Method for purifying polysaccharide iron complex based on ultrafiltration membrane method
A technology for polysaccharide iron and complexes, which is applied in the field of purification of polysaccharide iron complexes, can solve the problems of complex process, influence on product purity, membrane pollution, etc., and achieves the effects of simple operation process, easy continuous production and reduction of salt concentration.
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Embodiment 1
[0026] use figure 1 The device shown in the figure deals with the crude pumpkin polysaccharide iron complex aqueous solution synthesized by the ferric chloride method. The ultrafiltration membrane module installed on the device is a multi-channel tubular ceramic ultrafiltration membrane module. The material of the membrane support is alumina, and the material of the membrane layer is Zirconia, with an average pore size of 5 nm, operated as cross-flow filtration. First, concentrate the crude pumpkin polysaccharide iron complex aqueous solution (sodium chloride content is about 15.0%wt, iron content is about 50mg / L) in the feed liquid tank 1 at a temperature of 60°C and a pressure of 0.15MPa. When the volume of the retained liquid in the liquid tank 1 is concentrated to 35% of the original volume, continue to add deionized water to the feed liquid tank, and control the water addition rate to be equal to the permeation flux of the ultrafiltration membrane until the sodium chlori...
Embodiment 2
[0029] use figure 1 The device shown in the figure deals with the crude aqueous solution of angelica polysaccharide iron complex synthesized by the ferric chloride method. The ultrafiltration membrane module installed on the device is a roll-type polyethersulfone ultrafiltration membrane module with a molecular weight cut-off of 5KDa, and the operation method is cross-flow filtration. . Firstly, the crude product aqueous solution of angelica polysaccharide iron complex in feed tank 1 (sodium chloride content is about 15.0%wt, iron content is about 50mg / L) is dialyzed at a temperature of 30°C and a pressure of 0.3MPa, and continuously Add deionized water in the feed liquid tank, control the rate of water addition to be equal to the permeation flux of the ultrafiltration membrane, until the concentration of sodium chloride in the ultrafiltration membrane permeate drops to 2.0%wt, then stop adding water, and the interception in the feed liquid tank 1 The liquid volume was conce...
Embodiment 3
[0032] use figure 1 The device shown in the figure deals with crude aqueous solution of Lycium barbarum polysaccharide iron complex synthesized by ferric chloride method. The ultrafiltration membrane module installed on the device is a flat polyamide ultrafiltration membrane module with a molecular weight cut-off of 10KDa, and the operation method is dead-end filtration. First, concentrate the crude Lycium barbarum polysaccharide iron complex aqueous solution (sodium chloride content is about 15.0%wt, iron content is about 50mg / L) in the feed liquid tank 1 at a temperature of 25°C and a pressure of 0.2MPa. When the volume of the retained liquid in the liquid tank 1 is concentrated to 50% of the original volume, continue to add deionized water to the feed liquid tank, and control the water addition rate to be equal to the permeation flux of the ultrafiltration membrane until the sodium chloride in the permeate of the ultrafiltration membrane The concentration was reduced to 1....
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