Catalyst portfolio

Ammonia synthesis

KM1
Ammonia synthesis 
Shape:
  Irregular grains
Composition:
  Fe oxides
Range:
  340-550ºC/640-1020ºF

Description:

Excellent long-term stability
KM1R
Ammonia synthesis 
Shape:
  Irregular grains
Composition:
  Fe/FeO
Range:
  340-550ºC/640-1020ºF

Description:

Prereduced, excellent long-term stability

Feed purification

HTG-1
Chlorine absorption 
Shape:
  Ring
Composition:
  K2CO3
Range:
  Ambient to 400ºC/750ºF

Description:

HTZ-3
Sulphur absorption 
Shape:
  Extrudate
Composition:
  ZnO
Range:
  Ambient to 450ºC/840ºF

Description:

High sulphur content feedstock
HTZ-4
Sulphur absorption 
Shape:
  Extrudate
Composition:
  ZnO/Al2O3
Range:
  Ambient to 450ºC/840ºF

Description:

COS absorption
HTZ-5
Sulphur absorption 
Shape:
  Extrudate
Composition:
  ZnO
Range:
  Ambient to 450ºC/840ºF

Description:

Low sulphur content feedstock
HTZ-51
Sulphur absorption 
Shape:
  Extrudate
Composition:
  ZnO
Range:
  Ambient to 450ºC/840ºF

Description:

Low sulphur content feedstock
ST-101
Final purification 
Shape:
  Cylinder
Composition:
  Cu
Range:
  Ambient to 370ºC/700ºF

Description:

Trace sulphur removal
ST-201
Final purification 
Shape:
  Cylinder
Composition:
  Cu
Range:
  Ambient to 370ºC/700ºF

Description:

Trace sulphur removal
TK-250
Hydrogenation 
Shape:
  Ring
Composition:
  CoMo
Range:
  300-450ºC/570-840ºF

Description:

TK-261
Hydrogenation 
Shape:
  Extrudate
Composition:
  NiMo
Range:
  300-450ºC/570-840ºF

Description:

Automotive

DNX
SCR catalyst for diesel engines in standard Euro 4/5 like applications 
Shape:
 
Diameters 5,66"-12,7"
Length 6"-16"
Composition:
  V2O5/WO3/TiO2
Range:
  200-550ºC/390-1020ºF

Description:

Low weight, low pressure drop, flexible diameter and including sleeving. One supplier for all the components for a ready-to-mount catalyst.
DNXZ
SCR catalyst for diesel engines in high temperature applications, e.g. in combination with oxidation catalyst and soot filter. 
Shape:
 
Diameters 5,66"-12,7"
Length 6"-16"
Composition:
  Zeolite based
Range:
  200-750ºC/390-1382ºF

Description:

Low weight, low pressure drop, flexible diameter and including sleeving. One supplier for all the components for a ready-to-mount catalyst.
HTDOC
Oxidation catalyst for combined systems for diesel engines 
Shape:
 
Diameters 5,66"-12;7"
Length 6"-16"
Composition:
  Pt/TiO2-based
Range:
  150-750ºC/390-1382ºF

Description:

Low weight, low pressure drop, flexible diameter and including sleeving. One supplier for all the components for a ready-to-mount catalyst.
DOXCAT
Oxidation catalyst for diesel engines with high sulphur fuel 
Shape:
 
Diameters 5,66"-12,7"
Length 6"-16"
Composition:
  Pd/TiO2-based
Range:
  150-550ºC/210-1020ºF

Description:

Low weight, low pressure drop, flexible diameter and including sleeving. One supplier for all the components for a ready-to-mount catalyst.
BMC-211
DFP filter coat 
Shape:
  Coat applicable on all available DFP filters
Composition:
  Pd/MeO-based
Range:
  100-1000ºC/210-1832ºF

Description:

Low T50 for HC and CO, NO2 reducing ability and a low cost alternative

CO conversion

SK-201-2
High temperature shift 
Shape:
  Cylinder
Composition:
  Fe/Cr/Cu
Range:
  325-500ºC/620-930ºF

Description:

High temperature shift
LK-813
Medium temperature shift 
Shape:
  Cylinder
Composition:
  Cu/Zn/Al
Range:
  200-330ºC/390-625ºF

Description:

Medium temperature shift
LK-817
Medium temperature shift 
Shape:
  Cylinder
Composition:
  Cu/Zn/Al
Range:
  200-330ºC/390-625ºF

Description:

Medium temperature shift
LK-821-2
Low temperature shift 
Shape:
  Cylinder
Composition:
  Cu/Zn/Al
Range:
  185-275ºC/365-530ºF

Description:

Low temperature shift
LK-823
Low temperature shift 
Shape:
  Cylinder
Composition:
  Cu/Zn/Al/Cs
Range:
  185-275ºC/365.530ºF

Description:

Low MeOH formation. Reduces MeOH formation with a factor 8 compared to LK-821-2.
LSK-2
Chlorine guard 
Shape:
  Cylinder
Composition:
  Cu/Zn/Al
Range:
  185-275ºC/365-530ºF

Description:

Chlorine guard for LTS service
TK-20
Topping material 
Shape:
  7-hole cylinder
Composition:
  Inert
Range:
  185-500ºC/365-930ºF

Description:

High void topping material for all shift converters

Oxidation catalysts

CK-302
VOC abatement 
Shape:
  3-5 mm balls
Composition:
  CuMn
Range:
  200-600ºC/390-1110ºF

Description:

Most applications, silicon resistant
CK-304
VOC abatement 
Shape:
  3-5 mm balls
Composition:
  Pd
Range:
  200-600ºC/390-1110ºF

Description:

CO, alkans, aromates
CK-305
VOC abatement 
Shape:
  3-5 mm balls
Composition:
  Cr
Range:
  200-550ºC/390-1020ºF

Description:

Halogenated, hydrocarbons, halogen resistant
CK-306
VOC abatement 
Shape:
  3-5 mm balls
Composition:
  CrPd
Range:
  200-550ºC/390-1020ºF

Description:

CO, halogenated hydrocarbons, halogen resistant
CK-307
VOC abatement 
Shape:
  3-5 mm balls
Composition:
  Pt
Range:
  200-525ºC/390-970ºF

Description:

Most applications, sulphur resistant
CK-322
VOC abatement 
Shape:
  4.8/2.8 x 5-10 mm rings
Composition:
  CuMn
Range:
 

200-600ºC/390-1110ºF

Description:

Most applications, silicon resistant

CK-395
VOC abatement 
Shape:
  3-5 mm balls
Composition:
  Mn
Range:
  200-600ºC/390-1110ºF

Description:

Halogenated hydrocarbons, halogen resistant
CK-428
VOC abatement 
Shape:
  10/4x10 mm rings
Composition:
  CuMnPt
Range:
  200-525ºC/390-970ºF

Description:

H2S, COS, CS2, ammonia, sulphur resistant
DNO
CO abatement 
Shape:
  corrugated monoliths
Composition:
  V2O5/WO3/TiO2/precious metal
Range:
  200-450ºC/390-840ºF

Description:

CO, ammonia

DME

DMK-10
DME synthesis 
Shape:
  Extrudate
Composition:
  Activated alumina
Range:
  250-400ºC/480-750ºF

Description:

Feedstock and product flexibility

DeNOx

DNX-HD
For high-dust DeNOx units, typically on coal-fired boilers 
Composition:
  V2O5/WO3/TiO2

Description:

Channel sizes: 6.4-9 mm (5-10 CPSI). Available with 0.8 mm and 1.0 mm wall thickness.
The DNX-HD types are custom formulated with nine different vanadium levels to balance DeNOx activity and SO2 oxidation rate to a specified level.
DNX-MD
For DeNOx units with medium-range dust load e.g. boilers firing low-ash coal, FCC units in refineries and stationary diesel engines 
Composition:
  V2O5/WO3/TiO2

Description:

Channel sizes: 4.5-5.6 mm (13-17 CPSI). Available with 0.8 mm and 1.0 mm wall thickness.
The DNX-MD types are custom formulated with nine different vanadium levels to balance DeNOx activity and SO2 oxidation rate to a specified level.
DNX-LD
For low-dust DeNOx units e.g. oil-fired boilers, chemical process units and waste incinerators 
Composition:
  V2O5/WO3/TiO2

Description:

Channel sizes: 3.4-5.1 mm (19-39 CPSI). Wall thickness: 0.4 mm.
The DNX-LD catalyst types are custom formulated with different vanadium levels to balance DeNOx activity and SO2 oxidation rate to a specified level.
DNX-ND
For operation in dust-free gases, e.g. from gas turbines and gas engines 
Composition:
  V2O5/WO3/TiO2

Description:

Channel sizes: 2.7 mm (60 CPSI). Wall thickness: 0.4 mm
The DNX-ND catalyst type is available with different vanadium levels to adapt the catalyst to specific operating temperatures up to 550ºC (1020ºF).
DNX-029HT
For high-temperature operation in dust-free gases, e.g. from gas turbines and gas engines 
Composition:
  Non-vanadium type on a TiO2 carrier.

Description:

Channel sizes: 2.7 mm (60 CPSI). Wall thickness: 0.4 mm
The DNX-029HT catalyst is a unique, non-vanadium catalyst type for operation at very high temperatures up to 600°C/1100°F.

Methanation

PK-7R
Methanation 
Shape:
  Ring
Composition:
  Ni
Range:
  190-450ºC/375-840ºF

Description:

Prereduced

Methanol

MK-121
Methanol synthesis 
Shape:
  Cylinder
Composition:
  Cu/Zn/Al
Range:
  200-310ºC/390-590ºF

Description:

All-round catalyst suited for all types of methanol reactors. High activity, selectivity and long-term stability.

Refining

Grading and demet

TK-10
Pressure drop and contamination control 
Shape:
  7 hole cylinder
Composition:
  Inert

Description:

TK-10 is an inert hold-down catalyst applicable as topping layer in catalytic reactors instead of spherical material. It is shape-optimised and provides a high void fraction, and it is an important part of grading in composite catalyst fillings.

 

TK-15
Pressure drop and contamination control 
Shape:
  Butterfly-shaped
Composition:
  Inert

Description:

TK-15 is a shape-optimised, high-void fraction catalyst used for topping off catalytic reactors instead of spherical material. It is specifically designed for units experiencing high gas rates or carry-over of coke spalled from the heater or heat exchange train.
TK-25 TopTrap™
Pressure drop and contamination control 
Shape:
  Quadralobe ring
Composition:
  Inert

Description:

TK-25 TopTrap™ is an inert macroporous catalyst designed to pick up iron scale and other contaminants. It is shape-optimised as a quadralobe with a central hole, which provides a high void fraction.
TK-30
Pressure drop and contamination control 
Shape:
  Extrudate or ring
Composition:
  Inert

Description:

TK-30 is a high purity alumina catalyst shaped as rings or extrudates. As a separate layer, it functions as void grading material in catalytic reactors, but it can also be used as diluent for controlling catalyst activity in any hydroprocessing application.
TK-31
Phosphorous removal 
Shape:
  Extrudate
Composition:
  Proprietary

Description:

TK-31 is a high-activity catalyst that offers capacity for trapping phosphorous compounds present in the feed such as corrosion inhibitors.
TK-45
Arsenic guard 
Shape:
  Ring
Composition:
  Ni

Description:

TK-45 is a high-nickel catalyst based on an alumina carrier. It is ring-shaped and can be applied as an integrated part of grading systems, and it has been developed for use in catalyst bed grading systems, where arsenic pick-up is desired.
TK-47
Arsenic guard 
Shape:
  Extrudate
Composition:
  Ni

Description:

TK-47 is a high-nickel catalyst based on an alumina carrier. It is available in a quadralobe shape, and it has been developed for use in catalyst bed grading systems, where arsenic pick-up is desired.
TK-437
Coker naphtha hydrotreating 
Shape:
  Extrudate or ring
Composition:
  NiMo

Description:

TK-437 is a NiMo catalyst with some HDS and HDN activity, and it functions as silica guard for coker naphtha hydrotreating. Delayed coker naphtha fractions often contain high amounts of silica, and TK-437 exhibits a high surface area and low metals content, which maximise silica pick-up.
TK-453
VGO hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-453 is a NiMo catalyst with very high rates for removal of metals (Ni, V, Fe) and silicon, and it is an excellent guard in hydrotreaters that process heavy feeds. It exhibits moderate HDS and HDN activities, and the pore size distribution and pore volume have been optimised, resulting in a high capacity for accumulation of nickel, vanadium and silicon.
TK-550
Pressure drop and contamination control 
Shape:
  Ring
Composition:
  CoMo

Description:

TK-550 is a CoMo catalyst with medium HDS activity for both straight-run and cracked light distillate processing. It can be a cost-efficient alternative when processing heavier feedstocks in mild services. In ring shape, it is used as graded bed material.
TK-709
Pressure drop and contamination control 
Shape:
  Ring
Composition:
  Mo

Description:

TK-709 is a high-surface area, low-activity Mo catalyst with high HDM activity and metal storage capacity. It is typically used in various grading applications for all types of feeds, particularly where iron is encountered, and it is especially suitable for olefin containing feeds, where activity grading is needed to prevent formation of gum.
TK-710
Pressure drop control 
Shape:
  Ring
Composition:
  CoMo

Description:

TK-710 is a CoMo type catalyst with moderate HDS activity, limited loss of octane, high HDM activity and metal storage capacity. It is applied in FCC post-treatment and various grading applications.
TK-711
Pressure drop and contamination control 
Shape:
  Ring
Composition:
  NiMo

Description:

TK-711 is a NiMo catalyst with high HDM activity, metal storage capacity and moderate HDS activity. It is used in various grading applications for all types of feeds.
TK-743
Pressure drop and contamination control 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-743 is a demetallisation catalyst with moderate HDS activity for fixed-bed resid service and VGO hydrotreating. It is typically used for reduction of metals, asphaltenes and Conradson Carbon as a first-stage catalyst in composite catalyst fillings. The optimised pore system and high pore volume allow enhanced metal pick-up while maintaining activity.
TK-745
Pressure drop and contamination control 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-745 is a high porosity demetallisation catalyst for de-asphalted oil and heavy VGO containing resid. As such, TK-745 is applied in the front-end of fixed-bed VGO/resid hydrotreaters due to its enhanced ability to remove metals.
TK-831
Pressure drop and contamination control 
Shape:
  Ring
Composition:
  NiMo

Description:

TK-831 is a NiMo catalyst with high HDM activity, metal storage capacity and moderate HDS and HDN activity. It is used in various grading applications for all types of feeds.
 

Claus tail gas treating

TK-220
Tail gas treating 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-220 is a CoMo catalyst that is specifically developed for treating tail gases derived from Claus or other similar units.
TK-222
Tail gas treating 
Shape:
  Ring
Composition:
  CoMo

Description:

TK-222 is a CoMo catalyst specifically developed for treating tail gases derived from Claus or other similar units. It is of particular interest where catalyst bed pressure drop is limiting, since its ring shape exhibits lower pressure drop compared to other catalysts of same particle size.
TK-224
Tail gas treating 
Shape:
  Sphere
Composition:
  CoMo

Description:

TK-224 is a CoMo catalyst that is specifically developed for treating tail gases derived from Claus or other similar units.
 

Renewable fuels

TK-335
Diesel and biofuel hydrotreating 
Shape:
  Ring
Composition:
  Proprietary

Description:

TK-335 is developed for fixed-bed HDO service and is typically applied as top grading in diesel hydrotreating units, processing mixtures of atmospheric gas oils and phosphorous-containing biofuels. It is characterised by high HDO activity and relatively low activities of HDS, HDN and saturation, which help dissipate exotherms and reduce pressure drop build-up.
TK-339
Diesel and biofuel hydrotreating 
Shape:
  Extrudate
Composition:
  Proprietary

Description:

TK-339 is developed for fixed-bed HDO service and is typically applied as top grading in diesel hydrotreating units, processing mixtures of atmospheric gas oils and biofuels. It is characterised by high HDO activity and relatively low activities of HDS, HDN and saturation, which help dissipate exotherms and reduce pressure drop build-up.
TK-341
Diesel and biofuel hydrotreating 
Shape:
  Extrudate
Composition:
  Proprietary

Description:

TK-341 is developed for fixed-bed HDO service and is typically applied as second-stage catalyst in diesel hydrotreating units, processing mixtures of atmospheric gas oils and biofuels. It is characterised by high HDO activity and moderate activities of HDS, HDN and saturation, which help dissipate exotherms and reduce pressure drop build-up.
TK-351
Diesel and biofuel hydrotreating 
Shape:
  Extrudate
Composition:
  Proprietary

Description:

TK-351 is developed for fixed-bed HDO service and is typically applied as bulk catalyst in hydrotreating units, processing mixtures of atmospheric gas oils and nitrogen-containing biofuels. It is characterised by high HDO activity and high activities of HDN, HDS and saturation and is often applied in combination with dewaxing catalysts.
TK-928
Dewaxing 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-928 is specifically designed for cold flow improvement (dewaxing) of diesel, biodiesel and waxy feeds such as Fischer-Tropsch products.
TK-932
Dewaxing 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-932 is specifically designed for cold flow improvement (dewaxing) of nitrogen-containing diesel, biodiesel and waxy feeds.
 

Coker naphtha

TK-431
Coker naphtha hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-431 is a NiMo catalyst with medium HDS and HDN activity especially made for coker naphtha hydrotreating. Delayed coker naphtha fractions usually contain high amounts of silica, and TK-431 is optimised for silica pick-up while maintaining HDS and HDN.
TK-437
Coker naphtha hydrotreating 
Shape:
  Extrudate or ring
Composition:
  NiMo

Description:

TK-437 is a NiMo catalyst with some HDS and HDN activity, and it functions as silica guard for coker naphtha hydrotreating. Delayed coker naphtha fractions often contain high amounts of silica, and TK-437 gives higher silica pick-up with same HDS and HDN activity.
TK-439
Coker naphtha hydrotreating 
Shape:
  Extrudate
Composition:
  Inert

Description:

TK-439 is especially formulated for coker naphtha hydrotreating. Delayed coker naphtha fractions usually contain high amounts of silica, and TK-439 exhibits maximum silica pick-up.
 

Naphtha

TK-527
Naphtha hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-527 is a NiMo catalyst with medium HDS and HDN activity used for naphtha hydrotreating. It is suitable for HDS of all straight-run and cracked naphtha fractions.
TK-561 BRIM™
Naphtha hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-561 BRIM™ is a NiMo catalyst with high HDS and very high HDN activity in naphtha service. Therefore, it is the optimum choice for naphtha hydrotreaters processing nitrogen-rich feedstocks like FCC, visbreaker and coker fractions.
 

FCC post-treatment

TK-710
FCC post-treating 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-710 is a CoMo type catalyst with moderate HDS activity, limited loss of octane, high HDM activity and metal storage capacity. It is applied in FCC post-treatment and various grading applications.
 

Kerosene

TK-527
Kerosene hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-527 is a NiMo catalyst with medium HDS and HDN activity used for kerosene hydrotreating. It is suitable for HDS of all straight-run and cracked kerosene fractions.

TK-561 BRIM
Kerosene hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-561 BRIM™ is a NiMo catalyst with high HDS and very high HDN activity in kerosene service. Therefore, it is the optimum choice for kerosene hydrotreaters processing nitrogen-rich feedstocks like FCC, visbreaker and coker fractions.
TK-568 BRIM™
Kerosene hydrotreating 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-568 BRIM™ is a new generation BRIM™ catalyst specifically developed for ultra low sulphur diesel and kerosene applications. It provides high HDS activity and stability when processing both straight-run and cracked distillate fractions.
 

Diesel

TK-553
Diesel post-treating – colour removal 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-553 is a NiMo catalyst especially developed for colour removal (post-treatment) in ultra low sulphur diesel (ULSD) units operated at relatively high temperatures, where colour species may be formed.
TK-568 BRIM™
Ultra low sulphur diesel 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-568 BRIM™ is a new generation BRIM™ catalyst specifically developed for ultra low sulphur diesel and kerosene applications. It provides high HDS activity and stability when processing both straight-run and cracked distillate fractions.
TK-570 BRIM™
Ultra low sulphur diesel 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-570 BRIM™ is a new generation BRIM™ catalyst specifically developed for ultra low sulphur diesel applications. This catalyst provides high HDS activity and is suitable for both straight-run and cracked distillate fractions at low to medium pressure.
TK-576 BRIM™
Ultra low sulphur diesel 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-576 BRIM™ is the first generation BRIM™ catalyst with exceptionally high HDS activity specifically formulated for ultra low sulphur diesel production (less than 10 wt ppm sulphur). It is suitable for both straight-run and cracked distillate processing at low to medium pressure.
TK-578 BRIM™
Ultra low sulphur diesel 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-578 BRIM™ is a new generation BRIM™ catalyst which has significantly higher activity than the past generation of catalysts for ultra low sulphur diesel production (less than 10 wt ppm sulphur). It is suitable for processing of straight-run and cracked distillate fractions in units operating at low to medium pressure.
TK-607 BRIM™
Ultra low sulphur diesel 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-607 BRIM™ is the new generation, high-activity NiMo catalyst based on the BRIM™ Technology. It is the preferred choice for ULSD hydrotreating units, operating at medium to high pressure, and it is suitable for both straight-run and cracked distillate stocks.
TK-907
Dearomatisation 
Shape:
  Extrudate
Composition:
  Noble metal

Description:

TK-907 is an alumina-based noble metal catalyst specifically designed to make a low aromatic product from refinery feedstocks.
TK-911
Dearomatisation 
Shape:
  Extrudate
Composition:
  Noble metal

Description:

TK-911 is an enhanced-activity version of TK-907 specifically designed to make a low aromatic product from refinery feedstocks. It exhibits a greater tolerance to the inhibiting effect of sulphur and nitrogen.
TK-915
Dearomatisation 
Shape:
  Extrudate
Composition:
  Noble metal

Description:

TK-915 is the premium-activity HDA catalyst. It exhibits a greater tolerance to the inhibiting effect of sulphur and nitrogen.
TK-928
Dewaxing 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-928 is specifically designed for cold flow improvement (dewaxing) of diesel, biodiesel and waxy feeds such as Fischer-Tropsch products.
TK-932
Dewaxing 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-932 is specifically designed for cold flow improvement (dewaxing) of nitrogen-containing diesel, biodiesel and waxy feeds.
 

FCC pretreatment

TK-560 BRIM™
FCC pretreating 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-560 BRIM™ is specifically developed for FCC pretreatment applications, and it provides exceptional HDS and HDN activity along with aromatic saturation and some conversion into lighter products. The pore structure gives high catalyst stability when processing both straight-run and cracked VGO fractions.
TK-561 BRIM™
FCC pretreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-561 BRIM™ provides exceptionally high HDN and HDS activity along with aromatic saturation and some conversion into lighter products. The manufacturing process ensures high catalyst stability when processing both straight-run and cracked VGO fractions.
TK-562 BRIM™
FCC pretreating 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-562 BRIM™ is specifically developed for FCC pretreatment applications, and it provides the highest possible HDS and HDN activity along with aromatic saturation and some conversion into lighter products. The pore structure gives high catalyst stability when processing both straight-run and cracked VGO fractions.
 

Hydrocracker pretreatment

TK-561 BRIM™
Hydrocracking pretreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-561 BRIM™ provides exceptionally high HDN and HDS activity along with aromatic saturation and some conversion into lighter products. The manufacturing process ensures high catalyst stability when processing both straight-run and cracked VGO fractions.

TK-607 BRIM™
Hydrocracking pretreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-607 BRIM™ is the new generation, high-activity NiMo catalyst based on the BRIM™ Technology. It is optimised for use as a first stage catalyst in hydrocrackers, where maximum HDN of straight-run and cracked fractions in the VGO range are essential.
 

Hydrocracking

TK-925
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-925 is a hydrocracking catalyst optimised for maximum production of middle distillate products with very low aromatic content and excellent properties. It is also very suitable for mild hydrocracking applications, where high catalyst stability together with excellent product quality are required at low operating pressures.
TK-926
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-926 is a hydrocracking catalyst with excellent selectivity to diesel. It is optimised for maximum production of middle distillate products with good cold flow properties, and it is also very suitable for mild hydrocracking applications, where high stability and excellent cold flow properties of the products are required.
TK-931
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-931 is a hydrocracking catalyst with high selectivity to middle distillates, and it also enhances the quality of the products (high V.I. of UCO, high smoke point of jet, high C.I. of diesel).
TK-933
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-933 is a medium-activity hydrocracking catalyst used in services where very high middle distillate yield and very good cold flow properties are desired.
TK-941
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-941 has a high selectivity to middle distillates, and it can be used in applications where high cracking activity and high middle distillate yield are required and where high light ends yield is undesirable.
TK-943
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-943 is a medium to high-activity hydrocracking catalyst with excellent selectivity to diesel. It is optimised for maximum production of middle distillate products with good cold flow properties, and it is also very suitable for low conversion applications, where high stability and excellent cold flow properties of the products are required.
TK-947
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiMo

Description:

TK-947 is recommended for applications where high cracking activity and high middle distillate yield are required. Also, it is an excellent choice for MHC applications, where high product quality is required at moderate pressure and medium conversion.
TK-951
Hydrocracking 
Shape:
  Cylinder
Composition:
  NiW

Description:

TK-951 is a high activity hydrocracking catalyst which provides optimum diesel and naphtha yields while minimising overcracking. It has a strong hydrogenation function that improves the properties of the different product fractions.
 

Lube polishing

TK-561 BRIM™
Hydropolishing 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-561 BRIM™ provides high activity for hydrofinishing of lubes and waxes.
TK-562 BRIM™
Hydropolishing 
Shape:
  Extrudate
Composition:
  CoMo

Description:

TK-562 BRIM™ provides high activity for hydrofinishing of lubes and waxes.
 

Resid hydrotreating

TK-719
Resid hydrotreating 
Shape:
  Extrudate
Composition:
  Mo

Description:

TK-719 is a high-porosity demetallisation catalyst for fixed-bed resid service. It is applied in the front-end of resid hydrotreaters due to its enhanced ability to remove metals and asphaltenes and to reduce Conradson Carbon. Even though large particles usually result in lower HDM activity and a low metal storage capacity, the unique pore system of TK-719 enables this catalyst to maintain a high HDM activity and provide capacity for metal storage.
TK-743
Resid hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-743 is a demetallisation catalyst with moderate HDS activity for fixed-bed resid service and VGO hydrotreating. It is typically used for reduction of metals, asphaltenes and Conradson Carbon as a first-stage catalyst in composite catalyst fillings. The optimised pore system and high pore volume allow enhanced metal pick-up while maintaining activity.
TK-753
Resid hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-753 is a transition catalyst in fixed-bed resid HDS systems. In such applications, it would be preceded by a HDM-type catalyst and followed by a HDS-type catalyst (like TK-773). TK-753 exhibits good HDS activity and HDM selectivity, and the pore size distribution and pore volume have been optimised, resulting in a high capacity for uptake of nickel and vanadium and a low bulk density.
TK-773
Resid hydrotreating 
Shape:
  Extrudate
Composition:
  NiMo

Description:

TK-773 is a final-stage catalyst for fixed-bed resid HDS units. It has a high HDS, HDN and Conradson Carbon removal activity and, as such, has a low HDM selectivity. The pore size distribution and pore volume have been optimised, resulting in a better capacity for uptake of nickel and vanadium together with a low bulk density.
 

Steam reforming

RKNGR
Prereforming, naphtha 
Shape:
  Cylinder and 7-hole cylinder
Composition:
  Ni
Range:
  350-650ºC/660-1200ºF
            (typical range)

Description:

Prereduced. For prereforming of naphtha/heavy feedstocks.
AR-401
Prereforming 
Shape:
  Cylinder and 7-hole cylinder
Composition:
  Ni
Range:
  325-650ºC/620-1200ºF 
            (typical range)

Description:

Prereduced. For prereforming of feedstocks ranging from natural gas/refinery off-gas to LPG.
RK-202
Tubular reforming, naphtha 
Shape:
  7-hole cylinder
Composition:
  Ni/K
Range:
  350-750ºC/660-1830ºF 
            (typical range)

Description:

High alkali-promoted for steam reforming of naphtha feedstocks.
RK-212
Tubular reforming, naphtha 
Shape:
  7-hole cylinder
Composition:
  Ni/K
Range:
  350-750ºC/660-1830ºF 
            (typical range)

Description:

High alkali-promoted,prereduced for steam reforming of naphtha feedstocks.
R-67-7H
Tubular reforming, natural gas to LPG 
Shape:
  7-hole cylinder
Composition:
  Ni
Range:
  350-1000ºC/660-1830ºF 
            (typical range) 

Description:

Steam reforming of feedstocks ranging from natural gas to LPG.
R-67R-7H
Tubular reforming, natural gas to LPG 
Shape:
  7-hole cylinder
Composition:
  Ni
Range:
  350-1000ºC/660-1830ºF 
            (typical range) 

Description:

Prereduced. Steam reforming of feedstocks ranging from natural gas to LPG.
RK-201
Tubular reforming, natural gas to LPG 
Shape:
  7-hole cylinder
Composition:
  Ni/K
Range:
  350-1000ºC/660-1830ºF 
            (typical range)

Description:

Low alkali-promoted. Steam reforming of feedstocks ranging from natural gas to LPG.
RK-211
Tubular reforming, natural gas to LPG 
Shape:
  7-hole cylinder
Composition:
  Ni/k
Range:
  350-1000ºC/660-1830ºF 
            (typical range)

Description:

Low alkali-promoted, prereduced. Steam reforming of feedstocks ranging from natural gas to LPG.
RKS-2
Secondary and autothermal reforming 
Shape:
  Ring
Composition:
  Ni
Range:
  ≤1440ºC/≤2550ºF 
            (typical range)

Description:

Top layer in secondary and autothermal reforming reactors.
RKS-2-7H
Secondary and autothermal reforming 
Shape:
  7-hole-cylinder
Composition:
  Ni
Range:
  ≤1400ºC/≤2550ºF 
            (typical range) 

Description:

Secondary and autothermal reforming, bulk catalyst.
RKS-2P
Secondary and autothermal reforming 
Shape:
  Ring
Composition:
  Ni
Range:
  ≤1400ºC/≤2550ºF 
            (typical range)

Description:

Top layer in secondary and autothermal reforming reactors.

Sulphuric acid

VK-701 LEAP5™
High activity catalyst based on Topsøe’s new LEAP5™ technology optimised for operation in converted strong gasses. Enables new opportunities for reduction in SO2 emission from both single- and double-absorption plants. 
Shape:
  12 mm Daisy
Composition:
  V2O5/K/Na

Description:

Improved energy efficiency throughout the operating cycle due to low initial pressure drop.
VK38
All-round catalyst suited for all passes 
Shape:
 
12 mm Daisy
25 mm Daisy
6 mm cylinder
10 mm ring
Composition:
  V2O5/K/Na

Description:

12 mm Daisy improved energy efficiency throughout the operating cycle due to low initial pressure drop
25 mm Daisy dust protection catalyst with 100% longer on-stream time compared to the 12 mm Daisy in dusty feed gases
6 mm cylinder
and 10 mm ring
ensure an even gas distribution in applications with very low gas velocity converters
VK48
High vanadium catalyst with enchanced activity in the lower passes in high SO3 gas enviroment 
Shape:
 
12 mm Daisy
6 mm cylinder
Composition:
  V2O5/K/Na

Description:

12 mm Daisy improved energy efficiency throughout the operating cycle due to low initial pressure drop
6 mm cylinder
and 10 mm ring
ensure an even gas distribution in applications with low gas velocity converters


VK59
Caesium-promoted catalyst for accomodating strong SO2 feed gases, ignition layers and increased conversion single-absorption plants 
Shape:
  12 mm Daisy
Composition:
  V2O5/K/Na/Cs

Description:

Improved energy efficiency throughout the operating cycle due to low initial pressure drop
VK69
High-vanadium caesium-promoted catalyst for strongly reduced SO2 emission and/or increased production rate in double absorption plants 
Shape:
  9 mm Daisy
Composition:
  V2O5/K/Na/Cs

Description:

The high surface area of the 9 mm Daisy contributes to the high activity, and the high void fraction ensures a low pressure drop.

Wet gas sulphuric acid

VK-WSA
All-round catalyst optimised for operation in water-vapour containing process gases 
Shape:
 
12 mm Daisy
25 mm Daisy
Composition:
  V2O5/K/Na

Description:

12 mm Daisy: improved energy efficiency throughout the operating cycle due to low initial pressure drop
25 mm Daisy: dust protection catalyst with 100% longer on-stream time compared to the 12 mm Daisy in dusty feed gasses
VK-WSX
High activity catalyst for operation in the lower passes in highly converted water-vapour containing gases 
Shape:
  9 mm Daisy
Composition:
  V2O5/K/Na

Description:

The high surface area of the 9 mm Daisy contributes to the high activity, and the high void fraction ensures a low pressure drop.
VK-WH
Caesium-promoted catalyst for operation in high concentration gases (SO2 an SO3) containing water vapour 
Shape:
  12 mm Daisy
Composition:
  V2O5/K/Na/Cs

Description:

Improved energy efficiency throughout the operating cycle due to low initial pressure drop
VK-WL
Caesium-promoted catalyst for operation in low concentration gases (SO2 and SO3) containing water vapour 
Shape:
  9 mm Daisy
Composition:
  V2O5/K/Na/Cs

Description:

The high surface area of the 9 mm Daisy contributes to the high activity, and the high void fraction ensures a low pressure drop.