Device and method for inhibiting turbidity of liquid maltitol
A maltitol and liquid technology, applied in the field of functional sugar production, can solve the problems of easy turbidity, short storage period, increased cost and the like during the storage process of liquid maltitol, and achieve the effects of avoiding turbidity of liquid maltitol, low cost, and not easy to become turbid.
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Embodiment 1
[0048] like figure 1 As shown, the heat exchanger 1 adopts a plate heat exchanger.
[0049] (1) Add liquid maltitol with a temperature of 25°C and a light transmittance of 99.0% or more at 420nm detected by a spectrophotometer into the heat exchanger through the feed liquid inlet, while the thermocouple in the storage tank detects the temperature in the storage tank, and The second flow control solenoid valve is controlled by the second PID module to open. At this time, the heat source inlet is passed into the heat exchanger. The heat source is the waste heat of evaporation and concentration, and the temperature of the liquid maltitol is regulated at 50°C through the heat exchanger;
[0050] (2) The liquid maltitol after the temperature control of the heat exchanger in step (1) enters the storage tank through the feed hole, and the electronic flowmeter detects the feed volume of the liquid maltitol, and according to the density of the liquid maltitol, it can be converted Obta...
Embodiment 2
[0054] like figure 1 As shown, the heat exchanger 1 adopts a shell-and-tube heat exchanger.
[0055] (1) Add liquid maltitol with a temperature of 20°C and a light transmittance of 97.0% or more at 420nm detected by a spectrophotometer into the heat exchanger through the feed liquid inlet, while the thermocouple in the storage tank detects the temperature in the storage tank, and The second flow control solenoid valve is controlled by the second PID module to open. At this time, the heat source inlet leads to the heat source into the heat exchanger. The heat source is fresh steam, and the temperature of the liquid maltitol is controlled at 40°C through the heat exchanger;
[0056] (2) The liquid maltitol after the temperature control of the heat exchanger in step (1) enters the storage tank through the feed hole, and the electronic flowmeter detects the feed volume of the liquid maltitol, and according to the density of the liquid maltitol, it can be converted Obtain the qual...
Embodiment 3
[0060] like figure 1 As shown, the heat exchanger 1 adopts a shell-and-tube heat exchanger.
[0061] (1) Add liquid maltitol with a temperature of 55°C and a light transmittance of 99.5% or more at 420nm detected by a spectrophotometer into the heat exchanger through the feed liquid inlet, while the thermocouple in the storage tank detects the temperature in the storage tank, and The second flow control solenoid valve is controlled by the second PID module to open. At this time, the heat source inlet leads to the heat source into the heat exchanger. The heat source is fresh steam, and the temperature of the liquid maltitol is controlled at 70°C through the heat exchanger;
[0062] (2) The liquid maltitol after the temperature control of the heat exchanger in step (1) enters the storage tank through the feed hole, and the electronic flowmeter detects the feed volume of the liquid maltitol, and according to the density of the liquid maltitol, it can be converted Obtain the qual...
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