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Naphtha reforming catalysts

Naphtha reforming catalysts can be divided into semi-regenerative reforming and continuous regenerative reforming kind. Among them, continuous regenerative reforming has the advantages of high liquid yield, high product octane number, high hydrogen yield and long continuous operation period of the unit. , which is becoming the preferred process technology for new plants

Product introduction 

Catalytic reforming of naphtha is an important petroleum refining process. After naphtha is catalytically converted, the resulting reforming oil can be used as a blending component of low-sulfur, low-olefin content and high-octane gasoline, or as an aromatic hydrocarbon feedstock. , The production of benzene, toluene and xylene. The high-quality hydrogen by-product in the reforming process has the advantages of high purity and low cost, and is the most important source of hydrogen for the refinery hydrogenation unit.

Appropriate time of replacing naphtha reforming catalysts

① The time for changing the CCR catalyst is not static, there is no fixed running time or cycle

② It is meaningful to judge the time of changing the caltalyst through economic evaluation

③ Mastering the correct method to continuously regenerate the catalyst is the key to prolonging the service life of the catalyst

④ Changing it at the right time to maximize the device

⑤ Evaluate the necessity of changing it is  needed to carry out an economic analysis of the return on investment of the agent

⑥ Similar to other capital investment projects

⑦ Quantitative analysis of performance between new and existing catalysts

 


Product Basic Info

Several factors that lead to permanent naphtha reforming catalysts damage

① The catalyst support phase structure is destroyed

② Metal poisoning

Depletion of tin and even platinum can occur under extreme regeneration conditions of mishandling

Damaged catalysts cause many problems in reformers

① Low liquid yield of C5+, low yield of aromatics and hydrogen

② Chlorine holding capacity 1 catalyst activity is very poor

③ Equipment corrodes and requires frequent replacement of dechlorinating agents

④ High dust content and clogged filters

⑤ Sensitive to carbon deposits

A drop in normal specific surface area does not mean the catalyst is damaged


Product Specification

A

B

C

D

Index

Industrial Standard

High Activity

High Severity

High Yield

High Yield

ABD(g/cc)

0.56

0.68

0.58

0.68

Diameter(mm)

1.6

1.6

1.6

1.6

Shape

Sphere

Sphere

Sphere

Sphere

Surface Area(m2/g)

180

180

180

180

Average Crushing Strength(N)

50

75

50

75

Pt(Wt%)

0.29

0.25

0.29

0.25

Additive

No

No

Yes

Yes

 Catalyst Grade

Relative Bulk Density

Composation

W(Pt)/%

Pressure/MPa

Marks

CR-601

High

Pt-Sn-Additive

0.25

0.3-0.6

Producing Gasoline

CR-607

High

Pt-Sn-Additive

0.25

0.6-1.2

Producing Gasoline

CR-701

High

Pt-Sn-Additive

0.30

0.3-0.6

Producing

Aromatic Hydrocarbon

CR-707

High

Pt-Sn-Additive

0.30

0.6-1.2

Producing

Aromatic Hydrocarbon

CR-617

High

Pt-Sn-Additive

0.29

0.3-1.2

Other

CR-712

High

Pt-Sn

0.29

0.3-1.2

Other

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