Production method of high-quality clean fuel
A clean fuel and production method technology, which is applied in the petroleum industry, hydrotreating process, and hydrocarbon oil treatment, can solve the problems of high olefin content and sulfur content, low aromatic content, octane number loss, etc., and achieve yield and The effect of high octane number, simple process and low energy consumption
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Embodiment 1
[0018] Adopt the method provided by the invention, take catalytic cracking dry gas (composition see Table 1) and petroleum toluene as raw material. The DL0812 catalyst is filled in the reactor in equal proportions in 4 stages.
[0019] Table 1 Composition of catalytic cracking dry gas
[0020]
H 2
O 2
N 2
COx
CH 4
C 2 h 4
C 2 h 6
C 3 h 6
C 3 h 8
C 4
Others
vol%
15.21
0.43
22.37
2.98
25.93
19.52
11.62
1.29
0.43
0.12
0.1
[0021] FCC dry gas is divided into 4 paths according to the loading ratio of catalysts at all levels in the reactor. After heat exchange, it enters the inlets of catalyst beds at each level. Among them, the raw material of FCC dry gas at the first stage reaction inlet is mixed with toluene (including fresh toluene and recycled toluene) After heating, it enters the reactor and reacts on the catalyst. The reaction conditions are as follows: the...
Embodiment 2
[0024] Adopt the method provided by the invention, with enriched toluene light aromatics (toluene content~75wt%, all the other are benzene and aliphatic hydrocarbon), after ether C4 (olefin content~47wt%) and oxygen-containing compound (mass ratio is: methyl alcohol: two Methyl ether: ethanol: isobutanol=4:3:2:1) is raw material, wherein the mass ratio of carbon four after ether and oxygen-containing compound is 1:4. The DL0822 catalyst is loaded in 4 different stages in the reactor, and the catalyst loading ratio of each stage of the reactor is 15:20:30:35.
[0025] The C4 after the ether enters the inlet of the catalyst bed of the first stage after heat exchange, and enters the oxygen-containing compound raw material in the second to fourth stages. Among them, the C4 raw material at the entrance of the first stage reaction and the toluene raw material (including fresh toluene and recycled toluene) are mixed and heated and then enter the reactor, where alkylation, dehydration...
Embodiment 3
[0027] Using the method provided by the present invention, using propylene-rich gas (see Table 2 for its composition) and petroleum toluene as raw materials, the DL0805 catalyst is loaded in five equal stages in the reactor.
[0028] The propylene-rich gas is divided into 5 paths according to the catalyst loading ratio of each level of the reactor, and then enters the catalyst bed inlets of each level after heat exchange. Enter the reactor and react on the catalyst. The reaction conditions are as follows: the inlet temperature of the reaction bed in each stage is 170°C, the pressure is 3.0MPa, the molar ratio of benzene to olefin is 2.0, and the space velocity of olefin is 1.0h -1 . The conversion rate of propylene and total olefins is >99%, and the olefins generate C 5 + Selectivity >99%. After the product is separated, the toluene is recycled back to the alkylation reactor, and the hydrocarbonated liquid is fractionated to obtain high-octane gasoline and a small amount of...
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