Method for preparing biomass fuel by pyrolysis liquefaction of biomass
A biomass fuel and biomass raw material technology, applied in the preparation of biological raw materials, liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems that biomass oil cannot be used directly, affect the process yield, blockage, etc., and achieve good industrialization Foreground, increase product yield, effect of simple process
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Embodiment 1
[0028] The pyrolysis liquefaction of embodiment 1 bagasse
[0029] A certain amount of bagasse is dried to a water content lower than 10wt%, then crushed and sieved to obtain 30 grams of solid particles below 50 mesh (300 microns); the solid particles are mixed with 120 grams of washing oil and 1 gram of Na 2 CO 3 Stir and mix evenly in the container; add the obtained reaction mixture into a 0.5-liter stainless steel reaction kettle, heat up to 230°C under stirring conditions, the stirring speed used is 300 rpm, and the residence time of the reaction mixture in the reaction kettle The time is 3 hours, and the biomass oil obtained by pyrolysis and liquefaction is separated by rectification to obtain 3.45 grams of biomass light oil, 75 grams of biomass diesel oil and 70 grams of biomass heavy oil. It can be known from calculation that the yield of the pyrolysis liquefaction product in this embodiment is about 98.97%. In addition, it has been measured that the calorific value o...
Embodiment 2
[0030] The pyrolysis liquefaction of embodiment 2 corn cobs
[0031]Dry a certain amount of corncobs until the water content is lower than 10wt%, then crush and sieve to obtain 30 grams of solid particles below 70 mesh (200 microns); mix the solid particles with 120 grams of anthracene oil and 1.2 grams of CaCO 3 Stir and mix evenly in the container; add the resulting reaction mixture into a 0.5-liter stainless steel reactor, and heat it up to 260°C under stirring conditions. The stirring speed used is 200 rpm, and the reaction mixture stays in the reactor The time is 2.5 hours, and the biomass oil obtained by pyrolysis and liquefaction is separated by rectification to obtain 3.05 grams of biomass light oil, 70 grams of biomass diesel oil and 74 grams of biomass heavy oil. It can be known from calculation that the yield of the pyrolysis liquefaction product in this embodiment is about 98.03%. In addition, it has been measured that the calorific value of the obtained three bio...
Embodiment 3
[0032] Example 3 Pyrolysis and liquefaction of cotton stalks
[0033] Dry a certain amount of cotton stalks until the water content is lower than 10wt%, then crush and sieve to obtain 30 grams of solid particles below 60 mesh (250 microns); mix the solid particles with 120 grams of washing oil and 0.6 grams of K 2 CO 3 Stir and mix evenly in the container; add the resulting reaction mixture into a 0.5-liter stainless steel reactor, and heat it up to 240°C under stirring conditions. The stirring speed used is 350 rpm, and the reaction mixture stays in the reactor The time is 4 hours, and the biomass oil obtained by pyrolysis and liquefaction is separated by rectification to obtain 2.95 grams of biomass light oil, 69 grams of biomass diesel oil and 72 grams of biomass heavy oil. It can be known by calculation that the yield of the pyrolysis liquefaction product in this embodiment is about 95.97%. In addition, it has been measured that the calorific value of the obtained three ...
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Abstract
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