Heterogeneous coal tar suspension bed hydrogenation method
A coal tar and suspended bed technology, applied in the field of coal chemical industry, can solve the problems of inflexible cutting method, no coal tar raw material utilization, inability to transport, etc., achieve flexible and optimized plan, improve cetane number, and save processing steps Effect
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Embodiment 1
[0037] A typical coal tar is selected as the coal tar raw material of this example, and the properties of the coal tar raw material after conventional dehydration and mechanical impurity pretreatment are shown in Table 1:
[0038] Table 1 Properties of Coal Tar Raw Materials
[0039]
[0040]
[0041] The pretreated coal tar is distilled and separated into IBP~260℃, 260~350℃ and heavy fractions greater than 350℃, and the heavy fraction oil greater than 350℃ is used as the raw material oil of the suspension bed hydrogenation reactor for hydrocracking light reaction.
[0042] The catalyst used in this example is a molybdenum-iron composite suspension bed hydrogenation catalyst, and the catalyst used includes molybdenum with a high activity metal component and iron with a low activity metal component, wherein the metal molybdenum with a high activity component and the iron metal with a low activity component The weight ratio is 1:500, the water content of the catalyst is l...
Embodiment 2
[0053] A kind of coal tar with higher heavy fraction content is selected as the coal tar raw material of this example, and the properties of the coal tar raw material after conventional dehydration and mechanical impurity pretreatment are shown in Table 4: the heavy fraction content of this feedstock oil is high, and the viscosity Higher, the viscosity at 40 ° C is more than 17 times that of the raw material oil in Example 1. Considering the problem of industrial equipment transportation, the viscosity of the material is too high to realize transportation. The raw material pretreatment is that the cutting temperature of distillation and separation of heavy distillate oil should be at 310°C.
[0054] Table 4 Properties of Coal Tar Raw Materials
[0055]
[0056]
[0057] In this experiment, the pretreated coal tar was separated into IBP~310°C and greater than 310°C heavy fractions by distillation, and the heavy fractions greater than 310°C were used as the feedstock oil o...
Embodiment 3
[0067]A kind of coal tar with higher heavy fraction content is selected as the coal tar raw material of this example, and the properties of the coal tar raw material after conventional dehydration and mechanical impurity pretreatment are shown in Table 7: the heavy fraction content of this raw material oil is high, and the viscosity Higher, the viscosity at 40 ° C is more than 17 times that of the raw material oil in Example 1. Considering the problem of industrial equipment transportation, the viscosity of the material is too high to realize transportation. The raw material pretreatment is that the cutting temperature of distillation and separation of heavy distillate oil should be at 280°C.
[0068] Table 7 Properties of Coal Tar Raw Materials
[0069]
[0070] In this experiment, the pretreated coal tar was separated into IBP~280°C and greater than 280°C heavy fractions by distillation, and the heavy fractions greater than 280°C were used as feedstock oil for the suspens...
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