Regeneration of spent resid fluidized catalytic cracking catalyst by removing metal poisons such as V, Ni, and Fe

被引:11
作者
Park, SK
Jeon, HJ
Jung, KS
Woo, SI
机构
[1] Korea Adv Inst Sci & Technol, Dept Chem & Biomol Engn, Yuseong Gu, Taejon 305701, South Korea
[2] Korea Adv Inst Sci & Technol, CUPS, Yuseong Gu, Taejon 305701, South Korea
[3] LG Caltex Oil Corp, Daeduck Cent Res Ctr, Fuel Res Team, Taejon 305380, South Korea
关键词
D O I
10.1021/ie020515u
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Modified Demet III and Demet IV processes were studied to regenerate the spent resid fluidized catalytic cracking (RFCC) catalyst by removing metal poisons. A total of 33.1 wt % of V, 89.2 wt % of Ni, and 67.7 wt % of Fe were removed by modified Demet III, and 37.3 wt % of V was selectively removed by modified Demet IV. The results of a microactivity test (MAT) showed that the activity and selectivity of the regenerated catalysts were considerably enhanced. It was proven by the results of MAT, unit cell size of zeolite, and Brunauer-Emmett-Teller surface area and pore volume that the severe condition for the removal of poisonous metals such as sulfidation and calcination at excessively high temperature and washing with only oxalic acid caused destruction of catalyst structure and consequently did not rejuvenate the spent RFCC catalysts though lots of metal poisons were removed. The regenerated catalysts by Demet IV were tested in a Davison circulation riser (DCR), and the results showed that the conversion and gasoline yield of regenerated catalysts were increased without causing any operating problem.
引用
收藏
页码:736 / 742
页数:7
相关论文
共 9 条
[1]  
BURK EH, 1981, Patent No. 4293403
[2]   Regeneration of spent RFCC catalyst irreversibly deactivated by Ni, Fe, and V contained in heavy oil [J].
Cho, SI ;
Jung, KS ;
Woo, SI .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2001, 33 (03) :249-261
[3]  
ELVIN FJ, 1988, ACS SYM SER, V375, P17
[4]   FLUID CATALYTIC CRACKING OF HEAVY (RESIDUAL) OIL FRACTIONS - A REVIEW [J].
OTTERSTEDT, JE ;
GEVERT, SB ;
JARAS, SG ;
MENON, PG .
APPLIED CATALYSIS, 1986, 22 (02) :159-179
[5]   PREDICTION OF CRACKING CATALYST BEHAVIOR BY A ZEOLITE UNIT-CELL SIZE MODEL [J].
PINE, LA ;
MAHER, PJ ;
WACHTER, WA .
JOURNAL OF CATALYSIS, 1984, 85 (02) :466-476
[6]  
WOOLERY GL, 1997, FLUID CRACKING CATAL, P51
[7]   FLUID CATALYTIC CRACKING CATALYST DEMETALATION BY CONVERTING METAL POISONS TO WASHABLE SULFUR-CONTAINING-COMPOUNDS [J].
YOO, JS ;
KARCH, JA ;
BURK, EH .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1986, 25 (04) :549-553
[8]   DEMETALATION CHEMISTRY - CONTROL OF VANADIUM ON FLUID CRACKING CATALYST [J].
YOO, JS ;
BURK, EH ;
KARCH, JA ;
VOSS, AP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (07) :1183-1189
[9]   Metal recovery and rejuvenation of metal-loaded spent catalysts [J].
Yoo, JS .
CATALYSIS TODAY, 1998, 44 (1-4) :27-46