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Hydrotreating Catalyst

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产品名称: Hydrotreating Catalyst
产品型号: HHLDS-1,HHLDS-2,HHLDS-3
产品展商: Lihua
产品价格: 0.00 元

简单介绍
Hydrotreating Catalyst is specially developed for reforming pre-hydrogenation, solvent oil hydrotreating and Kerosene hydrotreating.

Hydrotreating Catalyst的详细介绍

1. Application
According to that light distillate has different features from different refinery depends on raw material and operation condition, HHLDS series Hydrotreating Catalyst is specially developed for reforming pre-hydrogenation, solvent oil hydrotreating and Kerosene hydrotreating.
 
2. Technology features
There are 3 types catalyst taking modified alumina as carrier.
HHLDS-1 has excellent hydrodesulfurization, high crush strength and small bulk density, specially suitable for light distillate of high sulfur.
With low pressure, low hydrogen/oil ratio, high space velocity, this catalyst could produce high quality reforming material with sulfur+nitrogen<0.5ppm.
HHLDS-2 also could remove nitrogen besides sulfur, which is suitable for hydrotreating process of light distillate specially for coking naphtha, pyrolysisgasoline and high nitrogen naphtha. This catalyst could work at 5℃ lower temperature than similar types of catalyst.
HHLDS-3 has large pore volume, large surface area to remove sulfur and nitrogen, which has working well for reforming prehydrogenation and coking gasoline hydrotreating process.


3. Chemical Composition and Physical Properties

Catalyst type

HHLDS-1

HHLDS-2

HHLDS-3

Active metal

Mo-Co

Mo-Ni

Mo-Ni-Co

Shape

sphere

trefoil

trefoil

Diameter, mm

f1.5~2.5

f1.5~2.5

f1.5~2.5

Pore volume,mL.g-1

≧0.40

≧0.40

≧0.42

Surface area, m2.g-1

≧200

≧200

≧220

Crush strength, N/pcs

≧40

≧140

≧140

Bulk density, g/cm

0.68~0.78

0.68~0.78

0.65~0.75

 

4. Operation Condition

Reforming Prehydrogenation

Reaction pressure

1.62.4 MPa

Temperature

270320 ℃

Volume space velocity

6.08.0 h-1

Hydrogen/oil volume ratio

80150

Coking naphtha and pyrolysis gasoline Hydrotreating

Reaction pressure

3.04.0 MPa

Temperature

180280 ℃

Volume space velocity

1.64.0 h-1

Hydrogen/oil volume ratio

300600


5. Operation Example of Reforming pre-hydrogenation under high space velocity

Item

Example 1

Example 2

   Raw material

    Product

    Raw material

    Product

Technical condition

 

 

Hydrogen partial pressure, MPa

1.6

1.6

 

Volume space velocity, h-1

8.0

6.0

Hydrogen/oil ratio

80

100

 

Operation condition, ℃

fiducial temperature

fiducial temperature

Oil properties

Raw material

Hydrotreated oil

Raw material

Hydrotreated oil

Sulfur, mg/g

702

<0.5

815

<0.5

Nitrogen, mg/g

1.5

<0.5

1.0

<0.5


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