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hydrogenation相关的网络例句

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与 hydrogenation 相关的网络例句 [注:此内容来源于网络,仅供参考]

A Pd /D005 resin catalyst was prepared by using ion exchangemethod.Selective hydrogenation for pentadiene in FCC C5 fractions and hydroetherification of tertiary pentanes with methanol were investigated.

采用离子交换法制备了Pd/D005树脂催化剂,对催化裂化C5馏分中戊二烯的选择性加氢和叔戊烯与甲醇的临氢醚化反应进行了研究。

A Pd /D005 resin catalyst was prepared by using ion exchange method.Selective hydrogenation for pentadiene in FCC C5 fractions and hydroetherification of tertiary pentanes with methanol were investigated.

摘 要:采用离子交换法制备了Pd/D005树脂催化剂,对催化裂化C5馏分中戊二烯的选择性加氢和叔戊烯与甲醇的临氢醚化反应进行了研究。

There are three isomeric pentene(C5H10)that yield 2-methylbutane on catalytic hydrogenation. Write structural formulas for these three isomers and indicate their relative stabilities based on the ΔH values

答:戊烯的三种同分异构体在催化加氢后可生成2-甲基丁烷,写出3个同分异构体的结构式,并依据他们的ΔH值判断出它们的相对稳定性

With the continuous increasing production of high-sulfur crude oil,non-hydrogenation deslulfurization technology has become the main developing goal in big petrolic corporations.

随着加工高硫原油量的不断增加,开发非加氢脱硫工艺成为各大公司科研开发的重点。

Aldol condensation 2, 5-dimethoxymethoxyacetophone with 2, 4, 6 -tri methoxymethoxybenzendehyde, then hydrogenation, reductive, the key intermediate 83 (84) of natural product 3, 5, 7, 2′, 5′- pentahydroxyflavan, was obtained; Mini reviewed EGCg activity, Then gallic acid and phloroglucin were used to synthsis EGCg, The key intermediate Chalcone 109 of EGCg was abtained through 7 steps from gallic acid.

重点介绍了以没食子酸为原料,经酯化,保护,还原,氧化,格氏反应,氧化六步反应得到3,4,5-三苄氧基苯乙酮,以间苯三酚为原料,经维斯迈尔反应,苄基保护,甲氧甲氧基保护三步反应得到2,4-二苄氧基-6甲氧甲氧基苯甲醛,酮106与醛108经羟醛缩合得到EGCg重要反应中间体查尔酮109。

Other 3-(2-aminoethyl)substituted phthalide\'s derivatives were synthesized by Reductive Alkylation of 3-aminoethylphthalide, which was obtained by hydrogenation of 3-acetonitrile phthalide.

比扣扣灵(Bicuculline,BIC)是GABAa受体的经典竞争性拮抗剂,它与GABA识别位点高亲和力结合,选择性阻断GABAa受体,故长期以来一直把它作为识别GABAa受体的工具药。

The colorless, odorless, good stability hydrogenation piperylene C5 petroleum resin, whose chroma is less than 1 and softening point is 92.6 ℃, can be obtained in this process.

可以制得色度在1以下、软化点为92.6℃的无色、无味、稳定性很好的加氢间戊二烯石油树脂。

The rhythmic hydrogenation reaction of piperylene C5 petroleum resin produced by Fushun Zhengchuan chemical plant was carried out by using the laboratory made catalysts that load of palladium is 1.0%, load of other metals is 1.0%. The best hydroprocessing conditions are:reaction temperature is 270 ℃, reaction pressure is 3.0 MPa, reaction time is 4 h.

采用含钯质量分数1.0%,其他金属质量分数1.0%的自制催化剂对抚顺市正川化工厂生产间戊二烯C5石油树脂,在高压釜中进行间歇加氢,最佳工艺条件为:反应温度270℃,反应压力3.0MPa,反应时间4h。

The main objective of this research project is to modify the Methyl-Acetylene/propadiene selective hydrogenation reaction system of the No.3 Naphtha Cracker in CPC. The original gas phase reaction system was redesigned to a liquid phase reaction so that higher propylene selectivity was achieved and lower rates of propane and green oil were produced. To recover effectively the higher production of valuable propylene from the reaction system, the following fractionator was also redesigned.

本研究之目的在於修改中油公司三轻工场老旧的甲基乙炔/丙二烯选择性氢化气相反应系统,使成为液相反应系统,藉由液相反应的优异性,提高由MAPD氢化得到丙烯之选择率,同时降低丙烷及绿油产率,以增加丙烯产率,另亦修改丙烯精馏系统,以提升蒸馏塔提纯之效率。

The reaction results of the selective hydrogenation of MethylAcetyleneand Propadiene in C 3 distillate by catalytic distillation were investigated with randomlypacked structure of packingtype catalyst, the combined structure of sieve tray and packingtype catalyst as well as the structure with interlaced packing and ordinary catalyst.

考察了填料状催化剂散装结构、筛板填料状催化剂复合结构、规整填料与普通催化剂交错排列结构等用于C3 馏分中丙炔、丙二烯催化蒸馏选择加氢过程的反应效果,综合考虑催化剂制备的难易、工业装置长周期运转的必要性、传质对反应的影响等因素,推荐在工业装置上采用规整填料与催化剂交错排列结

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