Method for extracting pectinos from gum arabic hydrolysate
A technology of arabinose and solution, applied in the field of simulated moving bed chromatographic separation, can solve the problems of inability to obtain separation, and achieve the effects of low production cost, small production site, and good adsorption and separation performance
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Embodiment 1
[0025] Example 1 Synthetic resin
[0026] Synthesize acidic calcium-type or lead-type chelating resins for special adsorption and separation of arabinose;
[0027] Among them, acidic calcium-type or lead-type chelating resins use acidic macroporous resins as carriers to chelate metal calcium ions or lead ions, and use the affinity between the acidic resin and metal calcium ions or lead ions to release metal calcium ions. Or lead ions are adsorbed on the surface of the acidic macroporous resin and fixed on the carrier resin with a crosslinking agent; the amount of the crosslinking agent is 4% to 20% of the weight of the acidic macroporous resin; the optimum is 10% to 14%.
[0028] metal Ca 2+ ion or Pb 2+ The ion is used in the form of metal Ca which can be dissolved under neutral or alkaline conditions 2+ ion or Pb 2+ Salts or oxides of ions, metal Ca 2+ ion or Pb 2+ The amount of ions to make the resin chelate reach 30% saturated amount to fully saturated amount;
Embodiment 2
[0029] Embodiment 2 separation and purification
[0030] A fixed bed equipped with the above-mentioned calcium-type or lead-type chelating resin is used to use simulated moving bed technology to separate and purify from the gum arabic hydrolyzate to obtain a pure arabinose product.
[0031] Simulated moving bed technology: In the simulated moving bed chromatographic separation device, the above-mentioned acidic calcium-type or lead-type chelating resin is used as the stationary phase adsorbent, and the affinity difference between the macromolecular metal adsorbent and various sugars is used to realize the separation of arabinose and semi-glucose. Complete separation of lactose, glucuronic acid and other miscellaneous sugars; using water as the eluent, the separation temperature is 35 ° C ~ 95 ° C, the optimal separation temperature is 70 ° C, continuous feeding and discharging operations, and at the same time Two types of output components, one is the component with arabinose ...
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