Cracking Metal-Contaminated Oils with Catalysts Containing Metal

and V) in gas oils have on the cracking activity and selectivity of commercial fluid ... in excellent agreement with JCPDS (Joint Committee on Powder...
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Chapter 10

Downloaded by UNIV OF CALIFORNIA SANTA BARBARA on September 2, 2015 | http://pubs.acs.org Publication Date: September 12, 1988 | doi: 10.1021/bk-1988-0375.ch010

Cracking Metal-Contaminated Oils with Catalysts Containing Metal Scavengers Effects of Sepiolite Addition on Vanadium Passivation Mario L. Occelli Unocal Science & Technology Division, Unocal Corporation, P.O. Box 76, Brea, CA 92621

The addition o f layered magnesium silicate p a r t i c l e s such as sepiolite to a high activity commercial fluid cracking c a t a l y s t (FCC), generates dual-functional cracking c a t a l y s t (DFCC) mixtures t h a t , even when metal contaminated with as much as 1.5 wt% vanadium, are capable o f r e t a i n i n g useful cracking a c t i v i t y (70% conversion) when cracking a light gas oil (with an API gravity o f 29.6) a t m i c r o a c t i v i t y t e s t (MAT) conditions. Improved coke and hydrogen selectivity were also observed. Transport experiments have been used to show that the DFCC enhanced vanadium resistance can be a t t r i b u t e d to the gas phase transport o f this metal from the host c a t a l y s t to the diluent (sepiolite) where it is sorbed and passivated. R e c e n t l y , i t has been reported i n t h e patent l i t e r a t u r e t h a t vanadium (and n i c k e l ) r e s i s t a n c e i n a FCC can be s i g n i f i c a n t l y enhanced by t h e a d d i t i o n o f c e r t a i n d i l u e n t s capable o f a c t i n g as metal scavengers ( 1 - 4 ) . In f a c t , a d d i t i o n o f alumina and a l u m i n a - c o n t a i n i n g m a t e r i a l s w i t h (1_) o r w i t h o u t [2) p a s s i v a t i n g agents (such as Sn o r Sb) o r a d d i t i o n o f n a t u r a l l a y e r e d magnesium s i l i c a t e s (20 as w e l l as a d d i t i o n o f c e r t a i n n a t u r a l z e o l i t e s ( 4 ) can i n h i b i t t h e d e l e t e r i o u s e f f e c t s t h a t metal contaminants ( l i k e "rTi and V) i n gas o i l s have on t h e c r a c k i n g a c t i v i t y and s e l e c t i v i t y o f commercial f l u i d c r a c k i n g c a t a l y s t s (FCC). The a d d i t i o n o f metakaolin microspheres t o improve a commercial c a t a l y s t r e s i s t a n c e to metals p o i s o n i n g has been proposed by B a r t h o l i c (J5). I t i s t h e purpose o f t h i s paper t o r e p o r t and e x p l a i n t h e high r e s i s t a n c e t o metals d e a c t i v a t i o n o f a d u a l - f u n c t i o n c r a c k i n g c a t a l y s t (DFCC) obtained by d i l u t i n g a high a c t i v i t y c r a c k i n g c a t a l y s t (Davison 6RZ-1) w i t h s e p i o l i t e granules 100 χ 325 mesh i n size. S e p i o l i t e (and a t t a p u l g i t e ) a r e f i b r o u s c l a y m i n e r a l s composed o f t e t r a h e d r a l chains o f s i l i c a l a y i n g i n planes j o i n e d together (through shared oxygens) by magnesium (and aluminum) atoms i n octahedral c o o r d i n a t i o n . T h e i r s t r u c t u r e has been d e s c r i b e d i n d e t a i l s by Grim (6). These l a y e r e d magnesium s i l i c a t e s c o u l d °

0097-6156/88/0375-0162$06.00/0 1988 American Chemical Society

In Fluid Catalytic Cracking; Occelli, M.; ACS Symposium Series; American Chemical Society: Washington, DC, 1988.

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p a s s i v a t e n i c k e l contaminants by forming s t a b l e s i l i c a t e s (_7) s i m i l a r to g a r n i e r i t e . ( G a r n i e r i t e i s a hydrous nickel-magnesium s i l i c a t e s i m i l a r to c h r y s o t i l e w i t h n i c k e l i n octahedral s i t e s . ) Vanadium p a s s i v a t i o n could r e s u l t from the formation of heat s t a b l e vanadates (7_).

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Experimental M a t e r i a l s and Gas O i l C r a c k i n g . The reference c a t a l y s t used (Davison's GRZ-1 ) i s a h i g h - a c t i v i t y c r a c k i n g c a t a l y s t c o n t a i n i n g about 35% c a l c i n e d r a r e - e a r t h exchanged z e o l i t e Y (CREY). The 100 χ 325 mesh granules of "Spanish S e p i o l i t e " (from TQLSA, S.A.) used t o study metals t r a n s p o r t a t hydrothermal c o n d i t i o n s , have been found to c o n t a i n a c l a y mineral c h a r a c t e r i z e d by a t y p i c a l f i b r o u s s t r u c t u r e , high s u r f a c e area (142 m / g ) , and pore volume (0.68 c c / g ) ; i t s chemical composition i s shown i n Figure 1. This mineral was e s s e n t i a l l y f r e e from phase i m p u r i t i e s and gave an x-ray p a t t e r n i n e x c e l l e n t agreement w i t h JCPDS ( J o i n t Committee on Powder D i f f r a c t i o n Standards) p a t t e r n No. 13-595, see F i g u r e 1. A f t e r steaming (760°C/5h) t h i s c l a y r e t a i n e d 70% of i t s o r i g i n a l BET s u r f a c e area and i t s pore volume remained e s s e n t i a l l y unchanged a t ^0.68 cc/g. C a t a l y t i c e v a l u a t i o n was performed using a m i c r o a c t i v i t y t e s t (MAT) s i m i l a r to the one d e s c r i b e d by C i a p e t t a and Anderson ( 8 ) . The weight h o u r l y space v e l o c i t y (WHSV) was 14-15; the r e a c t o r temperature was 510°C. A c a t a l y s t - t o - o i l r a t i o of 3.5-3.8 was used. The chargestock's s l u r r y o i l (S.O., b.p. >354°C), l i g h t c y c l e gas o i l (LCGO, 232°C < b.p.