CN1238341A - 高品质甜菊糖甙分离富集新工艺 - Google Patents

高品质甜菊糖甙分离富集新工艺 Download PDF

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CN1238341A
CN1238341A CN 98111347 CN98111347A CN1238341A CN 1238341 A CN1238341 A CN 1238341A CN 98111347 CN98111347 CN 98111347 CN 98111347 A CN98111347 A CN 98111347A CN 1238341 A CN1238341 A CN 1238341A
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glucoside
quality
glycoside
stevioside
raw material
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CN1098860C (zh
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管志健
陈为民
姚欣梅
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Institute of Botany of CAS
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Abstract

甜菊糖甙是由天然多年生草本植物甜菊叶中提取的物质,其中的主要成分有甜菊二糖甙(甙1)、甜菊甙(甙2)、菊甙B(甙3)和甜菊甙A(甙4)*。衡量甜菊糖的品质标准是以甙4与甙2的比,以比值高为质好。本发明是将甙4与甙2之比在0.5~1.1比值基础上的甜菊糖甙,采用分离、富集的新工艺,获得了甙4与甙2比值达到2.5以上的甜菊糖甙,提高了产品品质,满足国内外市场的需求,可取得显著的经济效益。甙4Redaudioside A甙2Stevioside

Description

高品质甜菊糖甙分离富集新工艺
甜菊糖甙是由天然多年生草本植物甜菊叶中提取的甜味物质。我国近年来,每年都有几十万亩地的甜菊叶种植,由于其中95%以上是老品种,且品质不断退化。由其作为原料生产出的甜菊糖甙具体品质指标甙4与甙2之比的值仅在0.2~0.9之间(见图1),因此价格低,销售不畅,影响农民种植积极性,造成工厂亏损等问题。
发明是用甙4与甙2之比在0.5~1.1的甜菊糖甙为原料,采用溶剂溶解原料、分离和富集的新工艺,提高甜菊糖甙的品质,产品品质为甙4与甙2的比值达到2.5倍以上(见图2)。其中的主要成分中文名称与英文名称对照如下:
 色谱峰编号  中文简称  中文名称       英文名称
①②③④    甙1甙2甙3甙4 甜菊二糖甙甜菊甙甜菊甙B甜菊甙A     SteviolbiosideSteviosideRedaudioside BRedaudioside A
本发明的新工艺实施后,可提高经济效益,解决种植和加工发展中的问题,拓展国内外市场的销售渠道。
本发明经查新无有关工艺的文献报导,属创造性的新工艺。
实例:
工艺步骤:
原料:甙4与甙2之比在0.5~1.1之间的甜菊甙
溶剂:去离子水
甲醇(80%以上)容器:500~700升反应罐一只
  500~700升蒸馏罐一只机械设备:加液泵;真空吸滤设备;搅拌机等步骤:    将50~150kg原料加入反应罐;加入甲醇300~800溶解原料,搅拌10~40分钟,有大量沉淀物产生,静置20~60分钟后,将上层溶液经滤膜真空吸滤,滤入蒸馏罐。蒸去大部分甲醇后,加水50~300升,将甲醇蒸净,得到一次提取液。
在反应罐中再加300升甲醇搅拌10~40分钟,静置20~60分钟后,将上层溶液经滤膜真空吸滤,滤入蒸馏罐,蒸去大部分甲醇后,加水50~300升,将甲醇蒸净,得到二次提取液。
将两次提取的清液合并,用离子交换树脂脱盐,用活性碳脱色,得到清液。经喷雾干燥后,得白色粉状产品。得率:产品为35~65%。效果:产品的甙4与甙2之比大于2.5,总甙量95%以上。

Claims (5)

1.一种用甜菊糖甙为原料,能提高甜菊糖甙中甙4与甙2比值的工艺技术,其特征为通过溶解原料,分离及精制后得到高品质的甜菊糖甙。
2.根据权利要求1,其溶解溶剂为甲醇,搅拌时间在2小时之内。静置时间在2小时内。
3.根据权利要求2,其原料的溶液过滤采用膜真空吸滤器。
4.根据权利要求3所得的滤液,用离子交换树脂脱盐、用活性碳脱色。
5.根据权利要求2~权利要求4的工艺技术,所得的白色粉状产品,其得率为35~65%,产品中甙4与甙2之比值达到2.5以上,总甙量为95%以上的高品质甜菊糖甙。
CN98111347A 1998-06-08 1998-06-08 高品质甜菊糖甙分离富集工艺 Expired - Fee Related CN1098860C (zh)

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