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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.
Case | Reference | Our catalyst |
Density(20oC),g/cm | 0.9136 | 0.9235 |
Viscosity,mm/s 80,100 | 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 |
Catalyst | Bottom cracking | LPG Yield | Light oil Yield | Octane number enhancement | Gasoline Yield | C3=, C4= selectivity | Iso-olefin selectivity | Ni Tolerance | V tolerance | |||||||||||||||||||||
Catalytic cracking catalyst (FCC RFCC) | ||||||||||||||||||||||||||||||
ZCM-7 | .. | .. | . | . | ||||||||||||||||||||||||||
RHZ-200 | . | . | .. | |||||||||||||||||||||||||||
RHZ-300 | .. | . | . | . | .. | . | ||||||||||||||||||||||||
MLC-500 | ... | .. | ... | .. | .. | |||||||||||||||||||||||||
ORBIT-3000 | .. | .. | ... | .. | .. | |||||||||||||||||||||||||
ORBIT-3300 | ... | . | .. | .. | ... | ... | ... | |||||||||||||||||||||||
ORBIT-3600 | ... | ... | .. | ... | ... | ... | ||||||||||||||||||||||||
COMET-400 | ... | ... | .. | .. | .. | .. | ||||||||||||||||||||||||
ZC-7000 | .. | ... | ... | .. | .. | |||||||||||||||||||||||||
ZC-7300 | .. | .. | ... | .. | .. | |||||||||||||||||||||||||
Catalyst for maximum production of LPG and high octane gasoline
(MGG ARGG) | ||||||||||||||||||||||||||||||
RMG-2 | . | ... | ... | ... | . | .. | ||||||||||||||||||||||||
RAG-1 | .. | ... | ... | ... | .. | .. | ||||||||||||||||||||||||
RAG-6 | .. | ... | ... | ... | .. | .. | .. | |||||||||||||||||||||||
Deep catalytic cracking catalyst(DCC- DCC-) | ||||||||||||||||||||||||||||||
CRP-1 | .. | ... | ... | .. | .. | . | ||||||||||||||||||||||||
CIP-1 | .. | ... | ... | .. | .. | . | ||||||||||||||||||||||||
CIP-2 | .. | ... | ... | .. | .. | . | ||||||||||||||||||||||||
CIP-3 | ... | ... | ... | .. | . . | . | ||||||||||||||||||||||||
Catalyst for maximum production of iso-olefin(MIO) | ||||||||||||||||||||||||||||||
RFC-1 | .. | ... | ... | .. | .. | .. | ||||||||||||||||||||||||

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