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methanol相关的网络例句

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与 methanol 相关的网络例句 [注:此内容来源于网络,仅供参考]

The domestic demand of acetic acid up to 1,440,000-1,620,000 tons can be anticipated in 2010, if 60% is produced by methanol, 520,000 tons of methanol will be consumed;③Methanol can be used as feedstock to directly produce various pesticides ,such as fenitrothion, omethoate, dipterex etc., we anticipate that approximately 340,000 tons of methanol will be used to produce pesticides in 2010.④ Various medicines use methanol as feedstock, such as sulfanilamide, vitamin B6 etc., we anticipate that approximately 180,000 tons of methanol will be used to produce medicines in 2010.⑤ In the duration of dye production, methanol can be used as feedstock or solvent, such as s carlet base RC, disperse red GLZ, phthalocyanin ⑥ Synthetic resin also need methanol as feedstock such as organic glass, we anticipate that about 70,000 tons of methanol will be used to produce synthetic resin and plastics in 2010;⑦Synthetic fibers and synthetic rubber industry, will use methanol about 800,000 tons in 2010;⑧ At present, the production of MTBE is increase rapidly, there are 27 set of plants, total production capacity is 620,000 tons every year, and the demand is about 800,000 tons, there is gap between demand and supply.

预计2010年我国醋酸的需求量将达144~162万吨,按甲醇羰基法占60%计,将需求甲醇达52万吨;③多种农药的生产直接以甲醇为原料,如杀螟松、乐果、敌百虫等,预计到2010年甲醇用于生产农药约为34万吨;④多种医药药品以甲醇为原料,如长效磺胺、维生素B6等,预计到2010年甲醇用于医药约为18万吨;⑤染料生产过程中用甲醇作原料或溶剂,如红色基RC、分散红GLZ、阴率子GRL、酞菁素等等,预计2010年甲醇用量约为10万吨;⑥有机玻璃等合成树脂也需用甲醇为原料,预计到2010年甲醇用于生产合成树脂与塑料用量约为7万吨;⑦合成化纤与合成橡胶工业,2010年甲醇用量约为13万吨;⑧我国MTBE生产正处于快速增长期,现有MTBE装置27套,总生产能力62万吨/年,而年需求量约80万吨,有一定缺口。

Its commercial technologic processes and products,such as Acetic Acid Production by Carbonylation of Methanol,Formyl Morpholine,Steam Reforming Catalyst,Low Pressure Methanol Synthesis,Dimethyl Formamide Production by Dehydrogenation of Methanol,Dimethyl Ether Synthesis by Methanol Dehydration,Hydrogen Production by Methanol Cracking,Methanol Synthesis Catalyst,PSA Gas Separation Devices, and etc.,have been applied in more than 800 plants over fields including chemical industry,petrochemical,food, metallurgy,machinery,military industry.Many technological products were exported to American,European,Asian countries as well as Hong Kong,Macao and Taiwan.Remarkable economic and social benefits are achieved.

甲醇羰基化合成醋酸,甲酰吗啉,转化催化剂,低压合成甲醇,甲醇脱氢制二甲基甲酰胺,甲醇脱水制二甲醚,甲醇裂解制氢,合成甲醇催化剂,变压吸附制氢等成套工业装置和产品应用于全国800多家化工,石化,食品,冶金,机械,军工等企业,并出口美国,欧州,亚州等国及港,澳,台地区。

It is shown that the methanol dimer and methanol cluster are the predominant species of methanol in gaseousness. So we believe that rather the methanol dimer is the original reactant of the methanol dehydration reaction to dimethyl ether than the mono-methanol.

研究表明,在气相中,甲醇分子主要以二聚体和多聚体的形式存在,据此提出甲醇脱水反应的原始反应物是甲醇二聚体,而不是单个甲醇分子。

An alternative way of the synthesis of methanol from syngas is low-temperature methanol synthesis via methyl formate in liquid phase, namely, carbonylation of methanol in the first step, and hydrogenolysis of methyl formate in the second step.

低温液相甲醇合成是指在(80-160℃)范围内,甲醇首先与合成气中的CO发生羰基化反应生成甲酸甲酯,甲酸甲酯再氢解生成甲醇的两个反应在一个反应器内串联进行的方法。

Kinetics of methanol dehydration to dimethyl ether on modified kaolin catalyst was studied in an integral reactor under normal pressure. It is deduced that the surface reaction of methanol molecule adsorbed on the active site of catalyst with methanol molecule in gas phase is the rate determining step. The hyperbolic type kinetic equation r=ksbMpM2/(1+bMpM+bpE) is obtained according to the theory of langmuir even adsorption and using the R-E mechanism.

采用积分反应器,考察了常压下在改性高岭土催化剂上甲醇脱水生成二甲醚的反应动力学,根据Langmuir均匀吸附理论,采用R-E机理,推断吸附的甲醇分子与气相主体中的甲醇分子发生的表面反应为速率控制步骤,得到双曲线型动力学方程为: r= ksbMpM2 /(1+bMpM+bpE)(r为反应速率, ks为反应速率常数, bM为甲醇的吸附平衡常数, b为二甲醚和水的吸附平衡常数之和, pM、 pE分别为甲醇、二甲醚的分压)。

The pigment in colored cotton fibers was extracted by methanol at room temperature. The results of color reactions HCl-Mg reaction, NaBH4 reaction, NaOH reaction, FeCl3 reaction and Pb(Ac2 reaction of the pigment extractive showed that the pigment extracted by methanol was flavone or flavonol with two adjacent hydroxide groups (Table 2, Fig. 1). The results of UV spectral analysis further proved that the pigment extracted by methanol from brown fiber belonged to flavone with two adjacent hydroxide groups in B ring, and that from the green fiber contained not only flavone but also flavonols with two adjacent hydroxide groups both in A ring and B ring and indican replaced a hydroxide group at 3-site of A ring Fig.

通过盐酸-镁粉反应、四氢硼钠还原反应、碱反应、醋酸铅反应、氯化铁反应和紫外光谱吸收的分析表明,甲醇室温提取的棕色棉纤维色素可能是黄酮类化合物,B环上带有邻二酚羟基;甲醇室温提取的绿色棉纤维色素除黄酮类化合物外,还含有3-位羟基被糖甙化的黄酮醇类化合物,A、B环上都带有邻二酚羟基。

Systematic isopiestic measurements have been made at the temperature 298.15K for the quaternary system {water (A1)+methanol (A2)+sodium bromide + ammonium bromide} with the mass ratios of water: methanol=9∶1 and 4∶1 and for the quinary system {water (A1)+methanol (A2)+ethanol (A3)+sodium bromide +ammonium bromide} with the mass ratios of water: methanol: ethanol=18∶1∶1 and 8∶1∶1, which were the first isopiestic determining examples for mixed solvent systems.

本文系统地测定了298.15K时混合溶剂各组元质量比为w〓∶w〓=9∶1和4∶1的四元系{H〓O+甲醇(A2)+NaBr+NH〓Br}和w〓∶w〓∶w〓=18∶1∶1和8∶1∶1的五元系{H〓O(A1)+甲醇(A2)+乙醇(A3)+NaBr+NH〓Br}的等压平衡,是混合溶剂体系等压性数据的首例。

Methods Control the methanol feeding in growth phase of Hansenula polymorpha by online monitoring. In induction phase, the expression levels of HBsAg when the methanol feeding were controlled by DO-Stat/pH-Stat method and by offline gas chromatography, as well as those when only methanol was fed and glycerol and methanol were fed alternatively, were compared.

在细胞生长阶段采用DO/pH线测量的控制方法,使酵母细胞密度达到一个较高水平,诱导期比较DO-Stat/pH-Stat法和离线检测甲醇两种控制流加甲醇的方法,同时也比较用甘油和甲醇双碳源间断流加法与单纯流加甲醇法对目的蛋白表达的影响。

The methanol contents of carambola wine fermented from fresh and frozen carambola juice were 33 and 74 ppm respectively. The alcohol content, soluble solid, specificity gravity, pH and titrable acid are almost the same during the fermentation of carambola juice and puree, the methanol content of the must would increase as the fermentation progressing. The methanol content of the wine fermented from carambola juice and carambola puree were 74 and 256 ppm respectively, so the separation of the pulp from carambola puree can decrease the methanol content efficiently in carambola winemaking.

新鲜及冷冻杨桃汁经发酵后,甲醇含量分别为33及74 ppm,杨桃汁与杨桃泥在发酵期间其酒精度、可溶性固形物、比重、pH、可滴定酸的变化情形相似,而甲醇则随著发酵时间增加而增加,杨桃汁及杨桃泥所酿造之杨桃酒其甲醇量分别为74 及256 ppm,结果显示杨桃发酵前汁渣分离将可有效降低杨桃酿造酒中甲醇含量。

The phase equilibrium data of SBO-FAME-Methanol, SBO-FAEE-Ethanol and Glycerol-FAEE-Ethanol systems were measured. The results indicated that it involved two different stages: liquid-liquid-solid reaction stage and liquid-solid reaction stage. When the molar ratio of methanol to oil is 12:1 at 65℃, the turning point is at a 55% biodiesel yield. The liquid-liquid-solid reaction model was proposed based on the double-membranes theory. It indicated that the process is reaction and mass transfer controlled together at the first stage, and the second stage is reaction controlled. The predictions of the model are matched with the experimental results.In the end, the acid was extracted using methanol and ethanol from jatropha curcas l oil.

测定了生物柴油制备过程中的SBO-FAME-Methanol、SBO-FAEE-Ethanol、Glycerol-FAEE-Ethanol三组分相平衡数据,表明固体碱催化过程分为液-液-固和液-固两个反应阶段,在醇油摩尔比为12:1、65℃的初始反应条件下,转化率达到55%时,为第一阶段向第二阶段的转折点;基于双膜理论建立了固体碱催化制备生物柴油的非均相液-液-固反应模型,表明两个反应阶段分别为传质、反应共同控制和反应控制,模型计算值与实验值吻合较好。

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