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含氧化合物

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It was noted that amongst the 74% cyclohexane conversion to oxygenates, 68% of that was the dimethyl adipate.

有人指出,其中74 %环己烷转化为含氧化合物, 68 %,这是二己二酸。

Cyclohexane with Mn as a catalyst in Trial 3 gave a total conversion of cyclohexane of 73% and 28.8% of which were oxygenates which contained 15.2% of dimethyl succinate, 19.6% of dimethyl glutarate and 65.2% of dimethyl adipate.

环己烷锰作为催化剂在审判3了总转化环己烷的73 %和28.8 %,其中含氧化合物其中载有15.2 %的二甲基丁二酸, 19.6 %的二甲基戊二和65.2 %的二己二酸。

All these lead to a suggestion of a two step method technical route in which CH 4 and CO 2 can be converted into high value products at low temperature directly.

对近年来 CH4 的低温活化的研究结果进行了评述,结合对 CH4 的两步反应同系化及CO2 加氢研究成果,提出了由 CH4 - CO2 低温转化直接合成 C2 +含氧化合物的两步法技术路线及催化剂体系,论证了其可能性

Anti-knock additive tetraethyl lead,vapor pressure,cetane number and content of aromatic hydrocarbon,ethylenes,sulfur and oxides respectively in the motor fuel are more detailedly analysed in regard to their effect on motor vehicle exhaust emission.

较为详细地分析了燃油中四乙铅抗爆剂、芳烃含量、烯烃含量、硫含量、蒸气压、十六烷值及含氧化合物等对汽车排放的影响,并简述了其发展趋势。

One test is circulating test which tailing water is filtered and reused,another test is adding a little frother in water before adding coal sample.

结果表明,循环水中积聚的有机物主要是醇、酮、羧酸盐等含氧化合物;有机物积聚可提高精煤回收率,改变浮选的选择性

Ethanol is by far the most commonly used alcohol oxygenate and bio-ethanol in particular is being increasingly used as a replacement for other fuel oxygenates.

乙醇是目前最常用的酒精氧化和生物乙醇,尤其是越来越多地使用替代其他燃料含氧化合物

The oxidation of saturated C-H bond is an important technical method to obtain oxygenous organic compounds.

饱和C-H键的氧化是合成有机含氧化合物的重要方法。

New method named GC-K3 group contribution method for the esxtimation of the octanol-water of oxygenous compounds is presented.

提出了估算含氧化合物的正辛醇/水分配系数的基团贡献法———GC-K3基团贡献法。

The appearance of the synthetic microspherical catalyst containing the SAPO molecular sieves is complete, the synthetic microspherical catalyst has a multi-level pore structure, and can be used for the reaction of producing alkene by converting an oxygen compound.

合成的含SAPO分子筛的微球催化剂形貌完整,且具有多级孔道结构,可以用于含氧化合物转化制烯烃反应。

Three results are obtained by an orthogonal experiment. The main components of essential oil in separating containerⅠare terpenoid, terpeneless compound is in separating container Ⅱ. Through second-level separation the technological conditions of de-terpene are: pressure 7MPa, temperature 32℃ in separating containerⅠ;pressure 4~5MPa, temperature 32℃ in separating containerⅡ. The optimum technological parameters of obtaining two essential oils are: particle size 0.60mm, pressure 10MPa, temperature 36℃, operating time 90 minutes. There are 1.46% and 1.88% essential oil in separating containerⅠand Ⅱ respectively.

通过正交试验表明:分离器Ⅰ中精油的主要成分是萜烯烃类化合物,分离器Ⅱ中精油的主要成分是由高级醇类、醛类、酮类、酯类等组成的含氧化合物;二级分离脱萜的适宜参数是:分离器Ⅰ的压力为7MPa,分离器Ⅱ的压力与循环压力相同,温度都为32℃;同时得到萜烯烃类精油和低萜精油的最优工艺组合是粒度0.60mm,萃取压力10MPa,萃取温度36℃,萃取时间90min,精油得率分别为1.46%和1.88%。

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