Method for preparing biomass gas from plant branches and trunks
A biomass gas and branch technology, which is applied in the preparation of combustible gas and liquid hydrocarbon mixture, chemical instruments and methods, etc., can solve the problem of reducing biomass gas conversion rate, low gas combustion calorific value, and low gas combustion calorific value. and other problems, to achieve the effect of shortening the liquefaction processing time, increasing the combustion calorific value, and small equipment investment
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Embodiment 1
[0038] 1. Raw material preparation
[0039]Crush the corn stalks into straw fragments with a length ≤ 20mm, and set aside.
[0040] 2. Hydrothermal liquefaction treatment
[0041] 1) Mix corn stalk fragments with the first catalyst, then add water and stir evenly to obtain a mixed material, wherein the first catalyst is a mixture of sodium carbonate and lanthanum oxide, and the weight ratio of sodium carbonate and lanthanum oxide is 92:8 The weight ratio of corn stalk fragments (dry weight) to the first catalyst is 100:1.5; the weight ratio of corn stalk fragment weight (dry weight) to the weight of water in the mixed material is 40:60;
[0042] 2) Send the mixed material into a vertical refiner (Shandong Zhucheng Beitel Paper Equipment Co., Ltd.) to make pulpy corn stalk slurry, wherein the particle size of the prepared corn stalk slurry is ≤3mm;
[0043] 3) The straw slurry is pumped by a high-pressure plunger to a shell-and-tube preheater (Sinopec Puyang Zhongshi Group Gr...
Embodiment 2
[0063] In addition to using Salix salix as raw material;
[0064] In the process of hydrothermal liquefaction, except that in step 1), the weight ratio of salix fragments (dry weight) and the first catalyst is 100:2, and the weight ratio of sodium carbonate and lanthanum oxide in the first catalyst is 90:10 The ratio of the weight (dry weight) of Salix salix fragments to the weight of water in the mixed material is 30:70; the temperature of the preheated slurry in step 3) is 220°C; the temperature of hydrothermal liquefaction treatment in step 4) is 280°C; ℃, the absolute pressure is 9MPa, and the treatment time is 20min; the relative pressure of the liquefied mixture sent into the high-pressure buffer vessel in step 5) is reduced to 0.1MPa and sent outside the flash tank, and the rest are the same as in Example 1;
[0065] In the cracking and gasification process, except that the heating temperature in step 1) reaches 320°C, the weight ratio of sodium carbonate, lanthanum oxi...
Embodiment 3
[0068] In addition to using soybean straw as raw material;
[0069] In the hydrothermal liquefaction process, except that the weight ratio of soybean straw (dry weight) and the first catalyst in step 1) is 100:1, the weight ratio of sodium carbonate and lanthanum oxide in the first catalyst is 91:9; The ratio of the straw weight (dry weight) to the weight of water in the mixed material is 35:65; the temperature of the preheated slurry in step 3) is 230°C; the temperature of the hydrothermal liquefaction treatment in step 4) is 270°C, and the absolute pressure It is 10MPa, and the treatment time is 15min; the relative pressure of the liquefied mixture sent in the high-pressure buffer vessel in step 5) is reduced to 0.3MPa and then sent outside the flash tank, and all the other are the same as in Example 1;
[0070] In the cracking and gasification process, except that the heating temperature in step 1) reaches 330° C., the weight ratio of sodium carbonate, lanthanum oxide, and ...
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