Continuous ion exchage extracting process for L-phenylalanine
A continuous ion and phenylalanine technology is applied in the field of continuous ion exchange extraction process of L-phenylalanine, which can solve the problems of low extraction yield and product purity, low utilization rate of upper column resin and high product extraction cost. , to achieve the effect of reducing extraction cost, realizing clean process production and saving acid and alkali consumption
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Embodiment 1
[0031] Take 10m 3 The upper column liquid, the concentration of L-phenylalanine is 20 g / L, with 2m 3 / h feed rate into the continuous chromatographic system, the adsorption pH is controlled at 2.0, and then 0.3mol / l eluent at 2m 3 The flow rate of / h washes off the phenylalanine adsorbed on the resin, and then obtains 197.6 kilograms of L-phenylalanine crystals after concentrating, crystallizing and drying the obtained L-phenylalanine eluent, and the purity is 98.8%, the yield is 98.5%.
Embodiment 2
[0033] Take 10m 3 The upper column liquid, the concentration of L-phenylalanine is 20 g / L, with 3m 3 / h feed rate into the continuous chromatographic system, the adsorption pH is controlled at 2.0, and then 0.3mol / l eluent at 2m 3 The flow rate of / h washes off the phenylalanine adsorbed on the resin, and then obtains 196.2 kilograms of L-phenylalanine crystals after concentrating, crystallizing and drying the obtained L-phenylalanine eluent, and the purity is 99.7%, the yield is 97.8%.
Embodiment 3
[0035] Take 10m 3 The upper column liquid, the concentration of L-phenylalanine is 20 g / L, with 4m 3 / h feed rate into the continuous chromatographic system, the adsorption pH is controlled at 2.0, and then 0.5mol / l eluent at 1m 3 The flow rate of / h washes off the phenylalanine adsorbed on the resin, and then obtains 195.6 kilograms of L-phenylalanine crystals after concentrating, crystallizing and drying the obtained L-phenylalanine eluent, and the purity is 98.4%, the yield is 97.2%.
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