Hydrorefining catalystis produced by using modified compound aluminum oxide as the carrier, contains active metal components and additives.
shape
Trifolium
Particle Size/mm
D(1.3~2.0)
Surface are /m2·g-1
≥ 200
Pore Volume /mL·g-1
≥ 0.32
Bulk Density/kg·L-1
0.88~0.98
Crushing strength/N·cm-1
≥ 150
2、Technical Index
Conditions Hydrogen pressure /MPa Temperature/℃ airspeed/h-1 Ratio of hydrogen 6.0 360 2.0 800 Oil of rescouse Coking diesel of Daqing Take off alkali nitrogen rate ≮90%
Conditions
Hydrogen pressure /MPa
Temperature/℃
airspeed/h-1
Ratio of hydrogen
6.0
360
2.0
800
Oil of rescouse
Coking diesel of Daqing
Take off alkali nitrogen rate
≮90%
3、Technological Conditions
conditions Type of rescourse oil Hydrogen pressure/ MPa Reaction temperature/℃ Airspeed/ h-1 Ratio of hydrogen Xinjiang victory and tube of catalytic diesel oil 3.0~6.0 260~300 1.0~2.0 300~600 Tube LianZha oil pipeline is mixed with catalytic diesel 3.0~6.0 270~310 1.0~2.0 300~500 Coking diesel of Daqing 3.0~6.0 280~320 1.0~2.0 400~600 Coking diesel of Shengli 6.0
conditions
Type of rescourse oil
Hydrogen pressure/
MPa
Reaction temperature/℃
Airspeed/
h-1
Xinjiang victory and tube of catalytic diesel oil
3.0~6.0
260~300
1.0~2.0
300~600
Tube LianZha oil pipeline is mixed with catalytic diesel
270~310
300~500
280~320
400~600
Coking diesel of Shengli
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