Process for extracting lysine by ion exchange method
An ion exchange method and ion exchange resin technology are applied in the field of extracting lysine, which can solve the problems of wasting sulfuric acid and ammonia water, environmental pollution, etc., and achieve the effects of improving economic benefits and reducing the difficulty of environmental protection treatment.
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Embodiment 1
[0017] A lysine production plant with an annual output of 10,000 tons. Fermentation acid production is calculated at 10%. The annual production is 330 days, and the daily output of fermentation and filtered clear liquid is 300m 3 , containing 30 tons of lysine.
[0018] After the fermentation of lysine is completed, it is directly heated to 84°C in the fermenter for 16 minutes, then filtered, and the slag is removed to obtain the clear liquid, which is stored in 400m 3 volume storage tank.
[0019] 30 strongly acidic hydrogen-type neutral ion exchange columns for adsorption, each column contains 10m of ion exchange resin 3 , flow rate 0.5~15m 3 / m 3 Resin per hour, after the adsorption is saturated, wash with water to remove impurities, and then elute with 2 molar calcium chloride solution, the flow rate is 0.5 ~ 15m 3 / m 3 resin hours.
[0020] Pour the high-concentration components of the eluted effluent into the treatment tank, under stirring, adjust the pH to 6-7 wit...
Embodiment 2
[0023] Annual output of 5,000 tons of lysine production plant, 10% acid production by fermentation, 330 days of annual production, daily production of 150m of fermented and filtered clear liquid 3 , containing 15 tons of lysine.
[0024] After the fermentation is completed, heat it to 85°C in the tank, keep it for 15 minutes, filter the clear liquid, and store it in 200m 3 volume storage tank.
[0025] 15 strongly acidic hydrogen-type neutral ion exchange columns for adsorption, each column contains 10m of ion exchange resin 3 , flow rate 0.5~15m 3 / m 3 Resin per hour, after adsorption is saturated, rinse with water to remove impurities, then elute with 3 molar calcium chloride solution, flow rate 0.5 ~ 15m 3 / m 3 resin hours.
[0026] Put the high-concentration components of the eluate into the treatment tank, add sodium carbonate to adjust the pH to 6-7 under stirring, remove calcium plasma, then add 1-4% powdered activated carbon, continue stirring for 30 minutes, and...
Embodiment 3
[0028] Embodiment 3: as described in embodiment 1, the difference is that the eluent is 1.5 molar sodium chloride solution.
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