Method for co-producing high-quality liquid fuel and system for implementing method
A technology for liquid fuels and raw materials, which is applied in the preparation of liquid hydrocarbon mixtures, biological raw materials, hydrocarbon oil treatment products, etc. The effect of carbon content
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Embodiment 1
[0158] Coal A was pulverized to <100 mesh (moisture content 12.36wt%), dehydrated and dried at 110°C for 0.5 hour to obtain dry coal powder as liquefaction feed. The residue coke from the residue slurry processing unit is pulverized as gasification feed. The heavy intermediate oil from the liquefaction separation / fractionation unit is mixed with the hydrogenated solvent oil from the solvent oil hydrogenation unit at a mass ratio of 6:4 as solvent oil.
[0159] Mix the liquefaction feed, solvent oil, and iron-based catalyst (see Example 1 of CN105363450B for specific composition) to obtain 1500 kg of liquefaction slurry with a solid content of 50 wt% (dry coal powder: solvent oil: iron in the catalyst = 100: 100:0.5, mass ratio); mix fresh hydrogen, circulating hydrogen and Fischer-Tropsch tail gas (volume ratio 10:60:30) as liquefaction reaction gas; in the slurry bed liquefaction reactor, liquefaction slurry and liquefaction reaction gas Under the conditions of 450°C, 4.5MPa...
Embodiment 2
[0167] Coal B and waste tires were crushed to below 100 mesh (water content 9.6wt%), dehydrated and dried at 110°C for 0.5 hours, as liquefaction feed (dry coal powder + dry waste tire powder), the catalyst was a nickel-containing additive 0.05 wt% of iron-based catalysts. The residual coke powder and coal powder from the residual slurry processing unit are used as gasification feed; the heavy intermediate oil and coal tar from the liquefaction separation / fractionation unit are mixed at a mass ratio of 1:1 as solvent oil.
[0168] Liquefied feed, solvent oil, iron-based catalyst (powdered FeOOH, additive component is 12wt% SiO 2 , 6wt%Al 2 o 3, 0.2wt% V and 0.5wt% Ni) mixed to make liquefied slurry 900kg of solid content 55wt% (coal powder: waste tire powder: heavy intermediate oil: coal tar: iron in the catalyst=45:10:35: 10:1, mass ratio). The recycled hydrogen and crude synthesis gas are mixed (volume ratio 4:1) as liquefied reaction gas. In the slurry bed liquefaction...
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