Device and process for recovering waste solvent generated in wet-process production of battery separators
A technology of battery diaphragm and recovery device, which is applied in the direction of only multi-stage serial refining process treatment, chemical instruments and methods, water/sewage multi-stage treatment, etc., to achieve the effects of high reliability, simple manufacturing process, and consistent pore size
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Embodiment 1
[0019] Collect the mixture containing dichloromethane, paraffin oil and water discharged from the wet process lithium ion battery diaphragm production line into the mixed liquid storage tank 1, and let it stand naturally for 10 minutes, so that part of the wastewater is easily separated from the dichloromethane and paraffin oil; The mixture containing dichloromethane, paraffin oil and water is transported to the first-stage circulating heating tower 3 through the mixed liquid delivery pump 2; the temperature in the first-stage circulating heating tower 3 is adjusted to 120°C, and the dichloromethane, The mixture of paraffin oil and water undergoes high-temperature evaporation. The evaporated gas is condensed in the environment of 40°C at the top of the first-stage circulating heating tower 3. After an interval of 1 minute, the mixed liquid circulating pump 6 is started, and the first-stage circulating heating tower 3 The material from the lower part is transported to the upper p...
Embodiment 2
[0021] Collect the mixture containing dichloromethane, paraffin oil and water discharged from the wet process lithium ion battery diaphragm production line into the mixed liquid storage tank 1, and let it naturally stand for 30 minutes, so that part of the waste water is easily separated from the dichloromethane and paraffin oil; The mixture containing dichloromethane, paraffin oil and water is transported to the first-stage circulating heating tower 3 through the mixed liquid delivery pump 2; the temperature in the first-stage circulating heating tower 3 is adjusted to 130°C, and the dichloromethane, The mixture of paraffin oil and water is evaporated at high temperature. The evaporated gas is condensed in the environment of 50℃ at the top of the first-stage circulating heating tower 3. After an interval of 2 minutes, the mixed liquid circulating pump 6 is started to turn the first-stage circulating heating tower 3 The material in the lower part is transported to the upper part...
Embodiment 3
[0023] Collect the mixture containing dichloromethane, paraffin oil and water discharged from the wet process lithium ion battery diaphragm production line into the mixed liquid storage tank 1, and let it stand for 20 minutes, so that part of the wastewater is easily separated from the dichloromethane and paraffin oil; The mixture containing dichloromethane, paraffin oil and water is transported to the first-stage circulating heating tower 3 through the mixed liquid transfer pump 2; the temperature in the first-stage circulating heating tower 3 is adjusted to 125°C, which will contain methylene chloride, The mixture of paraffin oil and water is evaporated at high temperature. The evaporated gas is condensed in the 45℃ environment at the top of the first-stage circulating heating tower 3. After an interval of 2 minutes, the mixed liquid circulating pump 6 is started to turn the first-stage circulating heating tower 3 The material from the lower part is transported to the upper pa...
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