首页> 外国专利> Clarification and concn. of fruit and vegetable juices - by ultrafiltration in at least two stages with retained material in molecular wt. range 15000 to 25000

Clarification and concn. of fruit and vegetable juices - by ultrafiltration in at least two stages with retained material in molecular wt. range 15000 to 25000

机译:澄清和控制。果汁和蔬菜汁-通过至少两个阶段的超滤,保留分子重量的物质。范围15000至25000

摘要

Process is described for clarifying juice which has been extracted from fruit or vegetables by pressing. The process is of the type in which the expressed juice is passed through an ultrafiltration membrane which gives a primary clarified filtrate and a primary retained material which is passed through a second ultrafiltration membrane which yields a second clarified filtrate and second retained material. At least one of the ultrafiltration membranes is suited to hold retained material with a nominal molecular weight within the range of 15,000-25,000. Pref. the pH value of the expressed juice is determined and the temp. adjusted before clarification to within plus or minus 3 deg.C of (80-6pH) deg.C. At least one stage of ultrafiltration has an inlet pressure between 3 and 5 kg per square cm and an outlet pressure between 1 and 2 kg per square cm. Pref. a secondary filtrate is added to the primary filtrate and the primary retentate is diluted before secondary ultrafiltration. The process is to separate, concentrate or purify solutes in the molecular weight range 15,000-25,000, partic. for the extn. of pectins, starches, proteins, tannins etc. This ultrafiltration process requires less time, labour and energy than previous extn. methods to produce the above prods. No filtration additives are required and the clarified filtrates are sterile without heat treatment. Waste matter is reduced and prod. yield higher than with conventional extn. processes.
机译:描述了澄清通过压榨从水果或蔬菜中提取的汁液的方法。该方法是这样的类型,其中使榨汁通过超滤膜,其产生初级澄清的滤液,并且使初级保留材料通过第二超滤膜,其产生第二级澄清的滤液和第二级保留的材料。超滤膜中的至少一个适合于保持标称分子量在15,000-25,000范围内的保留材料。首选确定所榨汁的pH值和温度。在澄清之前将其调节到(80-6pH)摄氏度的正负3摄氏度之内。超滤的至少一个阶段的入口压力为每平方厘米3至5千克,出口压力为每平方厘米1至2千克。首选将二级滤液添加到一级滤液中,并在二级超滤之前稀释一级保留物。该方法是分离,浓缩或纯化分子量范围为15,000-25,000的溶质。对于extn。与果胶,淀粉,蛋白质,单宁酸等相比。这种超滤过程比以前的extn需要更少的时间,劳动力和能源。产生上述产物的方法。无需过滤添加剂,澄清的滤液无需加热即可灭菌。减少废物产生。产量高于传统extn。流程。

著录项

  • 公开/公告号ES8305568A1

    专利类型

  • 公开/公告日1983-04-16

    原文格式PDF

  • 申请/专利权人 VERNIERSS.A.;YVES VRIGNAUD *;

    申请/专利号ES19820513873

  • 发明设计人

    申请日1982-07-09

  • 分类号A23L2/30;

  • 国家 ES

  • 入库时间 2022-08-22 10:44:54

相似文献

  • 专利
  • 外文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号