Method for preparing high-quality gasoline and diesel oil from lignin pyrolysis oil
A technology for lignin cracking oil and lignin, which is applied in the field of using lignin cracking oil to prepare high-quality gasoline and diesel oil, can solve problems such as environmental pollution and waste of resources, and achieves wide source of raw materials, low cost, and ingenious and efficient coupling of reaction processes. Effect
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Embodiment 1
[0020] Embodiment 1: take 4-propylphenol as the conversion of raw material on different solid acids
[0021] In this example, the raw material of 4-propylphenol, a representative derivative of lignin (purchased from Aldrich Company), was used to test the product composition of its conversion on different solid acid catalysts. The specific method is as follows: take 0.01mol raw material, mix with 0.04g Pd / C catalyst (5wt.%, purchased from Aldrich Company), 2.0g solid acid (see Table 1), and 80ml water and add them to the high-pressure Parr kettle together. At room temperature, the gas was ventilated three times with hydrogen, and then filled with hydrogen to 50 bar, and then the temperature was raised to 200° C. for 0.5 hour, and the stirring speed was 680 rpm. Naturally cool to room temperature after the reaction, the product is automatically divided into two phases, the upper layer is the oil phase of the organic hydrocarbon mixture, and the lower layer is the water layer. A...
Embodiment 2
[0030] Example 2: Hydroalkylation / deoxygenation conversion using 4-propylphenol as raw material under different catalysts and conditions
[0031] In this example, 4-propylphenol, a representative derivative of lignin, was used as raw material to test its hydroalkylation and deoxygenation conversion under different catalysts and reaction conditions. The specific method is: take 0.01mol raw material, and 0.04g Pd / C or Pt / C or Ru / C or Pt / C catalyst (5wt.%, purchased from Aldrich company) or 2.0g Ni-based catalyst (self-made), 2.0g Hβ (Si / Al=150) molecular sieve or Pd / Hβ catalyst (self-made) (see Table 2 for the specific catalyst ratio) and 80ml of water were mixed and added to the autoclave Parr. After exchanging hydrogen gas three times at room temperature, hydrogen gas was charged to 50 bar, and then the temperature was raised to the reaction temperature for 0.5 hours (see Table 2 for specific reaction conditions), and the stirring speed was 680 rpm. After the reaction was fin...
Embodiment 3
[0038] Example 3: Hydroalkylation / deoxygenation conversion starting from different lignin-derived phenolic compounds
[0039] In this embodiment, the main components of lignin cracking oil, phenol, 4-methylphenol, 4-ethylphenol, 4-propylphenol, 2-methoxyl-4-acetonylphenol, 2-methoxyl-4 -Methylphenol, 2-methoxy-4-ethylphenol and 2-methoxy-4-propylphenol were used as raw materials to test their hydroalkylation / deoxygenation conversion activity under the Pd / Hβ catalyst. The specific method is as follows: 0.01mol of phenolic compound, 2.0g of 0.1wt.% Pd / Hβ catalyst and 80ml of water are mixed and then added to the high-pressure Parr kettle. After replacing the reaction vessel with hydrogen for three times, 50 bar of hydrogen was charged under normal pressure, and the temperature was raised to 200° C. to react for 2 hours, and then to 250° C. to react for 0.5 hours. Naturally cool to room temperature after the reaction, carry out the qualitative and quantitative detection of GC an...
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