More than 30 kinds of FCC Catalysts with good bottom cracking ability ,high yield of light oils,low coke , better heavy metal resistance and high octane barrel are developed successfully in China, which active component include REY,REHY,USY,REUSY and MFI type zeolite.More than 100,000 ton/a FCC catalyst were manufactured in china and around 90% of domestic Chinese FCC Catalyst market was occupied by RIPP's technology to process different kind feedstock and run in different types of FCC units,such as in all SINOPEC subsidiary companies-BeiJing Yanshan company,QiLU company,Shanghai Gaoqioa company,Jinling company,Maoming company. Tianjin company,Changling company,Guangzhou company, Anqing company,Jingmen company,Luoyan company,SINOPEC JiuJiang company,JiNan company, WuHan company, Changzhou company, Beihai company, FuJian petrochemical Company Limitted (FPCL)ect.) and 29 refineries in CNPC  (mainly include Fushun company ,LanZhou company,DaQing company,JinZhou company and JinXi company ,ect.)Further more, catalysts developed by RIPP were also successfully applied in SK Corperation  (gasoline and propylene mode,Indonesia,2003-2004),which have exhibited good gasoline yield and good bottom cracking ability.

 WEPEC located at Dalian city,Liaoning province,China,is a China-French joint venture petrochemical enterprise,in which a RFCCU with capacity as 2Mt/a process mainly feedstock as 30towt% VGO+70% DSAR from Saudi Arabia and Iran light and heavy oil. In the beginning,RFCCU catalysts were purchased from international market.

In 1998,the catalyst in the RFCCU of WEPEC was replaced using RIPP's .The comparison data process performance between the two kinds of catalysts show in the following Tables.  

Table 20 Feedstock Properties

Case	Reference	Our catalyst
Density(20oC),g/cm³	0.9136	0.9235
Viscosity,mm²/s 80¡æ,100¡æ	33.09 18.07	38.92 20.40
Pour point, oC	+28	+23
CCR, wt%	4.4	5.4
Refraction index(70oC)	1.4959	1.5049
Element composition ,m%   C H S N	87.00 12.34 0.47 0.19	86.65 12.02 0.62 0.24
Metal content ,ppm	5.1	6.1
Ni	9.4	10.7
V	<0.1	<0.1
Cu	7.3	7.7
Fe	2.5	1.9
Na
Distillation	281	295
IBP	356	362
5%	384	386
10%	446	442
30%	506	499
50%	559(63.5%)	555(65.5%)
70%

Case	Reference	Our catalyst
Feed rate,t/d	5763	6062
Product yields,wt%
Dry gas	4.32	3.84
LPG	13.13	13.95
Naphtha	49.11	49.49
LCO	20.13	20.38
Slurry oil	4.39	3.59
Coke	8.37	8.30
Loss +acidic gas	0.55	0.45
Total	100.0	100.00
Conversion,wt%	75.48	76.03
Light oil yield ,m%	69.24	69.87
Liquid product yield ,m%	82.37	83.82

Item	Unit	Base Case	CASE A	CASE  B	CASE C
Date		July 22-24	Aug. 1-3	July 31-Aug.2	Aug.5-7
Catalyst		Base*	RIPP	IPP	RIPP
Feed Rate	B/D	52714	52110	51469	53916
CFT	oC	208	209	205	204
Rx.Temp	oC	519	519	519	519
#2 Reg.Temp	oC	714	719	720	713
Cat M/U	T/Day	24.6	20.0	20.0	41.32
Rx.Cat Cir Rate	T/min	40.60	38.31	37.84	41.332
Cat Oil Ratio	Wt/wt	7.51	7.18	7.17	7.52
Coke Yield	Wt%	9.06	8.98	9.03	8.93
Cat.Cooler Duty	Gcal/h	40.4	39.6	40.0	38.2
Normalized Yield   C3 C4 LCN HCN Total Naphtha LCO SLO Total Minus C2	V% V% V% V% V% V% V% V% wt%	9.71 13.87 58.66 16.12 74.78 2.14 8.25 108.76 2.40	10.23 14.86 58.51 15.72 74.23 2.05 8.0 109.36 2.41	10.08 14.54 58.51 15.78 74.29 2.09 8.12 109.11 2.45	10.94 16.02 59.44 14.56 74.00 1.99 7.26 110.21 2.23
Feedstock API CCR N Ni V	wt% Wppm Wppm Wppm	20.77 3.93 1,739 4.90 6.80	20.90 4.00 1,845 5.67 7.90	20.77 4.17 1,944 5.90 8.23	21.47 3.43 1,697 3.37 4.27