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In this paper, 2,2-dimethylolbutyraldehyde was synthesized through the acetal reaction of formaldehyde and butyraldehyde, using silicotungstic acid as catalyst.

通过实验研究了硅钨酸对此羟醛缩合反应的催化效果,研究探讨了硅钨酸对此缩醛反应的催化反应活性,以及催化剂的的用量,反应物配比,反应时间等因素对反应产品收率的影响,确定了最佳催化条件。

The optimum reaction conditions are as follows: diphenylmethanethiol : methyl chloroacetate is 1:1.5, and the reaction carried out at 100℃ for 4 h, 2- acetamide can be carried out in the room temperature for 20 h, the yield of 2- acetamide was 76%, hydrogen dioxide: 2- acetamide is 1:1, and the reaction carried out at 60℃ for 3 h, the yield of modafinil was 79%, the total yield of reaction can be reached 48%.

研究表明,采用氯乙酸甲酯作为醚化试剂,反应时间4h,反应温度100℃,二苯甲硫醇:氯乙酸甲酯=1:1.5,室温下氨解反应20h,二苯甲硫乙酰胺收率76%;采用过氧化氢作为氧化试剂,反应时间3h,反应温度60℃,过氧化氢:二苯甲硫乙酰胺=1:l,莫达非尼收率79%,反应总收率可达48%。

The results show that:First, concentration of hydrogen peroxide have the most obvious influence to oil yield and carbon black yield,with the increase of concentration of hydrogen peroxide the oil yield first increase then decrease,when concentration of hydrogen peroxide is 8.19% or so,the oil yield reach to the biggest value, and with the increase of concentration of hydrogen peroxide carbon black yield decrese;Then,reaction time have more obvious influence to oil yield and carbon black yield,oil yield increase but carbon black yield decrease with the increase of reaction time;Thirdly,reaction tempreture have some influence to oil yield and carbon black yield,samely,oil yield increase but carbon black yield decrease with the increase of reaction tempreture;Finally,reaction pressure does almost no influence on oil yield and carbon black yield.

研究结果表明:过氧化氢质量浓度对产油率和炭黑产率的影响最为显著,产油率随过氧化氢质量浓度的提高先提高后降低,在过氧化氢质量浓度为8.19%左右时达到最大值,炭黑产率随过氧化氢质量浓度的提高而降低;反应时间对产油率和炭黑产率的影响也比较显著,产油率随反应时间的增加而提高,炭黑产率随反应时间的增加而降低;反应温度对产油率和炭黑产率也有一定的影响,产油率随反应温度的提高而相应地提高,炭黑产率随反应温度的提高而降低;在本文实验范围内,反应压力对产油率和炭黑产率基本上没有影响。

In this thesis, the reaction of methanol conversion into hydrocarbons on HZSM-5 and SAPO molecular sieves, which is of great importance to industry, is selected as probe reaction to get deeper insights into the structure of solid catalysts and the interaction of reactants with catalysts during adsorption and catalytic reaction by solid state NMR.

本论文主要以固体NMR为研究手段,以甲醇制烃类作为探针反应,详细研究了催化剂的结构、吸附过程中反应物与催化剂的相互作用、反应过程中反应物与催化剂的相互作用,主要取得了如下结果: 1 原位MAS NMR实验结果表明,甲醇制烃类的过程是通过&碳池&机理来实现,&碳池&的组成随反应的进行而变化,在反应前期,&碳池&由饱和烃类构成,随着反应的进行,饱和烃类和不饱和烃类共同组成&碳池&。

In Wistar rats, latent period of a-wave in scotopic rod response after 1-week transplantation was shorten (P.05); and latent period of a-wave in scotopic rod response after 2-week transplantation was prolonged (P.05); while latent period of b-wave in scotopic maximum response after 1-week transplantation was shorten (P.05). In RCS rats, amplitude of a-wave in scotopic rod response and photopic response after 4-week transplantation was increased (PO.05); while latent period of a-wave in scotopic rod response after 4-week transplantation was shorten (PO.05).Conclusion 1. At the age of 3 months, photoreceptors of the RCS rat degenerated completely, which leaded to the reduction of amplitudes of a-wave and b-wave.

Wstar大鼠术后1周的暗适应视杆反应,a波潜伏期缩短o叼。05);术后2周的暗适应视杆反应,a波潜伏期延长o功刀5):术后1周的暗适应最大反应,b波潜伏期缩短o功刀5卜*CS大鼠术后4周的暗适应视杆反应和明适应反应,a波振幅增大o功刀匀;术后4周的暗适应视杆反应,a波潜伏期缩短o<0卜结论1、RCS大鼠在3月龄时感光细胞变性死亡,导致FERG的a、b波振幅明显降低;视网膜下腔仍存在感光细胞外节盘膜碎屑,外丛状层缺乏感光细胞的突触末端,同时Muler细胞出现反应性胶质纤维增生。

The results showed that the addition leading to -2-phenyl-2-(2-vinylpiperidin-1-yl) ethanol 7 could proceed with good diastereoselectivity and excellent yield (95%).(3) The selective N-deprotection of -2-phenyl-2-(2-vinylpiperidin-1-yl) ethanol 2 without affecting the vinyl group in the substrate were untaken.(4) The Zip reaction for the transformation of -1-(3-aminopropyl)-3-methylazecan-2-one 8 to -7-Methyl-1, Sdiaza-cyclotetradecan-6-one 9 were undertaken. The results showed that, under controlled conditions, acceptable yields (43%) could be achieved and racemization can be minimized during the ring expansion reaction.

该合成路线与文献方法相比,反应条件较温和,也缩短了反应时间;(2)哌啶衍生物2与乙烯基格氏试剂进行加成反应的条件和立体选择性,取得了较好的结果(差向异构体比为80:20,产率95%左右);(3)不饱和哌啶衍生物7在不影响碳碳双键的情况下去除苯基甘氨醇手性辅助基的条件;(4)具有羰基α位手性的氨基酰胺8在不同条件下经Zip重排反应转变为9的反应,控制反应条件,可使反应中消旋化减小到最小的程度。

To the product yield is mainly studied in the brominating process, and the best synthesizing process conditions is obtained; the effect of the selection, quantity of the solvent, the reaction temperature, reaction time, and the catalyzer to the product yield is researched in the process of ketalization and the relative preferable process conditions has been got.

在脱溴反应中,主要研究了溶剂的用量、溶剂配比、物料配比、反应时间和反应温度等对目标产物得率的影响;在选择性溴化反应中,主要研究了溶剂和溴化剂的选择、物料配比、溶剂的用量等参数对产物质量和得率的影响,最终得到了合成的最佳工艺条件;在缩酮化反应中,主要研究了溶剂的选择、溶剂的用量、反应温度、反应时间和催化剂的选择等参数对产物得率的影响,并得到合成的较佳工艺条件。

The experiments for determining the reaction kinetics of Daqing atmospheric residue were performed in a continuous flow, expanded bed rector. Four-lumped reaction kinetic model was developed to account for various feed and product fractions of Daqing atmospheric residue (gases, gas oil, residue and coke). The amounts of olefins and alkyls in the gas products were further analyzed to determine reaction kinetics of gas product distributions. Hence, a combined five-lumped reaction kinetic model was obtained for catalytic pyrolysis of Daqing atmospheric residue. The kinetic constants both in four-lump model and five-lump model were evaluated. A simulator for catalytic pyrolysis process was developed by incorporating the five-lumped kinetic model into the hydrodynamic flow model.

其次利用改进的固定流化床装置考察大庆常压渣油催化裂解反应规律,筛选反应工艺参数;分析了催化裂解工艺存在的主要化学反应类型,提出了渣油一次反应和二次反应网络图;将反应原料油作为单独集总组分,而将产品中的轻质油、气体、焦炭分别作为集总,从而建立了四集总动力学模型;在此基础上,把气体产物中的目的产物低碳烯烃独立划分,得到五集总动力学模型;采用最小二乘法分析实验数据,分别得到四集总动力学模型和五集总动力学模型中各集总间相互反应转化的反应速率常数。

Because the techniques of the biochemical waste treatment are very important, the techniques of the cultivation of the microorganism have received more attention in recent years. A study is conducted to analyze the steady states and dynamic bechavior of the reactions of the cell-substrate and the prey-predator interaction in two chemostats in series. For the reaction of cell-substrate in two chemostats in series, if the specific growth rate of the Monod model is used for the cell , there are three types of steady states for this reaction system. These three types of steady states and stability are analyzed in detail. The dynamic behavior of this reaction system is analyzed by the numerical method and computer graphs. The results show that the dynamic behavior of this system consists of stable steady states.

由於生物废弃物的处理技术相当重要,故最近几年来微生物的混合培养技术深受大家的重视,本研究实施菌类-基质(Cell-Substrate)和被捕食者-捕食者(Prey-Predator)相互作用之生化反应在两个生化反应槽串联之稳定状态和动态分析,对於菌类-基质之生化反应,若以Monod模式来表示菌类之比生长速率,则此两个生化反应槽串联之反应系统共有三种型态之稳定状态,本研究对此三种型态之稳定状态和稳定度作深入的分析,对於此反应系统之动态行为,则由电脑运用数值分析的方法及电脑绘图进行分析工作,动态分析的结果显示此生化反应系统之动态行为,以稳定之稳态为主。

From the potential energy profile, it can be predicted that, the dominant channel of this reaction consists of three steps: the two reactants first form a three-membered ring intermediate (INT1) through a barrier-free exothermic reaction of 19.2 kJ/mol; three-membered ring intermediate (INT1) isomerizes to a four-membered ring silylene(P2) via the transition state (TS2) with an energy barrier of 22.8 kJ/mol; four-membered ring silylene(P2) further reacts with ethene(R2) to form a silicic bis-heterocyclic compound (P3), which is also a barrier-free exothermic reaction of 132.2 kJ/mol.

用CCSD//MP2/6-31G*方法研究了单重态二甲基亚烷基硅烯与乙烯生成硅杂双环化合物环加成反应的机理,根据该反应的势能面可以预言,该反应的主反应通道有三步组成:第一步是两反应物(R1, R2)首先生成了一三元环中间体(INT1),它是一无势垒的放热反应,放出的能量为19.2 kJ/mol;第二步是三元环中间体(INT1)经过渡态TS2异构化为了四元环硅烯(P2),其势垒为22.8 kJ/mol;第三步是四元环硅烯(P2)进一步与乙烯(R2)反应生成了硅杂双环化合物(P3),该反应也是一无势垒的放热反应,放出的能量为132.2 kJ/mol。

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