产物的形成，提高了生物油中乙醇醛、乙醛以及小分子的醇类、酮醛类化合物的数量。     

快速准确书写糖基材料中基元结构的规律

在生命活动中发挥重要作用的糖类物质,因其结构相对稳定而广泛存在于自然界。随着对重要糖类化合物结构的认识,糖基材料越来越受到化学、生物医学、材料学领域的关注,相关研究不断深入。但在许多出版物中,其结构的书写、表达方式时常出现不当甚至错误,容易引起混乱。本文从分析环己烷的构型构象式出发,依次推导常见单糖、低聚糖、多糖结构单元的书写方法,如：葡萄糖、纤维二糖、麦芽糖、蔗糖、纤维素、淀粉、甲壳素、壳聚糖等。并总结相关规律,以便读者能够识别、分辨现行刊物中相关结构的正确性与准确度,并在撰稿时能够正确、准确、快速地书写相关糖类物质的结构式。     

醋酸丁酸纤维素合成研究

以纤维素为原料,乙酐、正丁酸为酰化剂,浓硫酸为催化剂,合成了醋酸丁酸纤维素。FT-IR分析证实了酯化产物的生成。采用冰醋酸、NaOH、浓H2SO4、乙二胺等前处理方法对纤维素进行预处理,应用XRD和粘度法表征了产物的结晶结构和聚合度,结果表明冰醋酸处理法较好。适宜的合成条件为:纤维素10g、催化剂用量0.25mL、乙酐/正丁酸摩尔比1∶5、酯化反应温度70℃、酯化反应时间1h。     

纤维二糖与葡萄糖催化转化制备乙二醇(英文)

选用纤维二糖作为探针分子,探索纤维素催化转化制备乙二醇过程的反应路径.分别考察了纤维二糖和葡萄糖在双组分催化剂H2WO4和Ru/C下的催化反应活性.结果表明,乙二醇不仅来自于纤维二糖水解产物葡萄糖的逆羟醛缩合作用,同时也可以来自于纤维二糖的直接逆羟醛缩合过程.而且,纤维二糖的直接逆羟醛缩合作用对糖苷键的水解也有一定的促进作用.比较发现,钨基催化剂作用下纤维二糖的逆羟醛缩合反应活性比葡萄糖要低,因此乙醇醛可以缓慢产生并在Ru/C催化剂上迅速加氢生成乙二醇.使得以纤维二糖作为原料比以葡萄糖作为原料时获得更高的乙二醇收率.     

纤维二糖与葡萄糖催化转化制备乙二醇(英文)

选用纤维二糖作为探针分子,探索纤维素催化转化制备乙二醇过程的反应路径.分别考察了纤维二糖和葡萄糖在双组分催化剂H2WO4和Ru/C下的催化反应活性.结果表明,乙二醇不仅来自于纤维二糖水解产物葡萄糖的逆羟醛缩合作用,同时也可以来自于纤维二糖的直接逆羟醛缩合过程.而且,纤维二糖的直接逆羟醛缩合作用对糖苷键的水解也有一定的促进作用.比较发现,钨基催化剂作用下纤维二糖的逆羟醛缩合反应活性比葡萄糖要低,因此乙醇醛可以缓慢产生并在Ru/C催化剂上迅速加氢生成乙二醇.使得以纤维二糖作为原料比以葡萄糖作为原料时获得更高的乙二醇收率.     

Mechanism of Formation and Consequent Evolution of Active Cellulose during Cellulose Pyrolysis

An intermediate product that was yellow, soluble, and solid was obtained in a high-radiation flash pyrolysis reactor. Under two different radiant heat fluxes, the yields tended to both increase initially until achieving a steady state, and then increase again with the progress of reaction. The compositional analysis of the yellow product was performed on high performance liquid chromatography (HPLC). It was indicated that the product mainly consisted of oligosaccharides, glucose, levoglucosan, methylglyoxal and so on. The compounds including oligosaccharides such as cellobiose and cellotriose, and monosaccharides such as glucose were regarded as active cellulose. Under the higher heat flux, the relative yield of the active cellulose increased initially, followed by a decreasing trend, and achieved a maximum mass fraction of 68% (w) in the soluble yellow product. The oligosaccharides with higher degree of polymerization (DP) were the primary components. Under the lower heat flux the yield of active cellulose was relatively lower, achieving a maximum of about 57% (w), and more saccharides with lower DP were contained. It was suggested that active cellulose was quite unstable at high temperature, and easily decomposed into saccharides with lower DP, even char, volatiles, and gaseous products. Finally an improved mechanism was proposed to describe the reaction route of formation and consequent evolution of active cellulose during cellulose pyrolysis.     

Cellulose hydrolysis using zinc chloride as a solvent and catalyst

Cellulose gel with < 10% of crystallinity was prepared by treatment of microcrystalline cellulose, Avicel, with zinc chloride solution at a ratio of zinc chloride to cellulose from 1.5 to 18 (w/w). The presence of zinc ions in the cellulose gels enhanced the rate of hydrolysis and glucose yield. The evidence obtained from X-ray diffraction, iodine absorption experiments; and Nuclear Magnetic Resonance spectra analysis suggested the presence of zinc-cellulose complex after Avicel was treated with zinc chloride. Zinc-cellulose complex was more susceptible to hydrolysis than amorphous cellulose. Under the experimental condition, cellulose gels with zinc ions were hyrolyzed to glucose with 95% theoretical yield and a concentration of 14% (w/v) by cellulases within 20 h. The same gel was hydrolyzed by acid to glucose with 91.5% yield and a concentration of 13.4% (w/v).     

Cellulose hydrolysis under extremely low sulfuric acid and high-temperature conditions

The kinetics of cellulose hydrolysis under extremely low acid (ELA) conditions (0.07 wt%) and at temperatures >200°C was investigated using batch reactors and bed-shrinking flow-through (BSFT) reactors. The maximum yield of glucose obtained from batch reactor experiments was about 60% for α-cellulose, which occurred at 205 and 220°C. The maximum glucose yields from yellow poplar feedstockswere substantially lower, falling in the range of 26–50%. With yellow poplar feedstocks, a large amount of glucose was unaccounted for at the latter phase of the batch reactions. It appears that a substantial amount of released glucose condenses with nonglucosidic substances. in liquid. The rate of glucan hydrolysis under ELA was relatively insensitive to temperature in batch experiments for all three substrates. This contradicts the traditional concept of cellulose hydrolysis and implies that additional factors influence the hydrolysis of glucan under ELA. Inexperiments using BSFT reactors, the glucose yields of 87.5, 90,3, and 90.8% were obtained for yellow poplar feedstocks at 205, 220, and 235°C, respectively. The hydrolysis rate for glucan was about three times higher with the BSFT than with the batch reactors. The difference of observed kinetics and performance data between the BSFT and the batch reactors was far above that predicted by the reactor theory.     

Thermal Degradation of Cotton Cellulose

The thermal degradation of cotton cellulose treated with chemical mixtures containing P and N was studied by thermal analysis, infrared spectroscopy, Char yield and limiting-oxygen-index (LOI). Our experiments demonstrated the following facts. The temperatures and activation energies of pyrolysis were lower for cotton cellulose treated with flame retardants than those for untreated samples and the values of Char yield and LOI were greater for treated cotton than those for untreated one. This revised version was published online in August 2006 with corrections to the Cover Date.     

[AEIM]Cl的合成及微波溶解微晶纤维素

以氯丙烯和N-乙基咪唑为原料合成了离子液体氯化1-烯丙基-3-乙基-咪唑盐([AEIM]Cl),利用FT-IR和¹HNMR对其化学结构进行了表征。采用微波加热法溶解微晶纤维素(MCC),考察 [AEIM]Cl对纤维素的溶解性能。研究了NaOH、微波和高压等3种预处理方式对微晶纤维素的相对结晶度、聚合度及溶解率的影响。利用FT-IR、XRD、TGA和SEM分别对溶解后得到的再生纤维素的化学结构、晶型变化、热稳定性及表观形貌进行测试与分析。结果表明,合成的离子液体是目标产物,对微晶纤维素表现出很好的溶解能力,且高温高压条件下15％的NaOH水溶液对微晶纤维素处理后,得到的纤维素相对结晶度最小,聚合度最低,溶解率最高。溶解过程中纤维素没有发生衍生化反应,溶解后得到的再生纤维素的相对结晶度和微晶尺寸变小,热稳定性降低。     

钾元素对生物质主要组分热解特性的影响

采用热重-红外联用仪对松木及生物质主要化学组分半纤维素、纤维素、木质素的热解特性及钾元素对其热解特性的影响进行了研究.结果表明,半纤维素、纤维素、木质素发生热解的主要温度分别为200~350 ℃、300~365 ℃和200~600 ℃;半纤维热解产物中CO、CO₂较多;纤维素热解产物中LG和醛酮类化合物最多;木质素热解主要形成固体产物,气体中CH₄相对含量较高.三种组分共热解过程中发生相互作用使热解温度提高、固体产物增加,气体中CO增加而CH₄减少.添加K₂CO₃后半纤维素和纤维素热解温度区间向低温方向移动,固体产率提高.K对纤维素作用最明显,CO、CO₂气体与固体产物产率明显增加,醛酮类和酸类物质的产率降低;木质素受K影响相对较小,热解固体产物略有增加,挥发分中H₂O和羰基物质增加;三组分共热解减弱了钾元素的催化作用.     

Determination of neutral oligosaccharides in vegetables by matrix-assisted laser desorption/ionization mass spectrometry

In this work, matrix-assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI–TOF–MS) was used for characterization of oligosaccharides in some vegetable samples (Jerusalem artichoke, red onion, glucose syrup from potatoes). The selection of suitable matrix has critical importance for quality of MALDI–TOF spectra. Therefore six selected matrices (2,5-dihydroxybenzoic acid, 2,4,6-trihydroxyacetophenone, -cyano-4-hydroxycinnamic acid, 2-(4-hydroxyphenylazo)benzoic acid, 3-aminoquinoline and sinapinic acid) were tested. The optimization of experimental conditions was carried out for two model carbohydrates that are important in food chemistry—inulin and starch. The experiments were performed in both positive linear and reflectron mode. The signals of the standard samples in reflectron mode were weak and repeatability of the measurements was lower than in linear mode. 2,4,6-Trihydroxyacetophenone for inulin and 2,5-dihydroxybenzoic acid for starch were found as the best matrices. Therefore, the real samples were analyzed with these two matrices in linear mode. The distribution of oligosaccharides from Jerusalem artichoke showed the degree of polymerization (DP) of the oligosaccharides in the range from 2 to 25. Red onion contained the saccharides with DP from 1 to 14. Glucose syrup from potatoes had DP from 2 to 48. MALDI–TOF–MS was found more sensitive for detection of oligosaccharides than the chromatographic methods used for the some purpose.     

Characterization of the water-insoluble pyrolytic cellulose from cellulose pyrolysis oil

Water-insoluble pyrolytic cellulose with similar appearance to pyrolytic lignin was found in cellulose fast pyrolysis oil. The influence of pyrolysis temperature on pyrolytic cellulose was studied in a temperature range of 300–600 °C. The yield of the pyrolytic cellulose increased with temperature rising. The pyrolytic cellulose was characterized by various methods. The molecular weight distribution of pyrolytic cellulose was analyzed by gel permeation chromatography (GPC). Four molecular weight ranges were observed, and the M_w of the pyrolytic cellulose varied from 3.4 × 10³ to 1.93 × 10⁵ g/mol. According to the elemental analysis (EA), the pyrolytic cellulose possessed higher carbon content and lower oxygen content than cellulose. Thermogravimetric analysis (TGA) indicated that the pyrolytic cellulose underwent thermo-degradation at 127–800 °C and three mass loss peaks were observed. Detected by the pyrolysis gas chromatography–mass spectrometry (Py-GC/MS), the main pyrolysis products of the pyrolytic cellulose included saccharides, ketones, acids, furans and others. Fourier transforms infrared spectroscopy (FTIR) also demonstrated that the pyrolytic cellulose had peaks assigned to CO stretching and glycosidic bond, which agreed well with the Py-GC/MS results. The pyrolytic cellulose could be a mixture of saccharides, ketones, and their derivatives.     

Study on the Pyrolysis of Cellulose for Bio-Oil with Mesoporous Molecular Sieve Catalysts

Mesoporous materials possess a hexagonal array of uniform mesopores, high surface areas, and moderate acidity. They are one of the important catalysts in the field of catalytic pyrolysis. In this paper, mesoporous materials of Al-MCM-41, La-Al-MCM-41, and Ce-Al-MCM-41 were synthesized, characterized, and tested as catalysts in the cellulose catalytic pyrolysis process using a fixed bed pyrolysis reactor. The results showed that mesoporous materials exhibited a strong influence on the pyrolytic behavior of cellulose. The presence of these mesoporous molecular sieve catalysts could vary the yield of products, which was that they could decrease the yield of liquid and char and increase the yield of gas product, and could promote high-carbon chain compounds to break into low-carbon chain compounds. Mesoporous molecular sieve catalysts were benefit to the reaction of dehydrogenation and deoxidation and the breakdown of carbon chain. Further, La-Al-MCM-41 and Ce-Al-MCM-41 catalysts can produce more toluene and 2-methoxy-phenol, as compared to the non-catalytic runs.     

Xylan hydrolysis in zinc chloride solution

Xylan is the major component of hemicellulose, which consists of up to one-third of the lignocellulosic biomass. When the zinc chloride solution was used as a pretreatment agent to facilitate cellulose hydrolysis, hemicellulose was hydrolyzed during the pretreatment stage. In this study, xylan was used as a model to study the hydrolysis of hemicellulose in zinc chloride solution. The degradation of xylose that is released from xylan was reduced by the formation of zinc-xylose complex. The xylose yield was >90% (w/w) at 70°C. The yield and rate of hydrolysis were a function of temperature and the concentration of zinc chloride. The ratio of zinc chloride can be decreased from 9 to 1.3 (w/w). At this ratio, 76% of xylose yield was obtained. When wheat straw was pretreated with a concentrated zinc chloride solution, the hemicellulose hydrolysate contained only xylose and trace amounts of arabinose and oligosaccharides. With this approach, the hemicellulose hydrolysate can be separated from cellulose residue, which would be hydrolyzed subsequently to glucose by acid or enzymes to produce glucose. This production scheme provided a method to produce glucose and xylose in different streams, which can be fermented in separated fermenters.