Method for reducing content of chloride ions in paper-making method sheet tobacco
A technology of chloride ion content and reconstituted tobacco leaves, applied in tobacco, tobacco preparation, application, etc., can solve the problem of high chloride ion content, achieve the effect of reduction, resource saving, and emission reduction
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Embodiment 1
[0018] figure 1 Among them, it adopts a segmented helical one-stage co-current and two-stage counter-current extraction method including three-stage extraction and two dehydration processes. The specific process is:
[0019] It adopts three series-connected spiral extractors, and the first-stage spiral extractor is completed by the first-stage spiral extractor. The first-stage spiral extractor receives fresh solvent and fresh tobacco stems, and after extracting chloride ions, the obtained tobacco stems have a weight of 1.4 -1.6 times the primary extract with a chloride ion content of about 5-7g / L, the primary extract is treated with sewage and then discharged;
[0020] The tobacco stems obtained after the first-stage extraction are sent to the second-stage spiral extractor for the second-stage extraction. During the second-stage extraction, the secondary dehydration extract obtained from the second dehydration is used for extraction; The second-stage extracts are all sent to ...
Embodiment 2
[0022] figure 2 Among them, it adopts the one-stage downstream and two-stage countercurrent extraction method of the tank group, and the specific process is as follows:
[0023] The fresh solvent and fresh tobacco stems are sent to the first extraction tank for the first-stage extraction to obtain a primary extract with a weight of 1.4-1.6 times that of the tobacco stems and a chloride ion content of about 5-7g / L. After the sewage is treated and discharged, the first-stage extraction of the first extraction tank is the first-stage downstream;
[0024] The tobacco stems after the first-level extraction are sent to the second extraction tank in turn for the second-level extraction, and the third extraction tank for the third-level extraction; the second-level extraction obtained after the second-level extraction is all sent to the extraction liquid storage tank sent to the concentration section; at the same time, the second extraction tank also receives the extract from the ex...
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