Method for preparing coking coal by hydrogenating low-rank coal under catalysis of Ca
A low-rank coal and coking coal technology, applied in the field of coal modification, can solve problems such as complicated operation and impact on coke quality, and achieve the effect of improving component distribution and improving cohesiveness
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Embodiment 1
[0022] The test was carried out by hydrogenation of non-caking coal to produce coking coal.
[0023] 60g of 200-mesh non-caking coal, 80g of water and 2g of Ca-based catalyst (CaO 1.6g, Fe 2 o 3 0.3g, CeO 2 0.1g) into a high-temperature and high-pressure reactor and mix evenly, introduce a reducing gas mainly composed of CO, adjust the initial pressure to 4.5MPa (the content of CO is 95%), raise the temperature to 330°C, and the active hydrogen H·hydrogen supply is 16mol / kg of coal, and react for 60 minutes. After the reaction, cool the reactor to room temperature, take out the reaction materials, and separate the solid and liquid by filtration. The separated solid is the modified coal that can partially replace the coking coal.
[0024] The solid product was measured according to GB / T 5447-1997 by a cohesive index tester, and the cohesive index of the product was 93.
Embodiment 2
[0026] The coking coal produced by hydrogenation of weakly caking coal was tested.
[0027] 60g of 200 mesh weak caking coal, 70g of water and 1g of Ca-based catalyst (CaO 0.8g, FeO 0.15g, Ce 3 o 4 0.05g) into the reactor and mixed evenly, and the reducing gas mainly composed of CO was introduced, the initial pressure was adjusted to 4MPa (the content of CO was 90%), the temperature was raised to 320°C, and the amount of active hydrogen H·hydrogen supplied was 13.5mol / kg coal , and reacted for 45 minutes. After the reaction was completed, the reactor was cooled to room temperature, the reaction materials were taken out, and the solid and liquid were separated by filtration. The separated solid was the modified coal that could partially replace the coking coal.
[0028] The solid product was tested according to GB / T 5447-1997 by a caking index tester, and the caking index of the product was 90.
Embodiment 3
[0030] Experiment on producing coking coal by hydrogenation of long-flame coal
[0031] 200 mesh long flame coal 60g, water 60g and catalyst 1g (CaCO 3 0.85g, FeO 0.1g, CeO 2 0.05g) into a high-temperature and high-pressure reactor and mix evenly, introduce a reducing gas mainly composed of CO, adjust the initial pressure to 4.5MPa (the content of CO is 96%), raise the temperature to 335°C, and the active hydrogen H·hydrogen supply is 16.5mol / kg coal, react for 60 minutes, after the reaction is finished, cool the reactor to room temperature, take out the reaction material, filter and separate the solid and liquid, the separated solid is the modified coal that can partially replace the coking coal.
[0032] The solid product was tested according to GB / T 5447-1997 by a caking index tester, and the caking index of the product was 95.
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