Method for producing fuel oil by hydrogenation modification of coal tar
A hydrogenation modification and coal tar technology, which is applied in the direction of gasoline stabilization, refining to remove heteroatoms, etc., can solve the problems of high benzene insoluble matter, high prehydrogenation temperature, and large heat release, etc., to prolong the start-up period and reaction The effect of easing conditions and prolonging the operation cycle
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Embodiment 1
[0024] A medium-low temperature coal tar produced in a coking plant, the properties of which are shown in Table 1. After the light and heavy fractions are fractionated in the conventional fractionating tower, the light fractions are obtained by the conventional method of the coking plant to obtain about 3.5% crude phenol products, and the heavy fractions and the diluent oil (refinery catalytic diesel oil) are mixed uniformly in a ratio of 3:1 and then extracted. The heavy fraction was mixed with the dephenolized light fraction to obtain coal tar hydrogenation feed, and its properties are shown in Table 1. The pre-hydrogenation reactor is filled with molybdenum-nickel-based pre-hydrogenation catalyst and HG-1 hydrogenation protection agent, and the main hydrogenation reactor is filled with molybdenum-nickel-tungsten-phosphorus main hydrogenation catalyst. No coke inhibitor is added to the coal tar hydrogenation feed, and it enters the pre-hydrogenation reactor and the main hydr...
Embodiment 2
[0031] A medium-low temperature coal tar produced in a coking plant, the properties of which are shown in Table 3. After the light and heavy fractions are fractionated in the conventional fractionating tower, the light fractions are obtained by the conventional method of the coking plant to obtain about 4% crude phenol products. Finally, it is mixed with the dephenolized light fraction to obtain the coal tar hydrogenation raw material, and its properties are shown in Table 1. The pre-hydrogenation reactor is filled with molybdenum-nickel-based pre-hydrogenation catalyst and HG-1 hydrogenation protection agent, and the main hydrogenation reactor is filled with molybdenum-nickel-tungsten-phosphorus main hydrogenation catalyst. After adding 150ppm of coke inhibitor to the coal tar hydrogenation raw material, it enters the pre-hydrogenation reactor and the main hydrogenation reactor in turn. The pre-hydrogenation reaction conditions are pressure 12.0MPa, temperature 220°C, hydroge...
Embodiment 3
[0038] A high-temperature coal tar produced in a coking plant, the properties of which are shown in Table 5. After the light and heavy fractions are fractionated in the conventional fractionating tower, the light fractions are obtained by conventional methods in coking plants to obtain about 7% crude naphthalene products, and the heavy fractions and diluent oil (refinery catalytic diesel oil) are mixed uniformly in a ratio of 1:3 and then extracted. Finally, it is mixed with the dephenolized light fraction to obtain the coal tar hydrogenation raw material, and its properties are shown in Table 5. The pre-hydrogenation reactor is filled with molybdenum-nickel-based pre-hydrogenation catalyst and HG-1 hydrogenation protection agent, and the main hydrogenation reactor is filled with molybdenum-nickel-tungsten-phosphorus main hydrogenation catalyst. After adding 300ppm of coke inhibitor into the coal tar hydrogenation raw material, it enters the pre-hydrogenation reactor and the m...
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