1) cumene process
异丙苯法
1.
The typical industrial technology of producing phenol was cumene process containing four steps: alkylation,oxidation,purification and recovering.
异丙苯法是苯酚、丙酮的代表性工业制备方法,主要由烃化、氧化、精制、回收四个工序组成。
2) production phenols
异丙苯氧化法
3) diisopropyl benzene
二异丙苯
1.
Bis(tert-butylperoxy) diisopropyl benzene was synthesized from diisopropyl benzene by peroxidation,reduction,synthesis of BIPB.
以对(间)二异丙苯为原料经过过氧化反应、还原反应、双叔丁基过氧化二异丙苯(BIPB)的合成三步反应合成双叔丁基过氧化二异丙苯。
4) Isopropyl benzene
异丙苯
1.
preparation of p-nitroisopropyl benzene by nitration of isopropyl benzene;
异丙苯定位硝化制备对硝基异丙苯
2.
Alkylation of benzene with propylene to isopropyl benzene with ionic liquid as catalyst;
一种用于苯-丙烯烷基化反应制异丙苯的离子液体催化剂
5) diisopropylbenzene
二异丙苯
1.
Thermodynamic analysis of diisopropylbenzene transalkylation reaction;
二异丙苯烷基转移反应的热力学分析
2.
Synthesis of diisopropylbenzene and triisopropylbenzene by heterogeneous catalytic method;
异相催化法合成二异丙苯和三异丙苯
3.
Hβ-1,Hβ-2 and Hβ-3 molecular sieves modified with NH_4NO_3,diammonium citrate and triammonium citrate respectively were characterized by means of XRD,NH_3-TPD and IR,and used as catalysts for diisopropylbenzene(DIPB)isomerization.
考察了三元有机酸铵盐(柠檬酸三铵和柠檬酸氢二铵)和传统的硝酸铵对β分子筛改性的影响,采用X射线粉末衍射、氨吸附-程序升温脱附和吡啶吸附红外光谱技术对催化剂进行表征,并将改性后的催化剂用于二异丙苯的异构化反应。
6) cumene
['kju:min]
异丙苯
1.
Kinetics and mechanism for α-methylstyrene hydrogenation to cumene;
AMS加氢制异丙苯反应动力学及机理
2.
Preparation of cumene by hydrogenation of α-methylstyrene in a trickle-bed reactor;
滴流床反应器AMS加氢制异丙苯
3.
Flow boiling heat transfer and pressure drop of high saturation temperature organic fluid cumene in vertical tube;
垂直管内高沸点工质异丙苯流动沸腾换热与阻力
补充资料:2,6-二异丙基苯异氰酸酯
分子式:C13H17NO
分子量:203.31
CAS号:28178-42-9
性质:无色透明液体。闪点107℃,沸点117℃(10.00mmHg),相对密度0.9510。
制备方法:暂无
用途:暂无
分子量:203.31
CAS号:28178-42-9
性质:无色透明液体。闪点107℃,沸点117℃(10.00mmHg),相对密度0.9510。
制备方法:暂无
用途:暂无
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
参考词条