青霉素酰化酶在含铁MCM-41介孔分子筛上的固定化研究

制备了具有长程有序结构、孔径分布狭窄的含铁MCM-41介孔分子筛，利用直接法和共价结合法将青霉素酰化酶固定在分子筛表面。结果表明，两种方法制备的固定化酶对青霉素G水解反应的表观活性分别为782U/g和256U／g；经6次连续操作使用，二者保持初始活性的49．4％和81．2％，后者的操作稳定性好于前者。共价结合法制备的固定化酶活性较低，是由于Fe—MCM-41表面修饰后比表面积和孔径明显减小所致。     

青霉素酰化酶在甲基丙烯酸缩水甘油酯共聚物上的固定化

 用共价键合法将青霉素酰化酶固定化在珠状多孔的甲基丙烯酸缩水甘油酯（GM）共聚物上，研究了固定化反应时间、温度、pH值和酶液用量对固定化青霉素酰化酶的表观活性、表观偶联效率、活性回收及稳定性的影响．将GM共聚物载体加入到磷酸缓冲液（0．1mol／L，pH10．8）与青霉素酰化酶液（每克干载体用酶液1ml）的混合溶液中，在30℃下反应72h，单位质量（干重）固定化酶的表观活性为348U／g，表观偶联效率为66．7％，活性回收为31．7％．     

乙烯基Ia3d介孔硅分子筛的环氧化及其固定化青霉素酰化酶(英文)

采用直接共聚法合成表面含有乙烯基的具有立方相Ia3d结构的介孔硅分子筛(V-ClMS),然后对乙烯基团进行环氧化制备得到表面环氧基功能化的介孔硅分子筛(E-CIMS),采用X射线衍射、N2吸附-脱附、透射电镜、热重分析和13C固体核磁共振对制备的介孔硅分子筛进行了表征.结果表明,表面含有乙烯基的V-ClMS介孔硅分子筛能被一步成功合成,并易于发生环氧化而获得表面环氧基功能化的E-CIMS介孔硅分子筛.将E-CIMS介孔硅分子筛作为载体用于固定化青霉素G酰化酶(PGA),研究了表面环氧基团对固定化PGA初活性和操作稳定性的影响.结果表明,随着表面环氧基团数量的增加,介孔硅分子筛孔径减小,表面疏水性增加,导致载酶量和初活性减小.但介孔硅分子筛表面适量的环氧基团能增强E-CIMS介孔硅分子筛与PGA之间的相互作用,从而提高固定化PGA的操作稳定性.     

环氧基功能化SBA-15介孔分子筛的制备、表征及其固定化青霉素酰化酶

利用表面嫁接法和乙烯基环氧化法制备了环氧基团功能化介孔分子筛G-SBA-15和O-SBA-15,并对其结构和表面性质进行了表征.结果表明,G-SBA-15和O-SBA-15均具有良好的长程有序结构,二者环氧基团的含量分别为0.78 mmol/g和0.37 mmol/g,在O-SBA-15表面还存在一定数量的乙烯基基团.G-SBA-15和O-SBA-15用于固定青霉素酰化酶(pen ic illin G acylase,PGA),固定化酶PGA/G-SBA-15和PGA/O-SBA-15在37℃时水解青霉素G钾制备6-氨基青霉烷酸(6-APA)的表观活性分别为1075 IU/g和1761 IU/g.PGA/G-SBA-15经4次使用后表观活性趋于稳定,经10次使用后保持其初始活性的83.7%.PGA/O-SBA-15在重复使用中,表观活性出现持续衰减,10次使用后保持其初始活性的51.6%,PGA/G-SBA-15的操作稳定性明显好于PGA/O-SBA-15.     

功能基化聚丙烯酸甲酯固定化青霉素酰化酶

合成了一系列大孔丙烯酸甲酯－二乙烯苯交联共聚物,经酰肼化、叠氨后固定青霉素酰化酶,考察了反应条件对固定化酶的影响,当交联剂用量为３０％,至孔剂量为１３０％,混合致孔剂（正庚烷与乙酸乙酯）中正庚烷的质量分数为５５％时,所制的载体经活化后得到的固定化酶酶活较高,为９５ｕ／ｇ（湿）,用分批式反应器连续水解青霉素Ｇ钾盐,使用６３批次后仍保留酶活７９．４％。     

不同介孔材料固定青霉素酰化酶的稳定性研究

介孔材料由于具有在2～30nm之间可调的纳米级规则孔道、大比表面积和强吸附性能而成为固定化酶的优良载体．将酶固定于介孔材料的孔道中制备成的固定化酶与溶液酶相比,有易于与产物分离,并可回收和反复使用,可降低生产成本,减少酶的自水解和保持酶的活性．青霉素酰化酶（Penicillin acylase,PGA,EC．3．5．1．11）又称为青霉素酰胺酶或青霉素氨基水解酶,该酶属于球蛋白,分子量较大,由2个亚基组成：分子量为19500的含有侧链结合位点的亚基和分子量为60000的含有催化位点的亚基．     

高分子载体材料对青霉素酰化酶的固定化作用

介绍了天然高分子材料和合成高分子材料对青霉素酰化酶的固定化作用,着重讨论了高分子材料的制备、性质及其表面修饰对固定化酶活性和使用稳定性的影响。     

6-APA合成反应中固定化青霉素酰化酶载体及固定化研究进展

青霉素酰化酶 ( penicillin amidase E.C.3.5 .1 .1 1 ,简称 PA)能催化水解青霉素产生 6-氨基青霉烷酸 ( 6- aminopenicillanic acid,简称 6- APA)、水解扩环酸产生 7-氨基 - 3-脱乙酰氧基头孢烷酸 ( 7-aminodesacetoxycephalosporanic acid,简称 7- AD-CA) .该酶还能以 6- APA或 7- ADCA为母核 ,催化合成各种不同的半合成青霉素 (如氨基苄青霉素、羟氨苄青霉素等 )或头孢菌素 .由于半合成青霉素在效力与临床价值上优于青霉素 ,而青霉素又很容易通过发酵而大量生产 ,因此近几十年来 ,有关青霉素 G水解生产 6- APA的研究一直是一个…     

亲水性交联聚合物载体的合成及其固定化青霉素酰化酶

选用含环氧基团的甲基丙烯酸缩水甘油酯(GMA)和亲水性的N-乙烯吡咯烷酮(NVP)单体,以N,N′-亚甲基双丙烯酰胺(MBAA)为交联剂,甲酰胺作致孔剂,通过反相悬浮聚合技术成功合成了一系列大孔、珠状GMA-NVP-MBAA三元共聚物载体.N-乙烯吡咯烷酮介入共聚物体系,使共聚物载体具有较强的亲水性,有利于青霉素酰化酶的固定化.通过调节交联剂的用量和单体NVP与GMA的比例,可以调节共聚物载体的孔结构与表面性能.用合成的平均孔径为15.7nm、表面环氧基含量1.11mmol·g-1亲水性珠状载体固定青霉素酰化酶,固定化酶水解青霉素G钾盐的活性达491U·g-1;在4℃保存30d,活性保持不变.经4次使用后活性达到稳定(444U·g-1),再经14次使用后,活性没有明显变化.     

聚丙烯酸载体用于青霉素酰化酶的固定

以反应性单体丙烯酸和交联剂二乙烯基苯,以石油醚为致孔剂,通过悬浮聚合制备固定化酶的载体,并用于对青霉素酰化酶的固定。研究了丙烯酸与二乙烯基苯以不同摩尔比对青霉素酰化酶固定活性的影响,以及悬浮聚合时水油相比例的不同所合成的载体对固定化酶性能的影响。当丙烯酸和二乙烯基苯摩尔比为84.2:4时合成的载体固定青霉素酰化酶的酶活为2784U/g,而水油相比为2.75:1（丙烯酸和二乙烯基苯摩洋比为84.2:5）时固定青霉素酰化酶活达到2183U/g。固定青霉素酰化酶可使青霉素转化,得到半合成青霉素的中间体6-氨基青霉烷酸,由此可制成高效、广谱、服用方便的新青霉素。     

MCM-41分子筛的改性、表面结构与吸附性质的研究

用三甲基氯硅烷、二甲基二氯硅烷、甲基三氯硅烷、四氯化硅与甲基碘改性高硅MCM-41中孔分子筛。XRD,^2^9SiMASNMR,^1^3CMASNMR,以及N~2、水与环己烷吸附的表征,显示改性不同程度地改变了分子筛的表面组成与结构,减小孔径,增加孔壁厚度,因而影响吸附行为,减小吸附容量。硅烷化减少了MCM-41的表面硅羟基含量,增加其疏水性。用CH~3I改性使孔径减小1.4nm,而硅羟基含量并未显著减少。硅烷化以及用CH~3I改性可提高MCM-41分子筛的热稳定性。SiCl~4的改性作用相对不明显。样品的水及环己烷吸附容量与其表面硅羟基含量呈现不同的线性关系,揭示高硅MCM-41分子筛表面吸附中心的本性。     

外围为柔性链状取代基团Ni-酞菁配合物的合成及其在MCM-41中的装载

合成了外围具有柔性链状基团的2（3）,9（10）,16（17）,23（24）-四-（N,N-二乙胺基乙氧基）Ni-酞菁配合物（2）．以正硅酸乙酯为硅源,十六烷基三甲基溴化铵为模板剂,水热法将该Ni-酞菁配合物（2）装载到MCM-41中．利用UV-Vis-NIR,FT-IR,XRD,TEM,FESEM及N2吸附-脱附等温线对制备的样品进行了表征．研究表明制备的样品中Ni-酞菁配合物（2）主要以单体和二聚体的形式存在于MCM-41中．通过不同制备酞菁浓度的装载研究表明,较高制备酞菁浓度有利于制备结晶度及孔道有序性较高的介孔分子筛样品．     

Synthesis, characterization, and catalytic properties of stable mesoporous molecular sieve MCM-41 prepared from zeolite mordenite

Mesoporous molecular sieves (denoted as M-MCM-41) with ordered hexagonal structure have been successfully synthesized from the assembly of precursors from preformed zeolite Mordenite with CTAB surfactant micelle in alkaline media. The samples were characterized by XRD, N₂ adsorption, IR and DTG. The materials exhibit highly hydrothermal stability, as compared with conventional MCM-41. Characterization results indicate that the mesoporous walls of M-MCM-41 contain the secondary building units similar to those in microporous crystal of zeolite Mordenite. In catalytic dealkylation of C10⁺ aromatic hydrocarbon, M-MCM-41 shows higher activities in comparison with Mordenite and MCM-41, which would be ascribed to the combination of advantages of both MCM-41 (large pores) and Mordenite (strong acidity). Furthermore, this synthesis strategy could be used as a new general method for the preparation of hydrothermally stable mesoporous aluminosilicate materials under alkaline conditions.     

Epoxidation of cyclohexene on modified Ti-containing mesoporous MCM-41

Ti-MCM-41, B-Ti-MCM-41 and Ti-grafted MCM-41 were synthesized, characterized and studied in the epoxidation of cyclohexene. The synthetic methods and the effect of water in the oxidant are discussed.     

Hydrogenation of naphthalene on noble-metal-containing mesoporous MCM-41 aluminosilicates

Aromatic saturation of oil fractions is a key process in the refining industry due to increasing demand for cleanest distillates with superior performances. In this study, the behavior of different catalysts containing 1 wt.% of noble-metal inside a mesoporous MCM-41 (Si:Al=20) framework was investigated in the hydrogenation of naphthalene, as preliminary step to investigate bimetallic catalysts. While at atmospheric pressure only Rh and Pd showed a low hydrogenation activity, in the tests performed at 6.0 MPa the catalytic activity grew, exhibiting the following order: Pt>RhPd>>>Ru≈Ir. However, all the catalysts required a large H₂ excess, to avoid a decrease in hydrogenation and ring-opening activity, and gave rise to the best performance for a contact time of 6.8 s, favouring at lower values the partial hydrogenation to tetralin and at higher values cracking reactions. Finally, all the catalysts showed low thio-tolerance, with significant deactivation already feeding 100 ppm wt. of dibenzothiophene (DBT), with a partial reversibility only for the Pt-containing catalyst (CAT 3).     

自制Ti/W-MCM-41介孔分子筛催化制备乳酸戊酯

采用自制的介孔分子筛Ti/W-MCM-41催化乳酸与正戊醇的酯化反应,合成了乳酸正戊酯;利用红外光谱仪分析了催化剂的化学特征,考察了分子筛的WO3质量分数、催化剂用量、醇酸物质的量比、反应时间、催化剂重复使用性能等因素对目标产物酯化率的影响.结果表明,在nSi∶nTi=30∶1,WO3质量分数10%,550℃下焙烧6h条件下制得的催化剂具有良好的催化性能;其催化合成乳酸正戊酯适宜的反应条件为:0.2mol乳酸,催化剂用量0.5g,n(正戊醇)∶n(乳酸)=1.6∶1,反应时间100min,酯化率可达94.4%.该催化剂使用7次酯化率仍可达86.6%.     

萘在介孔分子筛MCM-41与SBA-15上的吸附特性研究

对低浓度气相萘在两种常见介孔分子筛MCM-41和SBA-15上的吸附特性进行研究。得到了萘在两种吸附剂上的吸附等温线和不同初始浓度下的穿透曲线,并分别与吸附等温线模型(Langmuir、Freundlich、D-R)和恒定浓度波动力学模型进行了拟合。结果表明, Langmuir模型能很好描述低浓度气相萘的吸附等温线(R²均在99%以上);具有微孔结构的SBA-15对萘的吸附能力要优于仅具备介孔结构的MCM-41。动力学模型在初始浓度较低时能较好地预测萘在吸附剂上的穿透曲线,且在SBA-15上的相关系数高于MCM-41;萘在2.76 mol/L时具有较大介孔的SBA-15的总传质系数K_a更高,表明萘在SBA-15上的总传质阻力更低,更能较快达到传质平衡。     

Preparation of mesoporous molecular sieve based hydrocracking catalysts

A series of hydrocracking catalysts based on mesoporous molecular sieves MCM-41 and SBA-15 with different silica to alumina ratios was prepared. Nickel and molybdenum were used as active metals to impregnate the extrudates prepared by using molecular sieves. The catalysts were characterized for physical and chemical properties and evaluated for the hydrocraking of desulfurised vacuum gas oil. The conversion of DS-VGO was lower as compared to that of the catalyst based on USY zeolite. However, the gas yield was lower in case of mesoporous materials based catalysts.     

The Synthesis and Characteristics of Vanadoaluminosilicate MCM-41 Mesoporous Molecular Sieves

A series of vanadoaluminosilicate MCM-41 mesoporous molecular sieves with various compositions have been hydrothermally synthesized. Hexadecyltrimethylammonium bromide was used as a surfactant in the synthesis. The samples were characterized with nitrogen sorption, X-ray diffraction, differential thermal analysis, thermogravimetric analysis, Fourier transform-Infrared spectroscopy, UV-visible spectroscopy, scanning electron microscopy, transmission electron microscopy, and solid state NMR. The solid products had the MCM-41 structure and contained only atomically dispersed vanadium and aluminum consistent with framework vanadium and aluminum. The samples were hydrophobic and contained large amount of surfactant in the as-synthesized samples. The surfactant could be removed upon calcination at 450°C. N₂ sorption measurements and TEM demonstrate the high mesoporosity of [V, Al]-MCM-41. The incorporation of vanadium and aluminum into MCM-41 decreased the surface area to some extent. The morphologies of all the samples were the agglomerate of plates. ²⁹Si MAS NMR shows that the pore wall is amorphous. ²⁷Al MAS NMR shows that all of aluminum species were tetrahedrally coordinated even after calcination at 550°C.     

介孔分子筛MCM-41的硅烷化改性及吸附性能研究

高硅分子筛MCM-41具有均匀的中孔孔径分布、较大的比表面积(>900m2/g)[1-2],应用前景广阔.已在硅基分子筛的基础上合成了各种含有杂原子分子筛、金属氧化物分子筛、有机官能团分子筛[3-8].改变介孔MCM-41分子筛的表面组成可以较好地调节其吸附性能[9].本文以直接反应的方法用三甲基氯硅烷来修饰MCM-41.通过XRD、红外吸收光谱和比表面和孔隙率测定对样品进行了表征,并分别对改性前后样品进行了水与苯的吸附性能研究.