Direct coal liquefaction oil hydrogenation stabilization method
A technology of direct coal liquefied oil and liquefied oil, which is applied in the direction of refining to remove heteroatoms, etc., can solve the problems of high investment cost, high energy consumption in operation, and huge hydrogenation equipment, so as to reduce investment cost and energy consumption in operation, and improve effective Throughput, downscaling effects
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Example Embodiment
[0063] Example 1
[0064] The properties of the direct coal liquefied oil used in this example are listed in Table 1. The hydrogenation catalyst used is a HDO-2 catalyst produced by Hunan Changling Petrochemical Technology Company. This embodiment adopts Figure 5 The method shown performs hydrotreating of coal directly to liquefy oil. Among them, the structure of the gas-liquid mixer is as Figure 4 As shown, the structure of the components of the gas-liquid mixer for adjoining the liquid channel and the gas channel is a pipe formed of porous material (commercially purchased from Beijing Zhongtianyuan Environmental Engineering Co., Ltd., with 19 channels evenly distributed on the pipe, each The inner diameter of each channel is 3.3mm, the average pore diameter of the holes on the pipe wall is 50nm, and the number of holes in the range of 50-55nm accounts for 98% of the total number of holes); the channel on the pipe is used as a liquid channel, and the pipe The space formed by ...
Example Embodiment
[0083] Example 2
[0084] The direct coal liquefied oil was hydrotreated by the same method as in Example 1, with the following differences.
[0085] (1) The components in the gas-liquid mixer are as follows image 3 The membrane tube shown (commercially purchased from Beijing Zhongtianyuan Environmental Engineering Co., Ltd.; the average pore diameter of the pores on the substrate is 100 μm; the average pore diameter of the pores on the porous membrane is 500 nm, and the pores on the porous membrane with the pore diameter in the range of 500-550 nm The proportion of the total pores is 95%); the porous membrane is located on the outer wall of the membrane tube; there are 7 channels evenly distributed, and the inner diameter of each liquid channel is 6mm; the channel on the membrane tube is used as the liquid channel, and the membrane tube The space formed by the outer wall and the inner wall of the casing serves as a gas channel, and the filling rate of the membrane tube in the cas...
Example Embodiment
[0089] Example 3
[0090] The direct coal liquefied oil was hydrotreated by the same method as in Example 1, with the following differences.
[0091] (1) The components in the gas-liquid mixer are as follows figure 2 The membrane tube shown (commercially purchased from Beijing Zhongtianyuan Environmental Engineering Co., Ltd.; the average pore diameter of the pores on the substrate is 100 μm; the average pore diameter of the pores on the porous membrane is 250 nm, and the pores on the porous membrane are in the range of 250-260 nm. The proportion of the total pores is 95%); the porous membrane is located on the inner wall of the membrane tube; there are 7 channels evenly distributed, and the inner diameter of each liquid channel is 6mm; the channel on the membrane tube is used as the liquid channel, and the membrane tube The space formed by the outer wall and the inner wall of the casing serves as a gas channel, and the filling rate of the membrane tube in the casing is 50%.
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