发明名称 |
Methods for producing phytoextracts from vegetation waters and olive oil pomaces and compositions obtained thereby |
摘要 |
Methods are provided for obtaining phytoextracts from vegetation waters and pomaces coming from olive milling. Such methods may be based on combining physical-chemical and enzymatic pre-treatment methods, membrane tangential filtration and vacuum evaporation. Such methods allow eco-sustainable and efficient extraction of the active ingredients involved. Compositions resulting from such methods are also provided. |
申请公布号 |
US8815815(B2) |
申请公布日期 |
2014.08.26 |
申请号 |
US201213479336 |
申请日期 |
2012.05.24 |
申请人 |
Phenofarm S.r.l. |
发明人 |
Germani Stefano;Vitagliano Massimo;Pizzichini Daniele;Pizzichini Massimo |
分类号 |
C07H17/04;A61K31/7048;A23L1/212;A23L1/30;A61K36/63 |
主分类号 |
C07H17/04 |
代理机构 |
|
代理人 |
Alderson, Jr. Robert E. |
主权项 |
1. A method for the extraction and concentration of polyphenolic compounds contained in vegetation waters and/or in pomaces obtained by processing of olives comprising the steps of:
i) collecting a liquid contained in vegetation waters and/or pomaces obtained by a milling processing; ii) pretreating said liquid chemically, physically and enzymatically; iii) tangentially filtering at a temperature from about 45 to about 50° C., thereby obtaining a concentrate fraction and a permeate fraction; iv) evaporating via vacuum technique the permeate phase; wherein said pretreating comprises: a) acidification to a pH between about 2.5 and about 4; b) enzymatic treatment by addition of a pool of cellulolytic and pectolytic enzymes, wherein during said enzymatic treatment the liquid is maintained under a hydraulic agitation by operating a process for a recirculation of the same liquid eccentrically with respect to the wall of a reactor, wherein said agitation is maintained for a time of 2 to 6 h, at a temperature in a range of 30 to 50° C. when working with vegetation waters or wherein said hydraulic agitation is maintained for about 12-24 h at a temperature in a range of 50 to 80° C. when working with pomaces; and c) elimination of a solid or semi-solid residue cap, which is collected on the surface at the end of said step b) wherein said residue has a density between about 0.7 and about 0.85 g/cm3, wherein said elimination takes place by pumping and sending a liquid mass collected on the bottom of the pre-treatment reactor to a subsequent filtration section, and said cap constitutes 2-7% by weight with respect to the total mass of the vegetable water and contains about 20% of the solids present in the initial vegetable waters thereby producing a consumable olive oil composition. |
地址 |
Rome IT |