固定化对恶臭假单胞菌腈水合酶催化特性的影响

酶法代替铜催化法使丙烯腈转化制内烯酰胺的研究,70年代起在国外开始进行.近年来,国内也相继开展了这方面的工作.他们筛选得到的恶臭假单胞菌JP-1具有较高腈水合酶活力,其完整细胞的腈水合酶催化特性也已进行了研究.本文研究了采用海藻酸钙包埋法制备的恶臭假单胞菌固定化细胞的酶学性质.     

腈水合酶的发酵及酶学性质

红球菌Rhodococceus rhodochrous J1在含有脲和钴的培养基中发酵产生腈水合酶,可以催化丙烯腈水合为丙烯酰胺。调节培养条件使发酵液的酶活力达到6150u／ml。温度30℃,反应体系呈中性酶活性很高并且稳定。底物浓度,酶浓度,反应时间的正交实验表明,底物丙烯腈是显著因子,最佳浓度7％,超过此浓度酶会失活;1min内,水合反应转化率可达80％。浓度超过15％的丙烯酰胺会抑制酶的活性。     

微生物腈水合酶的研究进展

腈水合酶 ( Nitrile Hydratase E C4.2 .1 .84,简称 NHase)是一种微生物酶 ,它可催化多种腈化合物水解生成酰胺[1] ,酰胺在酰胺酶 ( Amidase)的作用下 ,进一步转化生成羧酸及氨气 .这与腈水解酶( Nitrilase)催化腈水解一步生成羧酸的途径有所不同 .微生物 NHase可广泛地应用于氨基酸、酰胺、羧酸及其衍生物的合成 . 1 980年 ,Asano等人[2 ] 首次发现微生物 Rhodocococcus sp. N- 774NHase可降解有毒的乙腈 ,不久即被成功地应用于工业生产丙烯酰胺 .近来 ,NHase也被用于制备手性药物 ,如 Gilligan 等 [3 ]成功地用 Rhodocococcus equ…     

腈水合酶及其在丙烯酰胺生产中应用的研究进展

对近年来国内外腈水合酶的研究进行了回顾,就腈水合酶的种类、分布、生理合成调节、结构特点、反应机理、光敏性、热稳定性等方面及影响酶活性的几个主要因素做了具体的阐述.并进一步探讨了其在工业中的应用和发展,提出了一些建议和设想.     

强碱阴离子交换树脂催化合成羟丙腈

使用强碱阴离子交换树脂作为丙烯腈 (AN) 水合反应的催化剂制备羟丙腈 (HPN)。考察了反应时间、温度、催化剂类型、催化剂用量及投料比对羟丙腈产率的影响。优化的反应条件为: 温度50℃，时间6h，催化剂用量/丙烯腈 (wt) 取1.5∶1，丙烯腈/H2O (wt) 取11∶6，催化剂为201×7。在此条件下羟丙腈的摩尔产率达85%，催化剂经重复使用12次，活性没有降低。     

游离细胞法制备丙烯酰胺

采用新工艺游离细胞法半连续操作制备丙烯酰胺,探讨了反应的最佳条件。结果表明,在温度高于20℃时酶易失活,底物丙烯腈体积分数高于4％和产物丙烯酰胺质量浓度高于300g／L时,将对酶活性产生强烈的抑制作用;在较低温度下,采用底物流加及酶流加方法能保持较高的酶活性。当菌悬液体积分数为10％、反应温度为20℃、流动加入时,最终生成丙烯酰胺的质量浓度为366g/L,与菌悬液一次性加入相比,丙烯酰胺质量浓度提高23％。     

微乳液中脂肪酶和含明胶的微乳液凝胶中固定化脂肪酶的催化特性

在双2-乙基己基琥珀酸酯磺酸钠(AOT)油包水微乳液中Calytical脂肪酶催化月桂酸和戊醇的酯化反应动力学研究表明,反应符合乒乓(BiBi)机制.表观速率常数k_m酸=0.13518mol/L,k_m醇=0.22423mol/L,最大反应速度v_max=1.3873×10^-5mol/(L·min·mg).将该脂肪酶固定于含明胶的微乳液凝胶(MBGs)中,制得固定化脂肪酶,含酶MBGs在非极性溶剂中可作为固相催化剂,并研究了其在辛烷中催化酯化的性能.所制得的含酶MBGs物理稳定性好,重复利用10次以上,其转化率仍达初始转化率的90%.     

菠萝蛋白酶催化大豆蛋白水解反应的热动力学

利用热活性检测仪测定了菠萝蛋白酶催化大豆蛋白水解反应的热功率-时间曲线,按照热动力学理论和对比进度法解析出不同温度、酸度时菠萝蛋白酶催化大豆蛋白水解反应的米凯利斯常数（K_m）和最大速率（V_max）,并建立了K_m与温度和酸度的关系式,从而获得酶催化反应的最适温度（314.63 K）和最适pH（6.99）. 在最适温度和最适pH条件下,测定了金属离子可逆竞争时菠萝蛋白酶催化大豆蛋白水解反应的热功率-时间曲线,对曲线进行处理,得到了酶催化反应的米凯利斯常数（K_m’）和最大速率（V_max’）. 建立了K_m’与金属离子浓度间的关系式,比较了金属离子对酶催化反应的激活或抑制效果.     

核糖核酸酶A在丁酸十二铵-环己烷反胶束溶液中的催化动力学

研究了核糖核酸酶A(RNaseA)在丁酸十二铵(DAB)-环己烷反胶束溶液中催化水解胞苷2',3'-环单磷酸酯的动力学,数据符合Michaelis-Menten酶催化机理.以k_cat/K_m表示酶催化活性时,Rnase A在反胶束溶液中的催化活性是在水溶液中的14～30倍.无论是固定DAB浓度还是固定H₂O与DAB浓度之比,随增溶水量的增加,k_cat/K_m呈下降趋势.     

不同催化体系下腈的水合反应研究进展

腈可用于构建新的碳-碳、碳-杂原子键,所得产物丰富多样.酰胺基团广泛存在于医药、农药和天然产物中,此外,酰胺还是有机合成反应中重要的中间体.在目前报道的酰胺类化合物的合成方法中,腈的水合反应已成为学术界和工业界最广泛使用的获得初级酰胺类化合物的方法之一.早期腈的水合反应中通常涉及强酸、强碱的使用,但在该类反应体系下,往...     

Acrylamide production in an ultrafiltration-membrane bioreactor using cells of Brevibacterium imperialis CBS 489-74

Both differential and integral UF-membrane reactors were tested for the bioconversion of acrylonitrile into acrylamide. Use was made of the commercially available flat membrane cell Amicon Mod.52 and the UF-membranes FS81PP, GR81PP, and YM100. The enzymatic reaction was catalyzed by the nitrile hydratase (NHase) present in resting cells of Brevibacterium imperialis CBS 489-74. The system was operated at 4°C and 10°C. Acrylonitrile concentration ranged from 50 to 500 mM. The membrane resistance to chemicals was complete at acrylonitrile and acrylamide concentrations up to 800 mM and 2 M, respectively. No rejection of solute was determined. Membranes totally retained the resting cells and no fouling was observed working with 2 and 16 mg of biocatalyst in stirred systems. Membrane compaction was apparently responsible for roughly 35% flux loss during the first 3–4 h of operation. The laboratory scale membrane bioreactor, continuously operating, allowed to show the dependence of enzyme deactivation on acrylonitrile concentration and process time. Substrate concentration higher than 100 mM were highly detrimental for NHase stability. The acrylamide yield reached in the multi-cycle process operating with 5.6 g/l of resting cells was 93.7% and the product concentration during roughly 450 h of bioconversion attained 8.3% (w/v). Decay of specific membrane flux was 98% of the initial value.     

Influence des solvants sur la copolymérisation de l'acrylamide avec l'acrylonitrile

The copolymerization of acrylamide with acrylonitrile was investigated in various solvents, which can be put into three groups according to their influence on molecular associations; (1) solvents autoassociated by hydrogen- bonds (acetic acid, methanol, water, dimethylformamide); (2) polar solvents which can associate with the NH group of acrylamide (acetonitrile, dioxane, acetone); (3) inert solvents (toluene, benzene, hexane). The reaction kinetics and the compositions of the copolymers are different for each group of solvents. The composition of copolymers formed in solvents of group 1 vary widely, depend- ing on the solvent. Copolymers formed in all solvents of group 2 have the same composition which is that of copolymers formed in bulk. The amount of acrylamide is highest in copolymers formed in inert solvents of group 3. Such parameters as the degree of conversion, the reaction temperature, the mode of initiation and the extent of dilution only slightly affect the composition of copolymers. Homopolymerizations of acrylamide and acrylonitrile were investigated in all solvent used.The results suggest that the effects of solvents on the copolymerization of acrylamide with acrylonitrile are consequences of the various modes of molecular association of acrylamide. The solvents affect the equilibrium between auto- association of acrylamide and its association with solvent and thereby affect the reactivity of the monomer.     

Substrate selectivity and conformational space available to bromoxynil and acrylonitrile in iron nitrile hydratase

Nitrile hydratase (NHase) is used in the commercial conversion of acrylonitrile to acrylamide. There are two main types of NHase: the iron containing and the cobalt containing NHase. They catalyze the conversion of a wide variety of nitriles to their corresponding amides. The Co-NHases are more robust and have wider substrate specificity than the Fe-NHase. We have used dihedral and positional variational Monte Carlo conformational searches to determine the conformational space available to acrylonitrile and bromoxynil bound to the iron in the active site of NHase. Dioxane is an Fe-NHase inhibitor, but has no effect on Co-NHase activity. Our conformational searches showed that although the dioxane restricts the conformational freedom of the iron coordinated acrylonitrile, there is enough room in the active site for both the acrylonitrile and dioxane. A conformational search of dioxane in the active site of Fe-NHase, in the absence of a substrate, revealed that the acrylonitrile and dioxane do not share the same space. We have also shown that if the function of the metal ions in NHases is to activate the nitrile by binding to it and acting as a Lewis acid, then the entrance and channel residues are most likely responsible for Fe-NHase's inability to hydrolize bromoxynil.     

碱催化合成N-羟甲基丙烯酰胺的动力学

N-羟甲基丙烯酰胺(N-MAM)具有可聚合的双键和可缩合的羟基,能进一步与其它烯烃化合物反应生成共聚物及交联产物,是一种有重要经济价值的水溶性功能高分子单体。     

Theoretical study on the gas phase reaction of acrylonitrile with a hydroxyl radical

The mechanism and kinetics of the reaction of acrylonitrile (CH(2)=CHCN) with hydroxyl (OH) has been investigated theoretically. This reaction is revealed to be one of the most significant loss processes of acrylonitrile. BHandHLYP and M05-2X methods are employed to obtain initial geometries. The reaction mechanism conforms that OH addition to C[double bond, length as m-dash]C double bond or C atom of -CN group to form the chemically activated adducts, 1-IM1(HOCH(2)=CHCN), 2-IM1(CH(2)=HOCHCN), and 3-IM1(CH(2)=CHCOHN) via low barriers, and direct hydrogen abstraction paths may also occur. Temperature- and pressure-dependent rate constants have been evaluated using the Rice-Ramsperger-Kassel-Marcus theory. The calculated rate constants are in good agreement with the experimental data. At atmospheric pressure with N(2) as bath gas, 1-IM1(OHCH(2)=CHCN) formed by collisional stabilization is the major product in the temperature range of 200-1200 K. The production of CH(2)CCN and CHCHCN via hydrogen abstractions becomes dominant at high temperatures (1200-3000 K).     

Nitrile hydration by thiolate- and alkoxide-ligated Co-NHase analogues. Isolation of Co(III)-amidate and Co(III)-iminol intermediates

Nitrile hydratases (NHases) are thiolate-ligated Fe(III)- or Co(III)-containing enzymes, which convert nitriles to the corresponding amide under mild conditions. Proposed NHase mechanisms involve M(III)-NCR, M(III)-OH, M(III)-iminol, and M(III)-amide intermediates. There have been no reported crystallographically characterized examples of these key intermediates. Spectroscopic and kinetic data support the involvement of a M(III)-NCR intermediate. A H-bonding network facilitates this enzymatic reaction. Herein we describe two biomimetic Co(III)-NHase analogues that hydrate MeCN, and four crystallographically characterized NHase intermediate analogues, [Co(III)(S(Me2)N(4)(tren))(MeCN)](2+) (1), [Co(III)(S(Me2)N(4)(tren))(OH)](+) (3), [Co(III)(S(Me2)N(4)(tren))(NHC(O)CH(3))](+) (2), and [Co(III)(O(Me2)N(4)(tren))(NHC(OH)CH(3))](2+) (5). Iminol-bound 5 represents the first example of a Co(III)-iminol compound in any ligand environment. Kinetic parameters (k(1)(298 K) = 2.98(5) M(-1) s(-1), ΔH(?) = 12.65(3) kcal/mol, ΔS(?) = -14(7) e.u.) for nitrile hydration by 1 are reported, and the activation energy E(a) = 13.2 kcal/mol is compared with that (E(a) = 5.5 kcal/mol) of the NHase enzyme. A mechanism involving initial exchange of the bound MeCN for OH- is ruled out by the fact that nitrile exchange from 1 (k(ex)(300 K) = 7.3(1) × 10(-3) s(-1)) is 2 orders of magnitude slower than nitrile hydration, and that hydroxide bound 3 does not promote nitrile hydration. Reactivity of an analogue that incorporates an alkoxide as a mimic of the highly conserved NHase serine residue shows that this moiety facilitates nitrile hydration under milder conditions. Hydrogen-bonding to the alkoxide stabilizes a Co(III)-iminol intermediate. Comparison of the thiolate versus alkoxide intermediate structures shows that C≡N bond activation and C═O bond formation proceed further along the reaction coordinate when a thiolate is incorporated into the coordination sphere.     

In situ Fourier transform infrared spectroscopy as an efficient tool for determination of reaction kinetics

The performance of new FTIR-based monitoring technology to representatively determine reaction kinetics has been demonstrated on an example of homogeneously catalyzed liquid-phase sucrose hydrolysis to fructose and glucose. The reaction kinetics were investigated by using the ReactIR 1000 reaction analysis system, which enables determination of the component concentration from its characteristic FTIR spectrum. During the sucrose inversion, the ReactIR 1000 instrument connected to a computer controlled standard glass batch reactor provided the required operating conditions and information about the component concentration in real-time. We have studied the influence of hydrogen ion concentration, temperature and initial concentration of sucrose on the sucrose disappearance rate. It was found out that the inversion of sucrose is an irreversible reaction, which is not affected by the formation of fructose and glucose in the liquid-phase. Then, the parameters of the kinetic model (i.e., reaction rate constant and activation energy) were calculated. A comparison of the model output and the measured data showed that the kinetics of the sucrose inversion could be well described by means of the pseudo first-order kinetic model. Finally, the method of determining the kinetic model by FTIR spectroscopy was verified by comparing the results obtained in the batch reactor with the results obtained in the continuously stirred tank reactor.     

High-performance liquid chromatographic analyses for use in the acrylamide synthesis process

Summary Two liquid chromatographic methods are described for the separation and determination of components in the production of acrylamide by the catalytic hydration of acrylonitrile. The first of these provides a rapid technique by which concentrations and conversion can be directly determined for process control applications, whilst the second represents a more rigorous separation of all possible impurities for quality control purposes.     

工业丙烯腈中噁唑及其它有机杂质的气相色谱分析

提出了一种用毛细管气相色谱分析工业丙烯腈中微量噁唑及其它杂质的方法。用气相色谱．质谱法对丙烯腈中的噁唑及其它杂质进行了定性,并用化学法验证了噁唑的定性结果。采用有效碳数法计算出噁唑的质量相对校正因子为2．396,内标法测定了国内不同公司生产的丙烯腈中微量杂质的含量。其中噁唑的质量含量为0．001％-0．06％。方法已在某石化公司丙烯腈装置技术改造中应用于噁唑含量的控制分析。