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KC-102

The suitable operating conditions for KC-102 are listed as below:

  - Temperature: 180 - 480℃

  - Pressure: 1.0 – 5.0 MPa

  - Airspeed: 1000 - 6500h-1 (dry gas base)

  - Water-gas ratio: 0.1 – 1.0

  - Sulfur content: ≥0.005%(V/V) at low water-gas ratio

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Product Introduction

KC-102 is a Co-Mo-based sulfur-resistant CO-shift catalyst with the special carrier and new assistant agent, suitable for medium-pressure CO-shift processes of heavy oil, residual oil and coal. Particularly, it shows its great advantages in the low-temperature or low water-gas ratio shift processes of coal.

 

The active components of the KC-102 catalyst are the oxidation state of Co and Mo, which need to be sulfurized at the process start-up stage by using sulfur-containing process gas or sulfurizing reagent. During the sulfurization stage, only a small amount of water will be produced and discharged along with the process gas without generating any harmful chemicals.


Technical Features:

  - High mechanical strength and strength stability

  - High catalytic activity, especially for low-temperature or low water-gas ratio shift processes.

  - Excellent selectivity and active stability

  - High operating flexibility, with the adaptive capacity for high airspeed and wide water-gas ratio

  - Long working life and renewable.

 

Working Conditions:

  - Temperature: 180 - 480℃

  - Pressure: 1.0 – 5.0 MPa

  - Airspeed: 1000 - 6500h-1 (dry gas base)

  - Water-gas ratio: 0.1 – 1.0

  - Sulfur content: ≥0.005%(V/V) at low water-gas ratio


Physical and Chemical Properties:

Properties

Configuration 1

Configuration 2

Colour

Grey-green or blue-green   

Grey-green or blue-green

Configuration

Strip style

Small particle

Reactor

Axial shift reactor

Axial-radial or isothermal shift reactors

Dimensions (mm)

D 3.5 – 4.5

L 8.0 – 15.0

D 2.0 – 3.0

L 3.0 – 6.0

Bulk Density (kg/m3)

750 - 950

850 - 1000

Crushing Strength (N/cm)

≥130 (avg)

≥130 (avg)

Specific Surface Area (m2/g)       

≥100

(before sulfurization)

≥100

(before sulfurization)

Pore Volume (ml/g)

≥0.28

(before sulfurization)

≥0.28

(before sulfurization)

Catalyst dimensions can be adjusted based upon customer’s requirement, which may affect its bulk density and the bed pressure drop. 


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