Method for directionally lowering tobacco tar
A technology for tar and tobacco, which is applied in the field of reducing harmful tar of tobacco by supercritical fluid technology, can solve the problems of low energy, insufficient aroma, dull smoke, etc., and achieves the effects of less scrap material consumption, environmental friendliness and simple process
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Embodiment 1
[0017] (1). The extractor is loaded with 2Kg of raw cut tobacco. Supercritical carbon dioxide enters from the bottom and flows out from the top. The control pressure is 28MPa, and the temperature is 50°C.
[0018] (2). Flowing out from the extractor, the supercritical carbon dioxide containing cut tobacco extract enters a 4-stage rectification and separation tower equipped with activated carbon. The pressure of the rectification and separation tower is controlled to be 16Mpa, and the temperature is respectively 50, 60, 70, and 80°C.
[0019] (3). The supercritical carbon dioxide flowing out of the rectification separation tower is boosted to 28MPa, and then returned to the extractor after cooling down, and the cycle works for 4 hours.
[0020] (4). Lower the temperature of the extractor to 20°C, lower the pressure, and empty it to obtain the finished shredded tobacco.
Embodiment 2
[0022] (1). The extractor is loaded with 2Kg of raw cut tobacco. Supercritical carbon dioxide enters from the bottom and flows out from the top. The control pressure is 28MPa, and the temperature is 50°C.
[0023] (2). Flowing out from the extractor, the supercritical carbon dioxide containing cut tobacco extract enters a 2-stage rectification and separation tower equipped with diatomaceous earth. Control the pressure of the rectification and separation tower to 20Mpa, and the temperature to 60 and 80°C respectively.
[0024] (3). The supercritical carbon dioxide flowing out of the rectification separation tower is boosted, cooled and returned to the extractor, and the cycle works for 3 hours.
[0025] (4). Lower the temperature of the extractor to 20°C, lower the pressure, and empty it to obtain the finished shredded tobacco.
Embodiment 3
[0027] (1). The extractor is loaded with 2Kg of raw cut tobacco. Supercritical carbon dioxide enters from the bottom and flows out from the top. The control pressure is 28MPa, and the temperature is 50°C.
[0028] (2). Flowing out from the extractor, the supercritical carbon dioxide containing cut tobacco extract enters the 3-stage rectification and separation tower equipped with stainless steel mesh. The pressure of the rectification and separation tower is controlled to be 12Mpa, and the temperature is respectively 40, 60, and 80°C.
[0029] (3). The supercritical carbon dioxide flowing out of the rectification separation tower is pressurized and cooled and then returned to the extractor, and the cycle works for 5 hours.
[0030] (4). Lower the temperature of the extractor to 20°C, lower the pressure, and empty it to obtain the finished shredded tobacco.
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