Diesel oil hydrodesulphurization method
A technology for hydrodesulfurization and diesel oil, which is used in hydrotreating process, petroleum industry, processing of hydrocarbon oil, etc., can solve the problems of stable performance of the catalyst in the lower part of the reactor in the stable operation of the device, etc., so as to alleviate the reaction conditions and reduce the operation cost. , the effect of simple process
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Embodiment 1
[0035] Diesel feedstock 1 enters the first hydrogenation reactor, and the reaction conditions are: hydrogen partial pressure 5.8MPa, reaction temperature 352°C, hydrogen-oil volume ratio 300:1; the effluent enters the second hydrogenation reaction after passing through the gas stripping hydrogen dissolver device, the reaction conditions are: hydrogen partial pressure 5.5MPa, reaction temperature 348°C, hydrogen-oil volume ratio 200:1, total volume space velocity 1.9h -1 . The raw material oil properties and product properties are listed in Table 2.
[0036] It can be seen from Table 2 that the sulfur content of diesel products can be reduced to less than 50 μg / g by using this process technology, which meets the national standard IV clean diesel standard.
Embodiment 2
[0038] Diesel feedstock 2 enters the first hydrogenation reactor, and the reaction conditions are: hydrogen partial pressure 6.0MPa, reaction temperature 361°C, hydrogen-oil volume ratio 350:1; the effluent enters the second hydrogenation reaction after passing through the gas stripping hydrogen dissolver device, the reaction conditions are: hydrogen partial pressure 5.8MPa, reaction temperature 349°C, hydrogen-oil volume ratio 150:1, total volume space velocity 2.0h -1 . The raw material oil properties and product properties are listed in Table 3.
[0039] It can be seen from Table 3 that the sulfur content of diesel products can be reduced to 10 μg / g by using this technology, which meets the national standard V clean diesel standard.
Embodiment 3
[0041] Diesel raw material 3 enters the first hydrogenation reactor, and the reaction conditions are: hydrogen partial pressure 7.0MPa, reaction temperature 370°C, hydrogen-oil volume ratio 300:1; the effluent enters the second hydrogenation reaction after passing through the gas stripping hydrogen dissolver device, the reaction conditions are: hydrogen partial pressure 6.7MPa, reaction temperature 358°C, hydrogen-oil volume ratio 300:1, total volume space velocity 1.9h -1 . The raw material oil properties and product properties are listed in Table 4.
[0042] It can be seen from Table 4 that the sulfur content of diesel products can be reduced to less than 10 μg / g by using this process technology, which meets the national standard V clean diesel standard.
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