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- Acetylacetone peroxide
- Benzoyl peroxide (BPO)
- Cumene Hydroperoxide (CHP)
- Cumyl peroxyneodecanoate
- Cyclohexanone peroxide
- Di(2,4-dichlorobenzoyl) peroxide
- Dibutyl peroxydicarbonate
- Dicumyl peroxide (DCP)
- Dihexadecyl peroxydicarbonate
- Diisobutyryl peroxide
- Diisopropyl peroxydicarbonate (BIPB)
- Diisopropylbenzene hydroperoxide
- Dilauroyl Peroxide (DLP)
- Di-tert-butyl peroxide (DTBP)
- Ditetradecyl peroxydicarbonate
- Methyl Ethyl Ketone Peroxide (MEKP)
- Methyl isobutyl ketone peroxide
- Pivalate Peroxypivalate
- Tert-Butyl Cumene Peroxide
- Tert-Butyl Perbenzoate (TBPB)
- Tert-Butyl Peroxy-2-Ethylhexanoate (TBPEH or TBEC)
- Tert-Butyl Peroxyacetate (TBPA)
- Tert-Butyl Peroxyisobutyrate
- Tert-Butyl Peroxypivalate (TBPPI)
- Tert-Butylperoxy-3,5,5-trimethylhexanoate (TBPIN)
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- Aromatics Production Catalyst
- Toluene Production Catalyst
- Methanol Synthesis Catalyst
- Formaldehyde & DME Synthesis
- Propylene Oxide Catalyst
- Ethylene Oxide Catalyst
- Sulfuric Acid Catalyst
- Ammonia Synthesis Catalyst
- Polyethylene Catalyst
- Polypropylene Catalyst
- Isomerization Catalyst
- Hydrogenation/Dehydrogenation
- Reforming
- Alkylation
- Tail Gas Treating Catalyst
- PET/PTA Catalyst
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Products
Products
Products
Hydrocracking Catalyst
- Product Description
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- Commodity name: Hydrocracking Catalyst
FC-50/FC-60/FC-66/FC-80/FC-32/FC-46/FC-76/FC-86/FC-24/FC-52/FC-82/FC-24B/FC-70A/FC-70B/FC-90/RHC-210/RHC-210F/RHC-5/RHC-3/RHC-220
FC Series Middle Distillate Hydrocracking Catalyst
Application
FC-50/FC-60/FC-66/FC-80
Hydrocracking unit, Hydro-upgrading unit
Description
The catalyst with W-Ni or Mo-Ni has high activity, selectivity of middle distillate oil and good stability. It is applicable to fixed-bed hydrocracking and hydro-upgrading processes for medium and high pressure processes of VGO and diesel distillates. It can maximize the middle distillates yield. Thanks to the high adaptability of feedstock, it can maximize the production of clean diesel and high-quality jet fuels that are difficult to be obtained by secondary processing methods from heavy distillates with high sulfur and high nitrogen content. When the tail oil full recycle operation is adopted, the middle distillate yield is more than 75%, of which the jet fuel yield is not less than 45%.
FC Series Flexible Distillate Hydrocracking Catalyst
Application
FC-32/FC-46/FC-76/FC-86
Hydrocracking unit, hydro-upgrading unit
Description
With modified molecular sieves as the main cracking component, it is suitable for medium or high pressure one-stage and two-stage processes, it can flexibly produce naphtha, jet fuel and diesel. When using a once-through process, the yield of chemical raw materials (light and heavy naphtha + cracked UCO) is more than 85%. When the full recycle operation of hydrocracking UCO is adopted, the yield can reach 60%-65% with middle distillate scheme. With chemical raw material scheme, the total yield of target products can reach 60%-65%.
FC Series Light Distillate Hydrocracking Catalyst
Application
FC-24/FC-52/FC-82
Hydrocracking unit
Description
With low active metal content and modified Y-type molecular sieve as main HC activity components, the catalyst features in strong hydrocracking activity, excellent selectivity to heavy naphtha, excellent nitrogen resistance, excellent hydrogenation performance, low hydrogen consumption and excellent applicability to feedstock. Suitable for medium or high pressure one stage and two-stage processes, it can maximize the yield of chemical raw materials. By tail oil full recycle operation, heavy naphtha yield is more than 70%, which can meet the demand for high-quality catalytic reforming raw materials to the greatest extent.
FC Series Hydro-Upgrading Catalyst
Application
FC-24B/FC-70A/FC-70B/FC-90
Hydrocracking unit
Description
With low active metal content and modified Y-type molecular sieve as main HC activity components, the catalyst is suitable for inferior diesel hydro-upgrading reaction. The inferior catalytic diesel can be selectively hydrogenated and ring-opened to produce high octane
gasoline components with high added value or raw materials with high aromatics potential, while the by-product is clean diesel blending components. It is suitable for the hydro-upgrading process for inferior FCC diesel under medium pressure or high pressure conditions to produce high octane gasoline. With strong hydrocracking activity and comparatively weak hydrotreating activity, the gasoline yield is about 35-55%, gasoline octane number is not less than 90. diesel cetane number can be increased 10-30 units.
RHC Chemical Feedstock Oil Hydrocracking Catalyst Series
Application
RHC-210/RHC-210F/RHC-5
Hydrocracking unit, hydro-upgrading units
Description
They are suitable for medium or high pressure operation with one-stage and two-stage process, which can maximize chemical feedstock production. RHC-210 can produce high quality heavy naphtha with stable high selectivity in long-term operation. By-products are high quality jet fuel and tail oil, the latter is a high quality feed for cracking unit. RHC-210F can produce more heavy naphtha and jet fuel with lower H2 consumption. RHC-5 has obvious temperature raising effect, even blended with poor quality feeds such as CGO, high density catalytic diesel, etc.
The single operation cycle of the series can reach 5 years. The commercial case is more than 8 units.
RHC Flexible Hydrocracking Catalyst Series
Application
RHC-3/RHC-220
Hydrocracking unit
Description
The catalyst is suitable for medium or high pressure one-stage and two-stage process hydrocrackers to produce low sulfur and low aromatic diesel and high quality chemical and lubricant feedstock. The RHC-3 application can be flexibly switched among high yield of heavy naphtha, middle distillate and high quality tail oil. It has high selectivity of converting aromatics and cycloalkanes to light fraction from the heavy or inferior feedstock, which enables the production of tail oil with low BMCI leading to more ethylene or propylene for the downstream cracking units. RHC-220 has better product quality than RHC-3. the BMCI of tail oil decreases by 1.0-3.0 unit. The cetane number can reach more than 70 and the PAH is less than 1.0% when diesel is the target product. It can be loaded at the top bed to maximize the yield of middle distillates or at the bottom bed to gain high-quality chemical feedstock and jet fuel. The single operation cycle of the series can reach 5 years. The commercial cases are more than 15 units.
Keywords: Hydrocracking Catalyst
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