CN101525327B - 一种从越橘中提取花青素的方法 - Google Patents

一种从越橘中提取花青素的方法 Download PDF

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CN101525327B
CN101525327B CN2008100176412A CN200810017641A CN101525327B CN 101525327 B CN101525327 B CN 101525327B CN 2008100176412 A CN2008100176412 A CN 2008100176412A CN 200810017641 A CN200810017641 A CN 200810017641A CN 101525327 B CN101525327 B CN 101525327B
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cowberry
acid
extracting
anthocyanidin
resin
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CN101525327A (zh
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肖红
王晓莹
高娟
王春德
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SHAANXI JIAHE PHYTOCHEM CO., LTD.
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SHANXI JIAHE PLANT CHEMICAL CO Ltd
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Abstract

本发明涉及一种从越橘中提取花青素的方法。包含如下步骤:1]粉碎,2]提取,3]过滤:4]树脂纯化:i)控制操作过程温度≤60℃;ii)将步骤3]最终得到的膜过滤液用树脂吸附至饱和;iii)将吸附至饱和的树脂用水清洗,除杂,直至水洗液是无色;iv)用30~50%的乙醇或者甲醇解析大孔吸附树脂,收集流出液;v)浓缩流出液并干燥,得到花青素。本发明易于操作,成本低,提取含量高。

Description

一种从越橘中提取花青素的方法
技术领域
本发明涉及一种从植物中提取花青素的方法,尤其涉及一种从越橘中提取花青素的方法。
背景技术
现有越橘花青素的提取方法是采用大孔吸附树脂和离子交换树脂两种方法共同实现的,其具体实现步骤可参见2004年8月4日公告的公告号为CN1517343A的中国专利文件。现有方法使用乙醇浸泡越橘进而提取花青素,但此方法具有成本高,残留杂质较多,且采用离子交换树脂处理,由于离子交换树脂处理较为复杂,再生能力差,故操作过程较为繁琐的缺点。
发明内容
本发明提供了一种操作简单、成本低、纯度高的提取花青素的方法。
本发明的技术方案如下:
一种从越橘中提取花青素的方法,其特征在于,包含如下步骤:
1]粉碎:
i)取越橘果实,粉碎,将果实榨汁;
ii)将果实榨汁离心分离分别得到果渣和果汁;
2]提取
i)控制操作过程温度≤60℃,将所得果渣在30~50℃的操作温度下,用1~10%酸-水溶液浸泡,经浸泡搅拌提取2~3次,每次浸泡搅拌1.5~2h,得到提取液;
3]过滤:
i)控制操作过程温度≤60℃,
ii)将步骤2]最终得到的提取液与步骤1]中步骤ii)得到的果汁混合,形成混合液;
iii)将混合液经高速离心后,取上清液用无机膜超滤设备进行超滤,得到膜过滤液;其中无机膜超滤设备的膜孔径为10nm、20nm、50nm或100nm;
3]树脂纯化:
i)控制操作过程温度≤60℃;
ii)将步骤3]最终得到的膜过滤液用树脂吸附至饱和;
iii)将吸附至饱和的树脂用水清洗,除杂,直至水洗液呈无色;
iv)用30~50%的乙醇或者甲醇解析大孔吸附树脂,收集流出液;
v)浓缩流出液并干燥,得到花青素。
上述步骤1]中酸-水溶液中的酸为盐酸、硫酸、柠檬酸或冰乙酸。
上述步骤1]中酸-水溶液中的酸为冰乙酸。
上述步骤1]的操作温度为40℃,酸-水溶液浓度为10%。
上述步骤2]中无机膜超滤设备的膜孔径为50nm。
上述大孔吸附树脂为D101、AB-8、LSA-10、HPD-400、HP-20、ADS-17或XAD-2。
上述大孔吸附树脂为HP-20。
本发明具有以下优点:
1.易于操作。在整个工艺过程中使用的设备完全机械化,操作人员经过培训后即可上岗,因此操作简单。
2.花青素含量高。本发明采用先进的无机膜超滤设备进行超滤,除去大量淀粉、蛋白质、粘质液等杂质,经大孔吸附树脂柱进一步分离纯化,可达到50%,可使产品质量大大提高。
3.成本低。由于在提取过程中采用酸水提取,避免使用醇,降低了醇的消耗;而且超滤膜的使用,有效的除去大分子物质,最终使大孔吸附树脂的吸附量增加,提高了产品的收率,也同时降低成本。
具体实施方式
1.一种从越橘中提取花青素的方法,其特征在于,包含如下步骤:
1]粉碎:
i)取越橘果实,粉碎,将果实榨汁;
ii)将果实榨汁离心分离分别得到果渣和果汁;
2]提取
i)控制操作过程温度≤60℃,将所得果渣在30~50℃的操作温度下,用1~10%酸-水溶液浸泡,经浸泡搅拌提取2~3次,每次浸泡搅拌1.5~2h,得到提取液;酸-水溶液中的酸为盐酸、硫酸、柠檬酸或冰乙酸,采用冰乙酸为最佳,操作温度为40℃,酸-水溶液浓度为10%。
3]过滤:
i)控制操作过程温度≤60℃,
ii)将步骤2]最终得到的提取液与步骤1]中步骤ii)得到的果汁混合,形成混合液;
iii)将混合液经高速离心后,取上清液用无机膜超滤设备进行超滤,得到膜过滤液;其中无机膜超滤设备的膜孔径为10nm、20nm、50nm或100nm;膜孔径为50nm的效果最佳。
3]树脂纯化:
i)控制操作过程温度≤60℃;
ii)将步骤3]最终得到的膜过滤液用树脂吸附至饱和;
iii)将吸附至饱和的树脂用水清洗,除杂,直至水洗液呈无色;
iv)用30~50%的乙醇或者甲醇解析大孔吸附树脂,收集流出液;大孔吸附树脂为D101、AB-8、LSA-10、HPD-400、HP-20、ADS-17或XAD-2。
v)浓缩流出液并干燥,得到花青素。

Claims (10)

1.一种从越橘中提取花青素的方法,其特征在于,包含如下步骤:
1]粉碎:
i)取越橘果实,粉碎,将果实榨汁;
ii)将果实榨汁离心分离分别得到果渣和果汁;
2]提取
i)控制操作过程温度≤60℃,将所得果渣在30~50℃的操作温度下,用1~10%酸-水溶液浸泡,经浸泡搅拌提取2~3次,每次浸泡搅拌1.5~2h,得到提取液;
3]过滤:
i)控制操作过程温度≤60℃,
ii)将步骤2]最终得到的提取液与步骤1]中步骤ii)得到的果汁混合,形成混合液;
iii)将混合液经高速离心后,取上清液用无机膜超滤设备进行超滤,得到膜过滤液;其中无机膜超滤设备的膜孔径为10nm、20nm、50nm或100nm;
4]树脂纯化:
i)控制操作过程温度≤60℃;
ii)将步骤3]最终得到的膜过滤液用树脂吸附至饱和;
iii)将吸附至饱和的树脂用水清洗,除杂,直至水洗液呈无色;
iv)用30~50%的乙醇或者甲醇解析大孔吸附树脂,收集流出液;
v)浓缩流出液并干燥,得到花青素。
2.根据权利要求1所述的一种从越橘中提取花青素的方法,其特征在于:所述步骤2]中酸-水溶液中的酸为盐酸、硫酸、柠檬酸或冰乙酸。
3.根据权利要求2所述的一种从越橘中提取花青素的方法,其特征在于:所述步骤2]中酸-水溶液中的酸为冰乙酸。
4.根据权利要求1或2或3所述的一种从越橘中提取花青素的方法,其特征在于:所述步骤2]的操作温度为40℃,酸-水溶液浓度为10%。
5.根据权利要求1或2或3所述的一种从越橘中提取花青素的方法,其特征在于:所述步骤3]中无机膜超滤设备的膜孔径为50nm。
6.根据权利要求4所述的一钟从越橘中提取花青素的方法,其特征在于:所述步骤3]中无机膜超滤设备的膜孔径为50nm。
7.根据权利要求1或2或3所述的一种从越橘中提取花青素的方法,其特征在于:所述大孔吸附树脂为D101、AB-8、LSA-10、HPD-400、HP-20、ADS-17或XAD-2。
8.根据权利要求4所述的一种从越橘中提取花青素的方法,其特征在于:所述大孔吸附树脂为D101、AB-8、LSA-10、HPD-400、HP-20、ADS-17或XAD-2。
9.根据权利要求6所述的一种从越橘中提取花青素的方法,其特征在于:所述大孔吸附树脂为D101、AB-8、LSA-10、HPD-400、HP-20、ADS-17或XAD-2。
10.根据权利要求9所述的一种从越橘中提取花青素的方法,其特征在于:所述大孔吸附树脂为HP-20。
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CN102786506B (zh) * 2011-05-19 2015-04-22 长沙康隆生物制品有限公司 一种快速从越橘中制备25%花青素的工艺
CN102240316B (zh) * 2011-07-01 2013-06-12 宁波绿之健药业有限公司 一种从越橘上提取含有花青甙的提取物的方法
CN102807545B (zh) * 2012-08-08 2014-08-13 宁波杰顺生物科技有限公司 一种蔓越莓中原花青素提取物的制备方法
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CN103626733B (zh) * 2013-11-08 2015-07-29 天津大学 一种蓝莓花青素的分离方法
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CN105294633B (zh) * 2015-11-13 2018-08-28 大兴安岭林格贝寒带生物科技股份有限公司 一种从越橘中制备越橘花青素的工业化方法
CN114031952A (zh) * 2022-01-10 2022-02-11 罗麦(北京)营养食品研究有限公司 一种从植物中提取花青素的方法
CN114886886A (zh) * 2022-05-09 2022-08-12 中国计量大学 一种缓解紫外辐照损伤的越橘花青素的应用

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