Processing method for lysine-containing solution
A treatment method and technology of lysine, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problem of low yield of lysine
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Embodiment 1
[0055] use figure 2 In the process shown, the lysine-containing solution is contacted with multiple groups of cation-exchange resin column groups for ion-exchange chromatographic separation, and each group of cation-exchange resin column groups sequentially and cyclically passes through the adsorption zone, backfill zone, alkali conduction zone and regeneration zone , so that the cation exchange resin column group sequentially and cyclically performs exchange adsorption, purification and re-adsorption, desorption and regeneration, and obtains an eluent after desorption, wherein,
[0056] Three sets of cation exchange resin columns connected in series are in the adsorption area at the same time, each set of cation exchange resin columns is composed of 4 parallel cation exchange resin columns, and the cation exchange resin in the cation exchange resin column is WD-2 type lysine Special strong acid type cation exchange resin, the total exchange capacity of the cation exchange re...
Embodiment 2
[0061] use figure 2 In the process shown, the lysine-containing solution is contacted with multiple groups of cation-exchange resin column groups for ion-exchange chromatographic separation, and each group of cation-exchange resin column groups sequentially and cyclically passes through the adsorption zone, backfill zone, alkali conduction zone and regeneration zone , so that the cation exchange resin column group sequentially and cyclically performs exchange adsorption, purification and re-adsorption, desorption and regeneration, and obtains an eluent after desorption, wherein,
[0062] Three sets of cation exchange resin columns connected in series are in the adsorption area at the same time, each set of cation exchange resin columns is composed of 3 parallel cation exchange resin columns, and the cation exchange resin in the cation exchange resin column is WD-2 type lysine Special strong acid type cation exchange resin, the total exchange capacity of the cation exchange re...
Embodiment 3
[0067] use figure 2 In the process shown, the lysine-containing solution is contacted with multiple groups of cation-exchange resin column groups for ion-exchange chromatographic separation, and each group of cation-exchange resin column groups sequentially and cyclically passes through the adsorption zone, backfill zone, alkali conduction zone and regeneration zone , so that the cation exchange resin column group sequentially and cyclically performs exchange adsorption, purification and re-adsorption, desorption and regeneration, and obtains an eluent after desorption, wherein,
[0068] Three sets of cation exchange resin columns connected in series are in the adsorption area at the same time, each set of cation exchange resin columns is composed of 6 parallel cation exchange resin columns, and the cation exchange resin in the cation exchange resin column is WD-2 type lysine Special strong acid type cation exchange resin, the total exchange capacity of the cation exchange re...
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