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1)  tert-anyl ethyl ether
叔戊基乙基醚
2)  ethyl tert-amyl ether
乙基叔戊基醚
1.
The synthesis of ethyl tert-amyl ether(TAEE) was chosen as a model system.
用协同学方法分析了乙基叔戊基醚合成反应体系的反应速率问题 ,通过引入一种非奇异变换将相应的反应速率方程组直接转换成Haken形式 ,从而发现对系统演化影响较大的序参量 ,进而通过绝热消去法处理而得到反应体系的各组分浓度与反应时间的演化解析表达式 。
3)  TAME [英][teɪm]  [美][tem]
叔戊基甲醚
1.
Development of TAME process utilizing C_5 hydrocarbons;
利用C_5开发叔戊基甲醚
4)  TAME [英][teɪm]  [美][tem]
甲基叔戊基醚
1.
THERMODYNAMIC ANALYSIS OF SYNTHESIS REACTION OF TERT-AMYL METHYL ETHER (TAME);
甲基叔戊基醚合成反应的热力学分析
2.
Progress of the Synthesis of TAME by Etherification Reaction of Ampleness;
碳五烯烃醚化合成甲基叔戊基醚的现状与展望
5)  tert-amyl methyl ether
甲基叔戊基醚
1.
Synthesis of tert-amyl methyl ether from methanol and cracking C_5 fraction,and thermodynamic characteristics of the etherification system were studied.
以乙烯厂裂解碳五馏分和甲醇为原料,以国产QRE型大孔磺酸树脂为催化剂,在固定床反应器中考察了液相合成甲基叔戊基醚反应体系的热力学特征。
2.
Intrinsic kinetics for synthesis of tert-amyl methyl ether(TAME) from pyrolysis C5 and methanol on a sulfonic ion exchange resin catalyst(QRE) with free of both internal and external diffusions was studied in a continuous tubular reactor.
LH模型中的2-甲基-1-丁烯异构化和2-甲基-1-丁烯、2-甲基-2-丁烯与甲醇合成甲基叔戊基醚反应的活化能分别为:92。
6)  tertiary amyl methyl ether
甲基叔戊基醚
1.
Catalysts for decomposition of tertiary amyl methyl ether(TAME) were characterized by means of XRD,TG-DTA,FTIR,and analysis of adsorption and desorption of pyridine.
采用该催化剂,在等温固定床反应器中进行甲基叔戊基醚(TAME)的裂解实验,并对催化剂活性下降机理进行讨论。
2.
The market demand and technology status of the gasoline blender—tertiary amyl methyl ether (TAME) and its developmental trend in China are discussed in this paper.
介绍了汽油调合剂——甲基叔戊基醚(TAME)的市场情况、技术状况及国内发展动向。
3.
The discussion focused on following processes: Neste s NExTAME process featured in integration of distillation column with a side-stream reactor,Snamprogetti s DET process featured in combination of tertiary amyl methyl ether synthesis, olefin skeletal isomerization and paraffin separation.
重点介绍了Neste公司的NExTAME工艺,其特点是采用精馏塔和侧线反应器;Snamprogetti公司的DET工艺,主要特点是采用由甲基叔戊基醚合成、骨架异构化和烷烃分离组成的组合工艺;CDTECH公司的CDEthers工艺和UOP公司的Ethermax工艺均采用了催化精馏技术;抚顺石化公司、兰州石化公司和齐鲁石化公司的催化裂化轻汽油醚化工艺,其中兰州石化公司和齐鲁石化公司分别开发了催化精馏工艺。
补充资料:叔戊基乙基醚
分子式:CH3CH2(CH3)2OCH2CH3
CAS号:

性质:无色液体。沸点102℃。密度0.751g/cm3。在酸催化剂存在下,将三甲基乙烯与乙醇加成而制得。用作溶剂。

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