Method for preparing algae material fuel by catalytic liquefying method
A technology for catalytic liquefaction and seaweed, which is applied in the preparation of liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems of cumbersome separation process of reaction products, difficulty in direct use of fuel, and low calorific value of bio-oil, and achieve economic and social benefits. Obviously, to avoid equipment corrosion, the effect of high content
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[0014] Example 1:
[0015] In this example, the large seaweed Prolifera was first washed and removed from impurities, and 28 g of dried and pulverized prolifera were taken, 5.6 g of water was added, and 1.4 g of Fe / HZSM-5 catalyst was added. The heating rate of 60°C / min was heated to 350°C, kept for 15 minutes, the reaction was terminated, and the reaction was naturally cooled in the air. Then, the solid-liquid product was subjected to atmospheric distillation, and the fractions between 60 and 500°C were collected. After separating the water in the fractions The liquid fuel oil was obtained with a yield of 18.39%, a calorific value of 44.69 MJ / kg, a H / C molar ratio of 1.82, and an oxygen content of 3.12%; figure 1 For the GC-MS total ion current chromatogram of the obtained liquid fuel, through mass spectral peak analysis, the main components of the obtained liquid fuel hydrocarbons include toluene, ethylbenzene, trimethylbenzene, propylbenzene, 1-vinyl- 2-methylbenzene, dode...
Example Embodiment
[0016] Example 2:
[0017] In this example, the large seaweed Prolifera was washed and removed from impurities, and 28 g of dried and pulverized prolifera were taken, 4.2 g of water was added, 0.84 g of Fe / HZSM-5 catalyst was added, and the mixture was uniformly placed into a steel airtight reaction kettle. The heating rate of 60°C / min was heated to 400°C, kept for 20min, the reaction was terminated, cooled in air naturally, and then the solid-liquid product was subjected to atmospheric distillation, the fraction between 60-500°C was collected, and the water in the fraction was separated. Liquid fuel oil was obtained with a yield of 17.81%, a calorific value of 42.89 MJ / kg, a H / C molar ratio of 1.64 and an oxygen content of 4.06%.
Example Embodiment
[0018] Example 3:
[0019] In this example, the large seaweed prolifera was first washed and removed from impurities, 28 g of dried and crushed prolifera were taken, 8.4 g of water was added, 1.68 g of Fe / HZSM-5 catalyst was added, and the mixture was uniformly placed into a steel airtight reaction kettle. The heating rate of 60°C / min was heated to 450°C, kept for 20min, the reaction was terminated, and cooled naturally in the air, and then the solid-liquid product was subjected to atmospheric distillation, the fraction between 60-500°C was collected, and the water in the fraction was separated. Liquid fuel oil was obtained with a yield of 19.27%, a calorific value of 43.25 MJ / kg, a H / C molar ratio of 1.71, and an oxygen content of 4.10%.
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