Reconstituted tobacco extract concentration process and concentration system
A technology for reconstituted tobacco leaves and extracts, which is applied in the fields of tobacco, tobacco preparation, and tobacco treatment. It can solve the problems of low-temperature membrane concentration concentration ratio and low concentration efficiency, and overcome the difficulty of membrane cleaning and replacement, concentration ratio and concentration efficiency. The effect of reducing and slowing down the degree of membrane fouling
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Embodiment 1
[0042] Concentrating the reconstituted tobacco leaf extract with an initial solid content of 8.6% by using the above-mentioned concentrating process and concentration system for the reconstituted tobacco leaf extract includes the following steps:
[0043] 1) The reconstituted tobacco leaf extract is pre-concentrated by the low-temperature dehydration membrane distillation process, that is, the reconstituted tobacco leaf extract with an initial solid content of 8.6% is pumped into the hot side channel of the membrane distillation device, and then air is injected into the device as a purge gas Cold side channel, the flow rate of purge gas in the cold side channel is 1m / s, the vacuum degree of the cold side channel is 0.01Mpa, water vapor continuously evaporates from the hot side feed liquid, penetrates the porous hydrophobic membrane and enters the cold side air Among them, the porous hydrophobic membrane has a membrane pore size of 0.1 μm, a porosity of 80%, and an air permeabil...
Embodiment 2
[0049] Concentrating the reconstituted tobacco leaf extract with an initial solid content of 8.6% by using the above-mentioned concentrating process and concentration system for the reconstituted tobacco leaf extract includes the following steps:
[0050] 1) The reconstituted tobacco leaf extract is pre-concentrated by the low-temperature dehydration membrane distillation process, that is, the reconstituted tobacco leaf extract with an initial solid content of 8.6% is pumped into the hot side channel of the membrane distillation device, and then air is injected into the device as a purge gas Cold side channel, the flow rate of purge gas in the cold side channel is 3m / s, the vacuum degree of the cold side channel is 0.02Mpa, the water vapor continuously evaporates from the hot side feed liquid, penetrates the porous hydrophobic membrane and enters the cold side air Among them, the porous hydrophobic membrane has a membrane pore size of 0.2 μm, a porosity of 82%, and an air perme...
Embodiment 3
[0056] Concentrating the reconstituted tobacco leaf extract with an initial solid content of 9.3% by using the above-mentioned concentrating process and concentration system for the reconstituted tobacco leaf extract includes the following steps:
[0057] 1) The reconstituted tobacco leaf extract is pre-concentrated by the low-temperature dehydration membrane distillation process, that is, the reconstituted tobacco leaf extract with an initial solid content of 8.6% is pumped into the hot side channel of the membrane distillation device, and then air is injected into the device as a purge gas Cold side flow channel, the flow rate of purge gas in the cold side flow channel is 7m / s, the vacuum degree of the cold side flow channel is 0.04Mpa, water vapor continuously evaporates from the hot side feed liquid, penetrates the porous hydrophobic membrane and enters the cold side air Among them, the porous hydrophobic membrane has a membrane pore size of 0.3 μm, a porosity of 90%, and an ...
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