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Separation and purification of phycocyanin from Spirulina sp. using a membrane process

机译:螺旋藻藻蓝蛋白的分离纯化使用膜工艺

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摘要

The highest purity ratio of phycocyanin extract was obtained when fresh biomass was used as raw material. The crude extract was purified by membrane process using microfiltration and ultrafiltration. Membrane of pore sizes 5μm, at feed flow rate of 150mLmin~(-1), permeate flux of 58.5Lh~(-1)m~(-2) was selected for coarse filtration and membrane with pore size 0.8/0.2μm at the flow rate of 100mLmin~(-1), permeate flux of 336Lh~(-1)m~(-2) was selected for fine filtration, giving phycocyanin recovery of 88.6% and 82.9%, respectively. For ultrafiltration, membrane with MWCO at 50kDa, 69kPa and 75mLmin~(-1) of flow rate with a mean permeate flux 26.8Lh~(-1)m~(-2) and a retention rate of 99% was found to be optimal. Under these filtration conditions, food grade phycocyanin with the purity around 1.0 containing c-phycocyanin as the major component was obtained.
机译:当以新鲜生物质为原料时,藻蓝蛋白提取物的纯度最高。粗提物通过使用微滤和超滤的膜工艺纯化。进料流量为150mLmin〜(-1)时,孔径为5μm的膜,选择58.5Lh〜(-1)m〜(-2)的渗透通量进行粗滤,而膜的孔径为0.8 /0.2μm流速为100mLmin〜(-1),渗透通量为336Lh〜(-1)m〜(-2)进行精细过滤,藻蓝蛋白的回收率分别为88.6%和82.9%。对于超滤,膜的分子量为50kDa,69kPa,流速为75mLmin〜(-1),平均渗透通量为26.8Lh〜(-1)m〜(-2),保留率为99%的膜为最佳。 。在这些过滤条件下,获得了以c-藻蓝蛋白为主要成分的纯度约为1.0的食品级藻蓝蛋白。

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