CONTENT

EXPORT PRODUCT CATALOGUE

CATALYSTS, WHITE OIL, PETROLEUM COKE & WAXREFINERY & CHEMICAL PRODUCT EXPORT DIVISION

MARCH, 2010CONTENT41. Oil Refining Catalyst

4(1) Catalytic Cracking Catalyst

4Residue Cracking Catalyst

7Maximum Diesel Catalyst

8Olefin-Reducing Catalyst

10Special Catalyst for MGD Process

11Special Catalyst for ARGG Process

11Special Catalyst for DCC Process

12Special Catalyst for MIP-CGP Process

13(2) Catalytic Cracking Additive

13Catalytic Cracking Desulphurization Additive

14Catalytic Cracking Gas-Increasing Additive

14(3) Catalytic Reforming Catalyst

14Semi-Regeneration Reforming Catalyst

16(4) Hydroprocessing Catalyst

16Hydrorefining Catalyst

17Hydrorefining Catalyst for Clean Gasoline

17Catalytic Cracking Gasoline Selective Hydrodesulphurization

18Hydrorefining Catalyst for Clean Diesel

18Diesel Ultra Deep Desulphurization Catalyst

19Aviation Kerosene Hydroprocessing Catalyst

19Lube Hydrorefining Catalyst

20Lubricant Hydro-dewaxing Catalyst

20Paraffin Hydrorefining Catalyst

21Diene Selective Hydroprocessing Catalyst

21White Oil Hydroprocessing Catalyst

21Hydrocracking Catalyst

22Residue Hydro-demetallization Catalyst

23Residue Hydrodemetallization & Hydrodesuphurization Catalyst

23Residue Hydro-demetallization and Hydrodenitrogenation Catalyst

23Reforming Prehydroprocessing Catalyst

24Guard Catalyst

262. Polyolefin Catalyst

26(1) PE Catalyst Gas Phase Process

28(2) PE Catalyst Borealis Process

29(3) PE Catalyst Slurry Process

30(4) PP Catalyst Granular Shape

32(5) PP Catalyst Spherical Shape

333. Catalysts for Basic Organic Materials

33(1) Catalysts for Toluene Disproportionation and Transalkylation

33(2) Vinyl Acetate Catalyst

34(3) Acrylonitrile Catalyst

34(4) Pd/C Catalyst for Hydropurification of Terephthalic Acid

34(5) Silver Catalyst for EO/EG

35(6) Benzene and Ethylene Liquid Phase Alkylating Catalyst

35(7) Ethylbenzene Dehydrogenation Catalyst

35(8) Catalyst for Liquid-phase Selective Hydrogenation of Propyne and Propadiene in C3 Fractions

369Catalyst for Gas-phase Selective Hydrogenation of Acetylene in C2 Fractions

36(10)Catalyst for Selective Hydrogenation of Acetylene and MAPD in front-end process

37(11) Hydrogenation of Pyrolysis Gasoline

384. Other Catalysts

38(1) PX Sorbent

38(2) Non-crystal Alloy Hydrorefining Catalyst

38(3) Special Molecular Sieve Catalyst

39(4) Adhesive-Free 5A Small Spherical Molecular Sieve

39(5) C5/C6 Isomerization Catalyst

39(6) High-Temperature De-sulfurization Catalyst

39(7) De-Chlorination Catalyst

40(8): PA Catalyst

41Lube Base Oil

43White Oil

50Petroleum Coke

51Paraffin Wax

51Liquid Paraffin Wax

52Fully Refined Paraffin Wax

53Semi-Refined Paraffin Wax

54Microcrystalline Wax

55Specialty Wax

56Chewing Gum Special-Purpose Wax

Sinopec Catalyst Manual

Sinopec is the largest domestic producer and supplier of catalyst for oil refining and chemical purpose. Its main products include: oil refining catalyst, polyolefin catalyst, basic organic material catalyst and other catalyst etc. Besides meeting demands of domestic markets, products of Sinopec Catalyst are also exported to European, American, Asian, African and other international markets.

Sinopec advocates the construction of an enterprise team in type of Service, Study and Intelligence. It pursues the managerial philosophy of Quality the First and Service the Best and the enterprise spirit of Always Creative and Forever Vigorous. It will put into effect the competition strategy of product innovation, production efficiency, product diversity and producer development, in order to provide high-quality products and satisfying services for its vast customers. Sinopec is willing to establish long-term strategic partnership with its vast customers home and abroad, and to realize mutual progress and development.1. Oil Refining Catalyst

(1) Catalytic Cracking Catalyst

Residue Cracking Catalyst

ORBIT Series

Main purpose of ORBIT-3000 catalyst is to increase yield of gasoline and diesel oil in goal product. The following technological measures are taken in preparation process of this catalyst: adopting composite molecular sieve to endow this catalyst with both excellent coke selectivity and good activity stability; in production of ultra-stabilized molecular sieve, through modifying technology and exploiting middle holes of molecular sieve, the catalyst is suitable for cracking heavy oil macromolecules. With improved molecular sieve quality, it is effective to enforce macromolecule-cracking ability by means of modifying carrier into active alumina.

Based on basic performances of ORBIT-3000 catalyst (high cracking activity of macromolecules, good coke selectivity, suitable for heavy oil processing), ORBIT-3300 is a new-type RFCC catalyst successfully developed through replacing active components. This catalyst is suitable for RFCC plants with large processing capacity but low catalyst/oil ratio. Within flexible working range of the fractionator, debutanizer and gas compressor system, this catalyst can be used without any revamp on the plant. Through adjustment of active components in preparation process of ORBIT-3300, metal tolerance of the product has been improved for worse feedstock and uncertainties.

Aiming at processing high-vanadium feedstock from the Middle East and increasing total liquid yield, based on ORBIT-3300, ORBIT-3600 catalyst is a new type RFCC catalyst successfully developed through optimizing active components and modifying carrier. While improving performance of molecular sieve in preparation process, carrier is also modified, components with heavy metal resistance are also added, thus heavy metal resistance performance (especially vanadium) is effectively promoted; shape-selective zeolite component is also added to increase LPG yield appropriately.

ORBIT-3600B catalyst is a kind of anti-vanadium olefin-reducing catalyst based on anti-vanadium catalyst ORBIT-3600. Commercial results reveal that the catalyst has strong heavy oil cracking ability, high yield of light oil, high octane number of gasoline, strong olefin-reducing ability etc.

In order to realize the objective of reducing olefin content in gasoline on the basis of anti-vanadium heavy oil cracking catalyst ORBIT-3600, ORBIT-3600B has the following characters: through modification of Y-type molecular sieve and blending with active components, on the premise of maintaining heavy oil cracking activity, hydrogen transfer activity is strengthened to reach the goal of reducing olefin content in gasoline; acid distribution of catalyst is also adjusted reasonably to reduce the generation of coke and dry gas.

ZC Series

On the basis of successfully developed new one exchange, one calcination preparation technology and increased crystallinity of ultra-stable molecular sieve, ZC series catalyst has been developed through modifying active components, adjusting hole structure of carrier and gradient distribution of active catalyst components. Due to the above modifying technologies, ZC series catalysts are of high activity and stability, excellent coke selectivity, strong residue oil macromolecule cracking ability, high heavy metal resistance performance, high yield of high-value product and low unit cost of catalyst etc.

ZC-7000 catalyst is especially suitable for heavy oil cracking installations that use VRDS residue oil and residue oil as feedstock, where it is difficult for catalyst of high bulk density to fluidize. With this catalyst, material resources can be extended; meanwhile yield of light oil can be increased.

ZC7300 catalyst has higher activity than ZC-7000 catalyst, and is suitable for heavy oil cracking installations using VRDS residue oil that is hard to be cracked. For installation of low catalyst/oil ratio, ideal product distribution can also be achieved.

ZC-7000B is developed on the basis of ZC-7000, through treating with modification technology, olefin-reducing ability is strengthened, and olefin content in gasoline can be reduced by 5~6 units.

DVR Series

DVR-1 RFCC catalyst is a specially formulated catalyst for catalytic cracking installations that use entire vacuum residue oil as feedstock (abbreviated as VRFCC technology). VRFCC technology can further increase blending ratio of residue oil in catalytic cracking process, and increase economic benefit of oil refining enterprises to the full extent.

In order to meet the demand for blending various vacuum residue oils by large scale, the following technological measures are mainly taken in the preparation process of DVR-1 catalyst: treating ultra-stable molecular sieve with modification technology and exploiting large and middle holes of ultra-stable molecular sieve, which enables DVR-1 catalyst to crack heavy oil macromolecules; treating carrier with activation technology to improve acid distribution and hole distribution of carrier, so that cracking ability of carrier to residue oil macromolecule can be enhanced effectively. Additive technology is adopted to improve heavy metal resistance performance (especially nickel). Through optimization of production technology and post-treatment, regeneration activity and stability of catalyst is improved. For most domestic existing cracking installations, without the need to revamp plants, this catalyst has very broad spreading and application prospect in oil refining with large blending ratio of various residue oils.

To meet the demand for improving product distribution and reducing olefin content in FCC gasoline, DVR-2 catalyst is a product suitable for VRFCC process, while maintaining olefin-reducing performance. Results of industrial application reveal that on the premise of maintaining various performances of DVR-1 catalyst, DVR-2 catalyst can reduce olefin content in FCC gasoline as well.

CC-15 Series

CC-15 catalyst adopts REUSY molecular sieve as its main active component. The carrier has certain cracking activity, middle bulk density, high strength and certain heavy oil cracking ability. It can be used in catalytic cracking installations which use entire VGO or oil blended with less than 15% VR as feedstock. CC-15 can also be used in RFCC installations fed with entirely paraffin based ATB, or with small amount of poor-quality CGO or DAO. It has been commercially applied in nearly thirty domestic catalytic cracking installations, including FCC installations fed with blended VTB and RFCC installations with entire ATB. CC-15 (M) catalyst can also increase octane number of gasoline.

CHZ-4

CHZ-4 catalyst adopts new generation ultra-stable SRY molecular sieve as its main active component, which is prepared by withdrawing aluminum and replenishing silicon with hydrothermal + chemical method. SRY molecular sieve integrates advantages of molecular sieves prepared with hydrothermal and chemical method, possesses excellent thermal and hydrothermal stability, more secondary pore and strong heavy oil cracking ability. It has little non-framework aluminum inside with cleaning channels, therefore non-selective cracking reaction is avoided to the most extent, and coke selectivity is especially excellent. SRY molecular sieve is a new generation ultra-stable molecular sieve with international advanced level developed in the middle 1990s.

In order to meet the demand of nickel and vanadium resistance, and further enhance conversion ability to heavy oil, kaolin earth with fine particle, large specific surface area and high activity is adopted as carrier, which is blended with active alumina to enhance cracking ability of heavy oil. CHZ-4 catalyst has been widely used in ten sets of domestic catalytic cracking installations of heavy oil. Under high blending ratio of residue oil, product distribution is still very good.

CHN-1

CHN-1 is of excellent anti-alkali nitrogen performance, which has been specially developed for high content of alkali nitrogen feedstock inside Sinopec.

CHN-1 catalyst also adopts new generation ultra-stable SRY molecular sieve as main active component, which is prepared by withdrawing aluminum and replenishing silicon with hydrothermal + chemical method. In order to meet the demand of alkali nitrogen resistance and further enhance conversion ability to heavy oil, kaolin with fine particle, large specific surface area and high activity is adopted as carrier, which is blended with active alumina to enhance cracking ability to heavy oil.

CHV Series

CHV series catalyst adopts new generation ultra-stable SRY molecular sieve as main active component, which is prepared by withdrawing aluminum and replenishing silicon with hydrothermal + chemical method. SRY molecular sieve has high silicon/aluminum ratio, little non-framework aluminum and good hydrothermal stability. Meanwhile, it has excellent coke selectivity, isomerization performance and strong cracking ability to heavy oil. Core technology of anti-vanadium catalyst is the setting of vanadium trap, and amount of traps is determined by the vanadium content in processed feedstock. In order to improve cracking ability to heavy oil and anti-contamination ability from heavy metal, active alumina is also introduced. Other special components can also be added if there is need to increase yield of LPG or octane value. Under normal catalyst consumption, this catalyst can be used in catalytic cracking installations of heavy oil containing 4000~10000 ppm vanadium on E-cat. Series of anti-vanadium catalysts can be produced, and special catalyst can be tailored according to the practical situation of customers installation.

DOCP, DOCR

This series of heavy oil cracking catalyst is mainly designed for various heavy oil catalytic cracking installations where gasoline octane number is needed to upgrade. With such catalyst, 90# or higher grade gasoline can be produced directly. It is especially suitable for heavy oil catalytic cracking installations which process paraffin based feedstock.

ZRP-3 (RPSA) shape selective molecular sieve is introduced in DOCR catalyst as kernel active component, which has high thermal and hydrothermal stability, C3= and C4= increasing ability and isomerization ability. Octane value of gasoline and yield of LPG can both be increased.

ZRP-5 shape selective molecular sieve is introduced in DOCP catalyst as kernel active component, which has stronger isomerization ability than RPSA, and can transform straight chain gasoline into branch chain. So, octane value of gasoline can be increased, while yield of light oil and LPG is basically not influenced.

While obtaining perfect products distribution, at the same time, improving FCC gasoline octane number, the series catalysts are all applicable for processing blended heavy oil.

Maximum Diesel Catalyst

MLC-500, MLC-500ZA

MLC-500 heavy oil catalytic cracking catalyst is of high hydrothermal stability, strong anti-contamination ability from heavy metal, high remaining activity, high mechanical strength and strong cracking ability under rigorous conditions, and has prominent effect in increasing diesel/gasoline ratio. In commercial application, this catalyst can process heavy feedstock well and increase yield of light oil. In conjunction with corresponding technology, yield of diesel oil can be increased. With MLC-500 catalyst, by adopting multi-section feeding and selective cracking technology, product quality can be improved, and octane value of gasoline can be increased.

Main design thought of MLC-500 heavy oil catalytic cracking catalyst is to enhance cracking ability for heavy oil, to limit further cracking of intermediate fractions, and to make reasonable adjustment on matrix/zeolite ratio and acid distribution. Main technological measures include: increase surface cracking activity of large and middle pores and control activity of small pores; strengthen cracking ability to heavy oil through increasing conversion activity and selectivity of the matrix; adopt ultra-stable Y molecular sieve and adjust its acid distribution to make full use of its macromolecule cracking characteristic and limit its cracking function to intermediate fractions.

MLC-500ZA is a tailor made large bulk density catalyst specially developed for a 3 million t/a FCC plant of Zhenhai Petrochemicals Branch. Feedstock of the installation is mainly VGO blended with about 10% coker gas oil. On the premise of blending more residue oil, the product series can increase yield of diesel oil and octane value of gasoline. MLC-500ZA catalyst has high selectivity of LPG and gasoline with high octane value.

CC-20D Series

CC-20D is a maximum diesel FCC catalyst with high activity and coke selectivity etc. On the premise of ensuring conversion ability to heavy oil, activity of large pores of carrier is increased, and high yield of light oil is achieved. CC-20D series catalyst adopts complex molecular sieve preparation technology, varieties and ratio of PSRY, REUSY and SRCY molecular sieves are adjusted, selective RPSA or ZRP-5 zeolite with different Si/Al ratio is also adopted. On customers demand, maximum diesel catalyst considering LPG, octane value and anti-vanadium ability can be produced.

CC-20DV is a maximum diesel catalyst considering anti-vanadium ability.

CC-20DF is a catalyst product specially designed for double-riser technology.

CC-200D

CC-200D is a kind of diesel oriented catalyst with mid bulk density. Yield of LPG, anti-contamination from vanadium and blending with residue oil are taken into consideration simultaneously.

Olefin-Reducing Catalyst

GOR-C, GRV-C

GOR-C olefin-reducing catalyst adopts modified Y molecular sieve, MOY, as its main active component, which is modified with unique oxide and endowed with excellent hydrogen transfer activity, fine coke selectivity and excellent cracking ability to heavy oil. The catalyst has high activity and strength, which can realize selective hydrogen transfer reaction and ensure effective utilization of hydrogen resource in feedstock and reasonable distribution in product. This catalyst also has the ability to reduce olefin in FCC gasoline prominently by 10~15V%. Combined with operation techniques, olefin content in FCC gasoline can be steadily controlled under 35V%, while content of isomerized alkane and aromatics can be increased and yield of LPG keeps at a high level.

GRV-C is a kind of new type high-efficiency anti-vanadium olefin-reducing catalyst. This catalyst is composed of active components and carrier with high cracking activity to heavy oil and good coke selectivity, which are specially developed toward intermediate feedstock. Semi-synthesized carrier bonded with alumina is adopted to improve anti-contamination ability of catalyst from heavy metal. PTI preparation technology of catalyst is developed to improve interfacial adhesion between carrier and molecular sieve, and further increase anti-abrasion strength. Cracking activity and hydrogen transfer activity are adjusted and appropriately matched to endow the catalyst with both olefin-reducing function and strong cracking ability to heavy oil. AEP matrix is also adopted to adjust acid distribution and pore distribution of catalyst to achieve good coke selectivity.

CDC

CDC is a brand-new chemically designed catalyst with gradient pore distribution and gradient acid center, which makes it possible for heavy oil macromolecule to access active center and being of excellent desorbing/diffusing ability. CDC catalyst possesses excellent activity and stability, profound conversion ability to heavy oil and high hydrogen transfer activity. Coke can be reduced at the same time. Through formulation adjustment, it can increase propylene content in product. As a new type FCC catalyst, it can meet various demands of oil refiners.

COR Series

This series of olefin-reducing catalysts adopt modified Y molecular sieve, MOY, as its main active component, which is modified with unique oxide and endowed with excellent hydrogen transfer activity, fine coke selectivity and excellent cracking ability to heavy oil. The catalyst has high activity and strength, which can realize selective hydrogen transfer reaction and ensure effective utilization of hydrogen resource in feedstock and reasonable distribution in product. This catalyst also has the ability to reduce olefin in FCC gasoline prominently by 10~15V%. Combined with operation techniques, olefin content in FCC gasoline can be steadily controlled under 35V%, while content of isomerized alkane and aromatic hydrocarbon can be increased.

COR-C catalyst is suitable for catalytic cracking installation with non-paraffin based feedstock.

CORV is suitable for catalytic cracking installation with feedstock of heavy metal, especially vanadium.

CORH has excellent anti-contamination performance from metal.

CORS is of high yield of diesel oil and high octane value of gasoline.

DOCO

DOCO olefin-reducing catalyst is good for selective hydrogen transfer reaction, which can control the coke and dry gas yield effectively and ensure liquid yield. This catalyst has the ability to reduce olefin in gasoline prominently by 10~11V% at the same time, and olefin content can be steadily controlled under 35V%, which can meet the demand of new standard gasoline. This catalyst also has strong isomerization ability, and isomerization index (isobutane to isobutene ratio in LPG) can be increased by 1.02~1.05%, isoalkane in gasoline can be increased by 8.09%, aromatic can be increased by 1.89%, which is very important to keep octane number.

GOR-II

Based on industrial applications of the first generation olefin-reducing catalyst, GOR-II is developed to meet the demand of oil refining plants to improve product distribution and further enhance cracking ability to heavy oil.

GOR-II catalyst has the following characters. Effective match of selective hydrogen transfer activity and cracking activity is ensured through performance improvement and blending of active components. Good selective hydrogen transfer activity can ensure olefin-reducing effect to gasoline, while high cracking activity can increase conversion with heavy oil. New type matrix is adopted to control pore distribution and increase medium pore proportion to enhance heavy oil cracking ability, increase yield of diesel oil, and restrain coking at the same time. Acid distribution of catalyst is adjusted properly to reduce coke and dry gas.

GOR-III

The third generation olefin-reducing catalyst, GOR-III, is developed to further improve olefin-reduction performance. Through further modification of main active components, selective molecular sieve and matrix, olefin-reducing margin and cracking ability is further enhanced, hydrothermal stability of catalyst is elevated, coke selectivity and product distribution is improved. Industrial application result reveals: in comparison with the second generation olefin-reducing catalyst, E-cat activity of GOR-III can be decreased by 3% more and octane value of gasoline is elevated slightly.

RMS-8

In order to meet the increasingly diversifying demands of customers for product distribution, RMS-8 catalyst is a new type residue FCC catalyst developed to increase gasoline yield and reduce olefin of gasoline. Commercial application result reveals that RMS-8 has strong cracking ability to heavy oil macromolecule, high gasoline yield, good anti-contamination ability from heavy metal, and appropriate olefin reducing ability etc.

Special Catalyst for MGD Process

RGD-1

RGD-1 is a catalyst of excellent cracking ability to heavy oil macromolecule. It can selectively restrain further cracking of intermediate fractions and enhance secondary cracking of gasoline fraction, so that yield of diesel oil and LPG in catalytic cracking installation can be raised at the same time. By adjusting density and strength of molecular sieve active centers, hydrogen transfer reaction is increased appropriately, and olefin content in gasoline is lowered. In its preparation process, the following measures are taken: through modification of kaolin, pores bigger than 100 and smaller than 5 are increased to make carrier have good pore distribution gradient. Moderate weak-acid big pores can crack macromolecule hydrocarbon, restrain secondary cracking of intermediate fractions, and reduce coking. Moderate strong-acid small pores can further crack gasoline into LPG. Introduction of metal components in active centers adjusts acid strength properly, and enhances cracking degree of gasoline into LPG. Meanwhile hydrogen transfer ability in gasoline is elevated, which is favorable for reducing olefin content in gasoline. Adoption of modified selective molecular sieve is favorable for increasing yield of LPG and octane value of gasoline.

RGD-C

RGD-C catalyst has good industrial application effect on increasing yield of LPG and diesel oil. Modified and composite ultra-stable molecular sieve is adopted in RGD-C catalyst, appropriate selective molecular sieve and trapping components for metal contaminations are added, and content of middle-pore active components are increased. This catalyst has strong conversion ability to heavy oil, strong anti-contamination ability from heavy metal, good coke and dry gas selectivity. Less coke and dry gas can be achieved in reaction of gasoline under rigorous condition. RGD-C can selectively crack gasoline to LPG with high yield of LPG and diesel oil.

CMOD Series

CMOD catalyst adopts multiple high-performance molecular sieves (ultra-stable Y molecular sieve, RPSA molecular sieve etc) as its active components. It is produced with high solid content technology. With high activity and strength, CMOD catalyst has prominent effect in increasing yield of diesel oil and LPG. When yield of LPG reaches 15~20m%, yield of diesel oil is basically maintained. CMOD catalyst has good vanadium resistance. CMOD catalyst also has good basic nitrogen resistance, where large proportion coking gas oil can be processed.

CMOD-100 can tolerate vanadium over 10,000 ppm on E-cat.

CMOD-200 catalyst can tolerate vanadium 5,000~10,000 ppm on E-cat.

Special Catalyst for ARGG Process

RAG Series

RAG-1 catalyst is specially designed for ARGG technology. It is especially suitable for processing feedstock blended with high content of residue oil, such as entire ATB, VGO blended with high proportion of ATB, VTB or de-asphalt oil. In preparation process of RAG-1 catalyst, performance of carrier is specially improved to make its distribution of secondary pores more perfect according to the characters of ATB feedstock. Meanwhile coordination and match between molecular sieve component and carrier performance are optimized. As a result, RAG-1 catalyst has stronger conversion ability to heavy oil, better product selectivity and heavy metal resistance. Its main characters are: stable structure, good pore distribution gradient, which makes molecules of various sizes, especially macromolecules contact and react with active centers selectively and thoroughly. Macromolecules can contain deposit of heavy metal. With high activity and good selectivity, its conversion ability to heavy oil and anti-contamination ability from heavy metal nickel is very strong.

RAG-6 catalyst is also specially designed for ARGG technology, with performance of strong conversion ability to heavy oil and heavy metal resistance. Its main characters are: It has stable structure, good pore distribution gradient, which makes molecules of various sizes, especially macromolecule contact and react with active centers selectively and thoroughly, meanwhile macromolecules can contain deposit of heavy metal. It has high activity, good selectivity, especially strong conversion ability to heavy oil and anti-contamination ability from heavy metal nickel. In comparison with RAG-1 catalyst, RAG-6 catalyst has larger pore size, higher activity and better heavy metal (especially nickel) resistance. In addition, by adopting of new type selective molecular sieve in preparation process, better selectivity is achieved.

RAG-7A is a catalyst with large bulk density, which is specially designed for the 600,000 t/a ARGG installation of Gaoqiao Refinery where 50% vacuum residue oil is blended in. Besides possessing inherent high activity and stability of RAG series catalyst, RAG-7A has high yield of LPG (especially propylene) and 90# gasoline with high octane value.

Special Catalyst for DCC Process

MMC-2, CIP-2

In order to meet the growing demand for propylene in market, based on special catalyst of original DCC-I technology, MMC-2 is a new generation catalytic pyrolysis catalyst developed through modification of active components, with which a higher yield of propylene and cracking ability to heavy oil can be achieved.

CIP-2 is a special catalyst for DCC-II catalytic pyrolysis technology. To meet the demand of high light olefin yield with residue oil as blended feedstock, CIP-2 must possess high activity for heavy oil and restrain activity for hydrogen transfer reaction. In preparation process of CIP-2, multi-function active components and other modification technology are applied to endow CIP-2 catalytic pyrolysis catalyst with high cracking activity, high stability, good olefin selectivity, high octane value of gasoline and strong anti-abrasion performance.

Special Catalyst for CPP Process

CD002

Combining catalytic pyrolysis process (CPP) with matched catalyst CD002, under the reaction temperature of 560~650 , light olefin, dominant in ethylene and propylene, can be produced with heavy petroleum hydrocarbon as feedstock. Furthermore, by controlling reaction condition, yield ratio of ethylene to propylene can also be adjusted to meet the demand change with flexibility. CD002 catalyst contributes to both high yield of light olefin and high hydrothermal activity and stability. It can meet rigorous operation demand of catalytic pyrolysis technology.

Special Catalyst for MIP Process

CR022

MIP is an FCC process that directly produces gasoline with low olefin content and high octane value. Its kernel technology is to revamp existing FCC riser reaction system appropriately, and divide conventional single reaction section into two reaction sections with different reaction temperature and reaction time. MIP technology makes catalytic cracking reaction proceed in each reaction section controllably and selectively, and realizes the goal to produce maximum isomerized alkane and FCC gasoline with low olefin content and high octane value directly.

CR022 catalyst is specialized for MIP technology. Industrial application result reveals that it has high heavy oil cracking performance, good coke selectivity, high yield of light oil and prominent olefin-reducing function.

CRMI-2

CRMI-2 catalyst is specialized for MIP technologywhich possesses the characters of high activity, high thermal and hydrothermal stability and good coke selectivity. In conjunction with MIP technology, it can reduce olefin content in gasoline, and maintain RON at the same time. CRMI series catalyst adopts preparation technology of composite molecular sieves, variety and ratio of molecular sieves (PSRY or REUSY) are adjusted, and selective molecular sieves (RPSA or ZRP-5) with different Si/Al ratio are adopted to increase yield of propylene on the premise of maintaining heavy oil conversion and total liquid yield.

Special Catalyst for MIP-CGP Process

CGP-1

MIP-CGP is an FCC technology with maximum isomerized alkane, higher yield of propylene and lower olefin content in gasoline. CGP series catalyst is a special designed catalyst for the process. Considering practical condition in specific Refinery and in conjunction with MIP-CGP technology, CGP-1 catalysts can guarantee olefin content in catalytic gasoline to meet Europe II or Europe III emission standard, on the premise of maintaining the same capacity of original installation, while octane value of gasoline is not lowered; yield of propylene (relative to material oil) is over 7~8m%.(2) Catalytic Cracking Additive

Catalytic Cracking Desulphurization Additive

MS011

FCC gasoline is the main blending component of vehicle gasoline. To reduce sulfur content in catalytic gasoline is one of the effective measures to meet new international gasoline standard. Sulfur-reducing additive MS011 can effectively reduce sulfur content by 15~20m% in FCC gasoline, while not influencing distribution of products.

Catalytic Cracking Propylene-Increasing Additive

MP031

MP031 is developed to increase the propylene content in LPG aiming at the increasingly growing demand for propylene in current market. Industrial application result reveals that under the same operating condition, with a proportion of 4~8m% additive, yield of propylene (relative to feedstock) can increase by 0.5~0.8m% on the premise of small increase in yield of LPG.

CHPA Series

CHPA is a kind of FCC additive to obtain high yield of propylene developed by RIPP. This additive adopts metal modified ZSM-5 molecular sieve as active components, and is prepared with particular carrier technology. The product has certain MAT activity without any influence to activity of the main catalyst. It can increase propylene content in LPG (i.e. yield of propylene) while maintaining conversion rate and total liquid yield.

Catalytic Cracking Gas-Increasing Additive

CA Series

CA series additive is jointly developed by RIPP and Sinopec Catalyst Changling Division. Main products include CA-1 catalytic cracking LPG-increasing additive, CA-2 catalytic cracking gasoline octane value-increasing additive, CA-100 high-efficiency catalytic cracking LPG-increasing additive, CA-3 catalytic cracking LPG-increasing additive of middle bulk density, CA-200 high-efficiency catalytic cracking gasoline octane value-increasing additive etc. CA series catalytic cracking additives contain MFI shape selective zeolite and other various molecular sieves as active components with strong cracking ability to heavy oil, strong isomerization ability, good coke selectivity and heavy metal resistance. In catalytic cracking installation, it can be used together with catalytic cracking catalyst at any ratio. It is an ideal catalytic cracking additive considering high yield of diesel oil and gas olefins or production of gasoline with high octane value.

(3) Catalytic Reforming Catalyst

Semi-Regeneration Reforming Catalyst

CB Series

CB series catalyst is made of high-purity Al(OH)3 powder, by molding and sintering to make spherical or strip -Al2O3 carrier, then infused with Pt and Re active components to get the catalyst product. Catalyst product is available either in oxidative state or in reductive state. Reductive state catalyst can lessen unit start-up time.

Among CB series catalyst, CB-6, CB-7, CB-9, CB-60 and CB-70 are semi-regeneration reforming catalysts developed by RIPP and produced by Sinopec Catalyst Changling Division. CB-6, CB-7, CB-9 catalysts have spherical shape, and CB-60, CB-70 catalysts have strip shape. Re-to-Pt ratio of CB-6, CB-60 catalysts is 1, and Re-to-Pt ratio of CB-7, CB-70 catalysts is higher than 1. The catalysts, such as CB-6/CB-7, CB-60/CB-70 adopt two-section filling process in commercial application. In comparison with CB-6, content of precious metal Pt in CB-7 catalyst is lowered by 30% while content of precious metal Pt in CB-60 catalyst is lowered by 20%. Reaction performance evaluation and commercial application result reveal that CB series catalysts performance has exceeded the level of imported reference catalyst with the characters of simple start-up procedure, short start-up time, low hydrogen consumption etc. Catalyst can be adjusted to water and chlorine balance quickly and effectively in normal running process. Regeneration is easy and safe by adopting a dry method pressurized process, which simplifies coke burning procedure, shortens coke burning time, lessens surface area loss and chlorine loss. Catalyst performance can be recovered very well after regeneration. Catalyst can be regenerated either on-site or off-site, and off-site regeneration has more advantage. CB series catalyst has been used more than sixty plants not only by domestic customers, but also by overseas customers.

PRT Series

PRT-A, PRT-B, PRT-C, PRT-D are new generation strip multi-metal semi-regeneration catalytic reforming catalysts developed by RIPP and produced by Changling Division. They have the characters of high carrier purity, proper pore distribution, high strength and chlorine-holding ability. Selectivity and stability are further improved, and carbon deposit velocity is decreased.

PRT-A and PRT-C are multi-metal catalysts of which Re-to-Pt ratio is 1, and PRT-B and PRT-D are multi-metal catalysts of which Re-to-Pt ratio is higher than 1. Two-section filling process is adopted in commercial application, for example, PRT-A and PRT-B are filled together, PRT-C and PRT-D are filled together. PRT-A/ PRT-B have the same performance with PRT-C/ PRT-D basically. In comparison with CB-60/ CB-70 catalysts, conversion rate of aromatic with PRT-A/ PRT-B and PRT-C/ PRT-D can be increased by over 5%, liquid yield can be increased by over 1%, while carbon deposit can be decreased by over 18% under the same reaction condition. Catalysts activity, selectivity and stability have all reached international advanced level with good regeneration performance and feed adaptability, and excellent processing ability even for lean naphthenic straight-run oil and secondary processing oil. In commercial application, continuous running time of PRT-A/PRT-B and PRT-C/PRT-D reached thirty months and twenty-nine months respectively in the first period. PRT series catalyst keeps the characters of CB series for applied process. Presently, PRT series catalyst has already been applied in ten plants.

Continuous Reforming Catalyst

GCR Series

GCR series catalyst is a new generation continuous reforming catalyst with high activity and hydrothermal stability developed by RIPP.

The obvious characteristic of the new generation GCR series continuous reforming catalyst is its improved activity. It is increased by 6 to 8 degrees centigrade in comparison with previous generation reforming catalyst applied widely in the domestic units. At the same time, due to the adoption of new type catalytic materials, the ability of anti-high temperature hydrothermal treating is improved significantly, the surface area decreasing rate is slowed, and its life time is prolonged double times more than previous generation, which improves the economics sharply. Moreover, the chlorine-holding ability is increased, and the injected chlorine quantity can be reduced to half, which can inhibit the chloride corrosion of downstream process obviously. The mechanical strength of the product is improved, with better anti-abrasion performance and less dust from circulation and transportation.

Within GCR series, GCR-100 is an economic catalyst with low Pt content, while GCR-100A has a slightly higher Pt content. GCR series catalyst product is in reductive state with small sphere diameter of 1.4~2.0 mm.

The new generation GCR series continuous reforming catalyst is suitable for the reforming process aiming at high-octane number gasoline, aromatic, and hydrogen with feedstock of straight-run naphtha, hydrocracking heavy naphtha, pyrolysis gasoline, coking gasoline, catalytic gasoline, condensed oil etc.

RC Series

RC series is a one of the newest generation, high selective and low carbon-depositing rate catalyst developed by RIPP in recent years. RC011PS-VI was applied successfully in Zhenhai Refinery Branch. RC011 is an economic catalyst with lower Pt content, and Pt content, while RC031PS-VIIhas a slightly higher Pt content.

RC series continuous reforming catalyst has obvious characteristics as follows: It has good selectiveness, with high C5+ liquid yield, and increased aromatic and hydrogen yield. Carbon-depositing rate decreases obviously for more than 20% under the same rigorous reacting condition. At the same time, good hydrothermal stability, chlorine-holding ability and excellent mechanical strength are kept.

The newest RC series continuous reforming catalyst is suitable for the reforming process aiming at high-octane number gasoline, aromatic, and hydrogen with feedstock of straight-run naphtha, hydrocracking heavy naphtha, pyrolysis gasoline, coking gasoline, catalytic gasoline, condensed oil etc. Because of the low carbon-depositing rate, it makes special sense for the capacity expanding and revamping, especially for the continuous reforming plants with a constrained regeneration ability. (4) Hydroprocessing Catalyst

Hydrorefining Catalyst

RN Series

RN-1 catalyst has high hydro-denitrogen, hydro-desulfur and hydro-dearomatics activity, high activity stability and wide adaptability to various feedstock with active component of Ni-W. It possesses high mechanical strength, low bed pressure drop and good regeneration performance. In April 1987, the first industrial application of this catalyst was carried out in Guangzhou Petrochemical Company, and great success was achieved. Its performance has reached international advanced level.

It is applicable for hydrorefining of straight-run fraction of high-nitrogen and high-sulfur content, such as gasoline, reforming feedstock, kerosene, jet fuel, straight-run diesel, vacuum gas oil, and lube oil.

It is applicable for hydrorefining of secondary processing fraction of high-nitrogen and high-sulfur crude, such as viscosity-breaking gasoline, catalytic cracking diesel, coking diesel, coking gas oil, mixture of coking gas oil and straight gas oil.

It is applicable for moderate and high pressure hydrocraking of high-nitrogen and high-sulfur crude, and hydrodenitrogenation and aromatic saturating of feedstock, also applicable for moderate pressure hydro-upgrading processing for refining section feedstock, such as hydrodenitrogenation of vacuum gas oil, residue catalytic cracking diesel, feedstock from atmospheric line 3 and vacuum line 1.

RN-2 is a trilobe-shape catalyst with active component of Ni-W. Besides possessing all the properties of RN-1, RN-2 catalyst increases HDN activity by 15% in comparison with RN-1. In August 1993, RN-2 was industrially applied in Changling Refinery.

RN-2 can be applied within all the range of RN-1, besides, it is especially suitable for hydrotreating of inferior feedstock (such as vacuum gas oil, coking gas oil), and pre-refining of feedstock for moderate-pressure and high-pressure hydrocracking.

RN-10 is a trilobe-shape catalyst with active component of Ni-W. RN-10 is an updated and substituted product for RN-1, with higher hydro-denitrogen, hydro-desulfur and hydro-dearomatics activity. In April 1997, the first industrial application of RN-10 was carried out in diesel hydroprocessing plant of Guangzhou Petrochemical Company, and great success was achieved.

RN-10 can be applied within all the range of RN-1, besides, it is especially suitable for processing imported high-sulfur fraction and domestic high-nitrogen fraction. It also give technical support to production enhancing.

RN-10B is a butterfly-shape catalyst with active component of Ni-W with high hydro-denitrogen, hydro-desulfur, hydro-dearomatics activity, high anti-crush strength and bed porosity, and dramatically decreased bed pressure drop. RN-10B can be applied with diversified feedstock as well.

RN-10B catalyst was applied in the diesel hydroprocessing plants of Sinopec Jingmen Branch and Sinopec Jinan Branch successfully.

RN-10B catalyst can be applied to straight-run fraction (such as gasoline, kerosene, straight-run diesel etc.) and secondary processing fraction (such as coking gasoline, coking diesel, coking gas oil, catalytic cracking diesel etc.). RN-10B is especially suitable for the production expanding plants that need to decrease pressure drop, and the new and old plants that need to improve the product quality.

RN-32 (including RN-32V) is a new generation high-performance hydrorefining catalyst developed by RIPP after complete optimization with very high de-nitrogen and de-sulfur activity. Compared with RN-2 catalyst, under reaction temperature of 375~385 , hydrogen pressure of 8.0 Mpa and volume space velocity of 1.0 h-1, de-nitrogen activity is increased by 20~28%, de-sulfur activity is increased by 82~136%, while maintaining good activity stability. RN-32V catalyst has already been applied in Sinopec Jinan Branch, Sinopec Changling Branch and Sinopec Jingmen Branch successfully.

RN-32 catalyst is suitable for preprocessing of hydrocracking feedstock, hydrotreating of gas oil, and catalytic cracking feedstock. RN-32 (including RN-32V) can not only solve the processing problem of high-nitrogen oil, but also give technical support to production expanding.

Hydrorefining Catalyst for Clean Gasoline

Catalytic Cracking Gasoline Selective Hydrodesulphurization

RSDS Series

RSDS series catalysts include RGO-2 guard catalyst and RSDS-1 selective hydro-desulfur catalyst, which can meet clean gasoline specification of Europe-III and Europe-IV emission standard for sulfur content. RSDS series catalysts have characteristics as follows: GRO-2 guard catalyst has weak acidity, high operation space velocity, strong low-temperature de-diene ability etc. In hydro-treating process of FCC gasoline, it can be used for long term operation, with main catalyst protected. RSDS-1 selective hydro-desulfur catalyst has high hydro-desulfur activity, low olefin and aromatics saturating activity, strong octane-holding ability, with good activity stability.

It is applicable for low-sulfur gasoline production with low octane loss when hydroprocessing high-sulfur content catalytic cracking gasoline.

Catalytic Cracking Gasoline Hydro-isomerization Desulphurization & Olefin-reduction

RIDOS Series

Catalytic Cracking Gasoline hydro-desulfur olefin-reducing technology (abbreviated as RIDOS technology), uses olefin-rich FCC gasoline as its feed, and separates gasoline into two fractions, light fraction and heavy fraction according to product objective and feed property. Light fraction is extracted and refined with alkali to remove thiol, while heavy fraction is hydro-desulfurized and olefin reduced and finally light fraction and heavy fraction are blended to get full-fraction gasoline product. This technology can be utilized in production of clean gasoline with sulfur content lower than 200 ppm, olefin content lower than 20 V%, and loss of anti-explosion index less than 2 units. It is recognized that RIDOS technology has reached advanced level in international like technologies.

Catalysts applied in RIDOS technology include RGO-2 guard catalyst, RS-1A hydro-refining catalyst and RIDOS-1 hydro-isomerization catalyst. Characters of RIDOS series catalysts are proper shape with strength increase and diffusion resistance decrease, high diene saturating performance, high hydro-desulfurization, olefin saturating and isomerization activity, efficient coke restrain and long-term operation. Its desulfurization rate is over 90%, olefin saturating rate over 60%, with minor loss of octane value. RIDOS technology was applied on the 220,000ton/a hydro-treating process of FCC gasoline successfully in Yanshan Branch.

It is applicable for deep desulfurization and olefin-decreasing of olefin-rich FCC gasoline, and object product is clean gasoline with low octane number loss.Hydrorefining Catalyst for Clean Diesel

Diesel Ultra Deep Desulphurization Catalyst

RS-1000

RS-1000 is a new generation high-performance diesel ultra deep desulphurization catalyst developed by RIPP with complete optimization. The active component of RS-1000 is Ni-W. It has excellent hydrodesulphurization and hydrodenitrogenation activity, and hydrodesulphurization performance has reached international advanced level of similar catalysts. Not only Europe III standard, but also Europe IV standard can be met when RS-1000 is used to produce diesel by refineries, and diesel with 50 (g/g or 10 (g/g ultra low sulfur content is available under the hydrorefining condition of 3.26.4MPa hydrogen pressure. RS-1000 was industrially applied in Sinopec Jingmen Branch in 2005, and the product clean diesel met Europe III standard. Because there is great potential demand for ultra low sulfur clean diesel in China, RS-1000 has broad application prospect.

This catalyst can be used either in hydrotreating of diesel oil under high space velocity for low-sulfur diesel oil meeting Europe III standard, or under normal hydro-refining condition for low-sulfur diesel oil meeting Europe IV standard with good adaptability to various diesel oil, including high-sulfur and high-nitrogen diesel oil.

Inferior Diesel Deep Hydrotreating Catalyst

RIC Series

Developed by RIPP, containing metal components (Ni and W) and molecular sieve, RIC-1/RIC-2 catalysts are used to raise cetane value and decrease density of diesel oil from FCC process with residue oil blended feedstock. These catalysts have high saturating activity to aromatics, high cracking activity, good selectivity, high activity to remove sulfur and nitrogen. They can improve cetane value by more than 8~12 units, decrease diesel oil density by more than 0.035 g/cm3, and diesel yield is more than 95%. Clean diesel with less than 50ppm sulfur content can be obtained, and the quality of inferior diesel oil such as FCC diesel oil can be upgraded.

RIC-1/RIC-2 catalysts are mainly used to upgrade the quality of inferior diesel such as FCC diesel. RIC-1/RIC-2 catalysts can either act as hydrotreating catalysts in the single catalyst and single section process, or act as hydrocracking catalysts in the double catalysts and double sections process.Aviation Kerosene Hydroprocessing Catalyst

RSS-1A

Aiming at the character of straight-run aviation kerosene, RIPP developed a jet fuel hydro-dethiol patent technology (RHSS technology) with a whole package of new hydro-dethiol RSS-1A catalyst and matched mild technological process. Industrial application result reveals that, under mild technological condition (reaction temperature of 235~247 , reaction pressure of 0.7~1.3 Mpa, volume space velocity of 4.0 h-1, and hydrogen/oil ratio of 30~55 V/V), RHSS technology has good de-thiol and de-acid effect, certain function to remove sulfur, raise smoking point and upgrade color of product, and product performances meet the quality standard of 3# jet fuel. RSS-1A catalyst has stable performance, and can meet the industrial demand for long-period operation. RSS-1A catalyst and RHSS technology were applied in the jet fuel hydroprocessing plants of Shanghai Petrochemical Company and Zhenhai Refinery etc. RSS-1A catalyst is mainly used in the hydrorefining process of straight-run aviation kerosene, also it can be used in olefin saturating of reformate raffinate aiming at solvent oil.

Lube Hydrorefining Catalyst

RL-1

Lubricant hydrogenation RL-1 catalyst has excellent balance between hydrogenation function and acid cracking function, and it has the function to improve viscosity-temperature performance of lubricant fraction effectively and increase its viscosity index. The catalyst has high aromatics saturating activity, high de-sulfur and de-nitrogen activity and certain isomerization ability. The catalyst has good activity stability, and its integral performance has reached current international level. RL-1, a trilobe-shape strip catalyst, takes Ni-W as its active component. It has wide adaptability to lubricant fractions from various feedstock. Experiment result reveals that RL-1 has good effect in hydrogenation of lubricant fraction under both high and moderate pressure. RL-1 catalyst has been industrially applied in Kelamayi Petrochemical Plant and Sinopec Jingmen Branch. From lubricant fraction of different feed, API, AP II, or AP III base oil, 120~150BS bright oil, rubber filling oil and white oil etc. can be produced.

It is applicable for hydrogenation process under both high and moderate pressure, top grade lube base oil can be produced from lubricant fraction of different feed.

Lubricant Hydro-dewaxing Catalyst

RDW-1

RDW-1 lubricant hydro-dewaxing catalyst is a high-performance catalyst developed by RIPP and produced by Sinopec Catalyst Changling Division. This catalyst is a selective cracking catalyst with shape selective molecular sieve as its main component, and is applied in hydro-dewaxing of lubricant oil. It can crack high solidifying point hydrocarbon into little molecular ones and separate them from oil, so as to decrease solidifying point. RDW-1, a trilobe-shape strip catalyst, adopts shape selective molecular sieve with high crystallization degree, complex co-extruding agent developed by RIPP, as well as particular preparation technology, which make cracking activity of catalyst be adjusted elaborately. RDW-1 catalyst has the characters of high activity, high strength, long hydrogen activating period. Compared with reference catalysts, RDW-1 catalyst can be used under higher space velocity. Industrial result reveals that RDW-1 has good stability and good regeneration performance. RDW-1 catalyst has been industrially applied in Kelamayi Petrochemical Company, 32# and 46# refrigerating machine oil, 45# transformer oil, rubber filling oil and 150BS bright oil can be produced from Kelamayi section-9 thick oil.

It is applicable for hydro-dewaxing of diesel and lube fraction.Paraffin Hydrorefining Catalyst

RJW Series

RJW-1 is a trilobe-shape strip catalyst with Ni-W as its active component. It is suitable for hydrorefining of paraffin. RJW-1 paraffin hydro-refining catalyst is of high hydrogenation and aromatics saturating activity, weak cracking ability, proper pore structure, small diffusion resistance, favorable for distribution of gas and liquid in reactor. In 1992, RJW-1 paraffin hydro-refining catalyst was applied on the 100,000 t/a paraffin hydro-refining plant of Jingmen Petrochemical Company.

RJW-2 is jointly developed by RIPP and Sinopec Jingmen Branch, it is a trilobe-shape strip catalyst with Ni-W as active component and suitable for hydrorefining of micro-crystalline paraffin. In 1994, it realized industrial production in Changling Division, and was applied on the 50,000 t/a paraffin hydro-refining plant of Jingmen Petrochemical Company in May 1995.

It is applicable for hydrorefining of diversified paraffin and micro-crystalline paraffin aiming at food grade product, also suitable for hydrorefining of lube to improve the invariability of base oil.

Diene Selective Hydroprocessing Catalyst

RDD-1

Considering the process and feedstock condition of PetroChina Liaoyang Company, RDD-1 catalyst is a diene-selective hydrogenation catalyst developed by RIPP and produced by Changling Division, with non-precious metal Ni as its active component. Industrial application result reveals that its activity and stability is superior to imported products. Fast activity-losing problem of Ni based catalyst is solved. It has been under steady operation for more than one and a half years on Liaoyang Synthetic Fiber Companys 70,000 t/a pyrolytic gasoline hydrogenation plant with maleic anhydride value in first-section product steadily under 10 mg/g.

Selective hydroprocessing technology (including its catalyst) can be applied not only in the refining of steam pyrolytic gasoline, but also in the refining of other chemical feedstock widely, for example, the refining of catalytic pyrolytic gasoline feedstock aiming at low-carbon olefin, the refining of high octane number component feedstock aiming at aether such as MTBE, TAME etc., getting rid of diene from feedstock as the above so as to protect the catalysts in the downstream process and prolong the catalysts lives.

White Oil Hydroprocessing Catalyst

RLF-10WRLF-10 W is a kind of precious metal catalyst used in hydrogenation of white oil. It has excellent hydrogenation and aromatics saturating performance, weak cracking performance, small diffusion resistance, proper shape and strength. RLF-10 W is mainly used in section-2 hydrogenation in white oil production with two-section hydrogenation technology. It is also used in process that has high demand for aromatic saturating performance.

It is applicable for producing food grade white oil of diversified viscosity grade.

Hydrocracking Catalyst

RT Series

Main components of trilobe-shape strip RT-1 catalyst are Ni, W, and Y molecular sieve. RT-1 catalyst has certain hydro-desulphurization, hydro-denitrogenation and aromatics saturating ability with good cracking selectivity and anti-nitrogen stability. It has been successfully applied on industrial plants.

RT-1 catalyst can also be used in middle-pressure hydrocracking technology of heavy vacuum gas oil (RMC).

Main components of trilobe-shape strip RT-5 moderate-pressure hydrocracking catalyst are W, Ni, and Y molecular sieve.

RT-5 catalyst has very strong hydrocracking activity and good anti-nitrogen stability with certain hydro-desulphurization, hydro-denitrogenation and aromatics saturating ability. It has been successfully applied in many domestic hydrocracking plants. Moderate-pressure hydrogenation upgrading technology combining RN-1 hydrorefining catalyst and RT-5 hydrocracking catalyst is regarded as one of the three great updated technologies in the world for producing diesel oil with low sulfur and aromatics content by American Oil & Gas magazine.

RT-5 catalyst can also be used in moderate-pressure hydrocracking technology of heavy vacuum gas oil (RMC).

RT-5 can be used in moderate-pressure hydrocracking technology of heavy vacuum gas oil (RMC), also it can be used in high-pressure hydrocracking process.

RHC-1

RHC-1 catalyst was developed by RIPP with characters of high hydrogenation activity and high selective ring-opening performance. It can decrease BMCI of product tail oil, and is especially suitable for the production of top grade chemical feedstock under moderate pressure condition (trim pyrolysis feedstock of low BMCI and reforming feedstock with high latent aromatics), and hydrocracking process of top grade transportation fuel with ultra-low sulfur content. RHC-1 catalyst was applied in the 1.3 million ton/a hydrocracking plant of Sinopec Yanshan Branch. The result revealed BMCI of tail oil decreased by about two units, which increased ethylene yield of downstream steamed cracking ethylene process.

Residue Hydro-demetallization Catalyst

RDM Series

RDM-1/RDM-2 are butterfly shape residue hydro-demetallization catalyst with Ni-Mo/Alumina as its components.

RDM-1/RDM-2 has larger pore volume and size with higher hydro-demetallization (Ni, V) activity and excellent active stability and certain de-sulfur and de-carbon residue ability at the same time. They can tolerate metal more than 80% weight of themselves. These catalysts have already been applied in industrial plants successfully.

They are applicable for residue hydrotreating (RHT) process filled behind guard catalyst. The main function is to remove Ni and V from residue and protect downstream catalysts. Residue Hydrodemetallization & Hydrodesuphurization Catalyst

RMS-1

RMS-1 is a butterfly shape residue hydro-demetallization and desulphurization catalyst with Co-Mo/Alumina as components.

RMS-1 has larger pore volume, proper pore size and concentrated pore distribution, proper acidity and density etc, with excellent hydro-desulphurization activity, hydro-demetallization (Ni, V) activity, higher metal containing ability, higher de-nitrogenation and de-carbon residue ability at the same time. The catalyst has already been applied in industrial plants successfully (running period reached eight months).

It is applicable in residue hydrotreating (RHT) process filled behind demetallization catalyst. The main function is to remove sulfur, metal, carbon residue and nitrogen from residue. Residue Hydro-demetallization and Hydrodenitrogenation Catalyst

RSN-1

RSN-1 is a butterfly shape residue hydro-demetallization and denitrogenation catalyst with Ni-W/Alumina as components.

RSN-1 has proper pore volume and concentrated pore distribution, proper acidity and density, and contain certain quality of B-acid etc, with excellent hydro-denitrogenation, de-carbon residue, and de-sulphurization activity. The catalyst has already been applied in industrial plants successfully (running period reached eight months).

It is applicable in residue hydrotreating (RHT) process filled behind demetallization and desulfurization catalyst. The main function is to remove nitrogen, carbon residue and sulfur from residue. Reforming Prehydroprocessing Catalyst

RS Series

RS-1 is a kind of high-activity hydrorefining catalyst for naphtha under high space velocity. Due to its good hydrogenation performance, high activity in sulfur and nitrogen removal and low aromatic hydrocarbon saturating activity, RS-1 is especially adaptable for pre-hydrogenation of reforming feedstock under high space velocity. RS-1 is a trilobe strip shape catalyst based on Ni-W system and mixed with other additives with unique composition structure. In industrial installation under high space velocity, this catalyst shows high hydro-desulfurization activity, good activity stability and high mechanical strength.

With RS-1, straight-run gasoline can be processed to produce reforming feedstock under condition of 8~10 h-1 high space velocity and low hydrogen/oil ratio; naphtha with 25% coking gasoline content can be processed to produce reforming feedstock under condition of 4~6 h-1 high space velocity. Under the pressure (2.0 MPa) of reforming pre-hydrogenation, hydrogenation of diversified feedstock from inside and outside of China like high-sulfur content feedstock from Middle East, and pre-hydrogenation of nitrogenous feedstock (N=+30+30

easy charring matter passpass

coefficient of refraction , nD201.4701.4851.4701.485

UV absorbance /cm(260420nm) =2.5% point, >= 230255240260

density ( 20 ) , kg/m3859880860880

Packing : 200L in metal pail or tanker

Note :1 . The standard is following the SH0164.2 . Store in cool, well-ventilated place, away from moisture and impurity.Injection white oil ( light white oil )

Outline of product :It is made from petroleum. It used in vaccine injections for animals.

Main index ( standard : China animal remedy standard 2001 )

Relative density0.8180.880

Kinematic viscosity ( 40 ), mm2/s1113

Acidityneutrality

Heavy metal , ppm