Degerming method for recycling somatic cells from amino acid zymotic fluid/extraction waste liquid
A technology for bacterial cells and fermentation broth, applied in the field of fermented food industry, can solve the problems of inability to remove water-soluble proteins in fermentation broth, reduced protein content in filter residues, low bacterial cell removal rate, etc., and achieves low power consumption and reduced addition amount. , the effect of improving the filtration efficiency
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Embodiment 1
[0031] Embodiment 1: A method for removing bacteria from the amino acid fermentation liquid / extraction waste liquid, adopting the following process steps:
[0032] 1. Glutamic acid fermentation broth, glutamic acid concentration 12%, temperature 32°C, continuously sent to the tube side of the heat exchanger, the tube side of the heat exchanger is the glutamic acid from the maintenance tank at a temperature of 100 °C in step 3 For sour fermentation broth, the two materials exchange heat on the inner wall of the heat exchanger. After the heat exchange, the original 32°C fermentation broth is heated to 76°C, while the original 100°C fermentation broth is cooled to 50°C;
[0033] 2. The fermented liquid heated to 76°C flows into the heater, heated to 100°C with steam at a pressure of 0.3Mpa, then enters the maintenance tank, and stays in the maintenance tank for 30 minutes;
[0034] 3. Return the fermented liquid in the tank at 100°C to the tube side of the heat exchanger describe...
Embodiment 2
[0040] Embodiment 2: A method for removing bacteria from the amino acid fermentation liquid / extraction waste liquid, adopting the following process steps:
[0041] 1. Glutamic acid extraction waste liquid, glutamic acid concentration 2%, temperature 15 ℃, continuously sent to the shell side of the heat exchanger, the tube side of the heat exchanger is the valley of the temperature 80 ℃ from the maintenance tank in step 3 Acid extraction waste liquid, the two materials exchange heat in the heat exchanger, after the heat exchange, the original 15°C extraction waste liquid is heated to 45°C, while the original 80°C extraction waste liquid is cooled to 48°C;
[0042] 2. The extraction waste liquid heated to 45°C flows into the heater, heated to 80°C with steam at a pressure of 0.2Mpa, then enters the maintenance tank, and stays in the maintenance tank for 20 minutes;
[0043] 3. The extraction waste liquid in the maintenance tank at 80°C is refluxed to the tube side of the heat ex...
Embodiment 3
[0049] Embodiment 3: A method for removing bacteria from the amino acid fermentation liquid / extraction waste liquid, adopting the following process steps:
[0050] 1. Lysine fermentation broth, lysine concentration 16%, temperature 30°C, continuously sent to the shell side of the heat exchanger, the tube side of the heat exchanger is lysine from the maintenance tank at a temperature of 80°C in step 3 For acid fermentation broth, the two materials exchange heat in the heat exchanger. After the heat exchange, the extraction waste liquid at 30°C is heated to 50°C, while the lysine fermentation liquid at 80°C is cooled to 53°C;
[0051] 2. The lysine fermentation broth heated to 50°C flows into the heater, heated to 80°C with steam at a pressure of 0.3Mpa, then enters the maintenance tank, and stays in the maintenance tank for 25 minutes;
[0052] 3. The lysine fermentation liquid in the maintenance tank at 80°C is returned to the tube side of the heat exchanger described in step ...
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