DEEP HYDROGENATION OF 2-ETHYLANTHRAQUINONE OVER PD/SIO2 CATALYST IN THE LIQUID-PHASE

被引:20
作者
DRELINKIEWICZ, A
机构
[1] Jagiellonian University, Faculty of Chemistry, 30-060 Cracow
来源
JOURNAL OF MOLECULAR CATALYSIS | 1992年 / 75卷 / 03期
关键词
D O I
10.1016/0304-5102(92)80134-3
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Hydrogenation of 2-ethylanthraquinone (eAQ) was carried out in a slurry reactor over Pd/SiO2 catalyst at atmospheric pressure of H-2 and room temperature. During hydrogenation 2-ethylanthrahydroquinone (eAQH2) was initially formed with a selectivity close to 100%. In the further process eAQH2 was hydrogenated and 2-ethyltetrahydroanthrahydroquinone (H4eAQH2) as the main product was formed in high yield (about 55-75%). eAQH-2 was also partly converted into other products termed 'degradation products'. The rate of hydrogenation, the yield of H4eAQH2 and the type of degradation products were examined as a function of the amount of catalyst. A complicated reaction pattern including consecutive (hydrogenation of aromatic rings) as well as parallel (hydrogenolysis of the carbon-oxygen bonds in eAQH-2) processes is postulated.
引用
收藏
页码:321 / 332
页数:12
相关论文
共 28 条
[1]  
Bayer O., 1925, BERICHTE, V58, P2667
[2]   SELECTIVITY ASPECTS OF THE HYDROGENATION STAGE OF THE ANTHRAQUINONE PROCESS FOR HYDROGEN-PEROXIDE PRODUCTION [J].
BERGLIN, T ;
SCHOON, NH .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (01) :150-153
[3]  
BOGDAN WN, 1988, NEFTEKIMIYA, V28, P379
[4]  
BURNS DT, 1978, ANAL CHIM ACTA, V100, P563
[5]  
COENEN WE, 1959, MECHANISM HETEROGENE
[6]  
CRONAN CS, 1959, CHEM ENG, V6, P118
[7]  
DRELINKIEWICZ A, 1991, B POL ACAD SCI-CHEM, V39, P63
[8]  
DRELINKIEWICZ A, IN PRESS B ACAD S SC
[9]  
FREJDLIN LH, 1960, IZV AKAD NAUK SSSR O, V4, P734
[10]  
FREJDLIN LH, 1960, DOKL AKAD NAUK SSSR, V131, P1362