Preparation device and method of tobacco raw material concentrated solution
A technology for preparing devices and concentrates, which is applied in the fields of tobacco, tobacco preparation, and tobacco treatment, and can solve the problems of non-continuous operation and low energy utilization efficiency, and achieve the effects of easy implementation, improved effect, and simple preparation method
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[0015] The invention provides a preparation device for tobacco raw material concentrate, comprising a pre-concentration tank 1, a centrifugal pump 2, a heat exchanger 3, a primary crystallization tank 4, a secondary crystallization tank 5, a micro heat pipe 6, a horizontal centrifuge 7, a washing machine The net tower 8, the pre-concentration tank 1 is used to store the tobacco raw material extract, the outlet end of the pre-concentration tank 1 is connected to the heat exchanger 3 through the centrifugal pump 2, and the outlet end of the heat exchanger 3 is connected to the primary crystallization tank 4 and the secondary crystallization tank 4. The tanks 5 are connected in series successively, the outlet end of the upper part of the secondary crystallization tank 5 is connected with the micro heat pipe 6 and the horizontal centrifuge 7 in sequence, the solid outlet end of the horizontal centrifuge 7 is connected with the washing tower 8, and the liquid of the horizontal centri...
Embodiment 1
[0019] A method for preparing tobacco raw material concentrate, comprising the steps of:
[0020] First, 10 kg of the tobacco raw material extract with a solid content of 8% in the pre-concentration tank 1 is introduced into the heat exchanger 3 (the present embodiment adopts a shell-and-tube heat exchanger) through the centrifugal pump 2, and is generated at a temperature of -5°C. Part of the fine ice crystals are sent to the primary crystallization tank 4 and the secondary crystallization tank 5 for crystallization in turn. The agitator speeds in the primary crystallization tank 4 and the secondary crystallization tank 5 are respectively 200r / min and 300r / min. After 15min, the large ice crystals Gradually grow, and then transport the large ice crystals to the micro heat pipe 6 for slight heating. The temperature of the micro heat pipe 6 is maintained at 40 degrees Celsius, and then sent to the horizontal centrifuge 7 for solid-liquid separation. The separated ice crystals are...
Embodiment 2
[0026] A method for preparing tobacco raw material concentrate, comprising the steps of:
[0027] First, 10 kg of the tobacco raw material extract in the pre-concentration tank 1 with a solid content of 7% is introduced into the heat exchanger 3 (a shell-and-tube heat exchanger is used in this embodiment) through a circulation pump, and some fine particles are generated at a temperature of -7°C. After the ice crystallization, send into primary crystallization tank 4 and secondary crystallization tank 5 to carry out crystallization. The rotational speed of the agitator in the primary crystallization tank 4 and the secondary crystallization tank 5 is respectively 300r / min and 400r / min. After 12 minutes, the large ice crystals gradually grow, and then the large ice crystals are transported to the micro heat pipe 6 for slight heating, and the temperature of the micro heat pipe remains at 50 degrees centigrade, and then sent to the horizontal centrifuge 7 for solid-liquid separatio...
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