MX2015010196A - Method for enriching valuable substances from a liquid raw material. - Google Patents
Method for enriching valuable substances from a liquid raw material.Info
- Publication number
- MX2015010196A MX2015010196A MX2015010196A MX2015010196A MX2015010196A MX 2015010196 A MX2015010196 A MX 2015010196A MX 2015010196 A MX2015010196 A MX 2015010196A MX 2015010196 A MX2015010196 A MX 2015010196A MX 2015010196 A MX2015010196 A MX 2015010196A
- Authority
- MX
- Mexico
- Prior art keywords
- extraction agent
- raw material
- liquid raw
- valuable substances
- charged
- Prior art date
Links
- 239000002994 raw material Substances 0.000 title abstract 3
- 239000000126 substance Substances 0.000 title abstract 3
- 239000007788 liquid Substances 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- 239000003795 chemical substances by application Substances 0.000 abstract 6
- 238000000605 extraction Methods 0.000 abstract 6
- 239000012141 concentrate Substances 0.000 abstract 3
- 239000003963 antioxidant agent Substances 0.000 abstract 1
- 235000010633 broth Nutrition 0.000 abstract 1
- 239000003086 colorant Substances 0.000 abstract 1
- 239000000284 extract Substances 0.000 abstract 1
- 238000000855 fermentation Methods 0.000 abstract 1
- 230000004151 fermentation Effects 0.000 abstract 1
- 150000002632 lipids Chemical class 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 235000017807 phytochemicals Nutrition 0.000 abstract 1
- 229930000223 plant secondary metabolite Natural products 0.000 abstract 1
- 150000008442 polyphenolic compounds Chemical class 0.000 abstract 1
- 235000013824 polyphenols Nutrition 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000002904 solvent Substances 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0403—Solvent extraction of solutions which are liquid with a supercritical fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0446—Juxtaposition of mixers-settlers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0488—Flow sheets
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
- C09F1/00—Obtaining purification, or chemical modification of natural resins, e.g. oleo-resins
- C09F1/02—Purification
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Extraction Or Liquid Replacement (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
In a method for enriching valuable substances, in particular phytochemicals, such as polyphenols, colorants, antioxidants and similar, from a liquid raw material, such as lipids, fermentation broths or solvent extracts, the raw material is mixed in a mixing device (5) with a compressed extraction agent, in particular CO2, from a storage container (1), whereupon the mixture is fed to a pre-concentrate separator (13) and the more highly soluble components in the extraction agent are separated from the undissolved components. The charged extraction agent is extracted from the pre-concentrate separator (13) and the undissolved components remain as a pre-concentrate, wherein the charged extraction agent is guided via a separation system, in which the dissolved substances are separated from the charged extraction agent, wherein the purified extraction agent is returned to the storage container (1).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ATA101/2013A AT513907B1 (en) | 2013-02-07 | 2013-02-07 | Process for the enrichment of valuable substances from a liquid raw material |
PCT/AT2014/000006 WO2014121311A1 (en) | 2013-02-07 | 2014-01-14 | Method for enriching valuable substances from a liquid raw material |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2015010196A true MX2015010196A (en) | 2016-04-28 |
Family
ID=50151052
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2015010196A MX2015010196A (en) | 2013-02-07 | 2014-01-14 | Method for enriching valuable substances from a liquid raw material. |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2953699A1 (en) |
AT (1) | AT513907B1 (en) |
MX (1) | MX2015010196A (en) |
WO (1) | WO2014121311A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104927665B (en) * | 2015-05-20 | 2017-06-16 | 山东天博食品配料有限公司 | A kind of method that utilization supercritical carbon dioxide extracting fermented capsicum prepares capsicum oleoresin |
JP7051088B2 (en) * | 2018-02-23 | 2022-04-11 | 国立研究開発法人産業技術総合研究所 | Liquid-liquid extraction method and equipment using high-pressure carbon dioxide using a micromixer |
CN111921228B (en) * | 2020-07-29 | 2022-05-17 | 邹林宏 | Ultrasonic reinforced supercritical fluid extraction method |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB769454A (en) * | 1953-08-24 | 1957-03-06 | Herbert Peter August Groll | Fractionation of oils or other soluble mixtures of organic substances by selective extraction |
US4770780A (en) * | 1984-04-25 | 1988-09-13 | Cf Systems Corporation | Liquid CO2 /cosolvent extraction |
JPS61268762A (en) * | 1985-05-24 | 1986-11-28 | Mitsubishi Kakoki Kaisha Ltd | Concentration of naturally-occurring dyestuff |
DE3810681A1 (en) * | 1988-03-29 | 1989-10-12 | Udo Kienle | METHOD FOR PRODUCING A NATURAL SWEETENER BASED ON STEVIA REBAUDIANA AND ITS USE |
DE4306303C2 (en) * | 1993-03-01 | 1996-08-08 | Barth Raiser Hopfenextraktion | Process for extracting vegetable oils |
DE4335321C2 (en) * | 1993-10-15 | 1996-08-01 | Joachim Brimmer Ingenieurbuero | Process for extracting coffee oil containing aroma components |
EP0942773B1 (en) * | 1996-12-06 | 2003-07-02 | Advanced Phytonics Limited | Materials treatment |
CN1280025A (en) * | 2000-08-14 | 2001-01-17 | 孙传经 | Multifunctional-supercritical CO2 extraction technology |
US6589422B2 (en) * | 2000-12-18 | 2003-07-08 | Ineos Fluor Holdings Limited | Apparatus and method for extracting biomass |
AT411429B (en) * | 2002-08-26 | 2004-01-26 | Natex Prozesstech Gmbh | Extraction of impurities from thinly-coated fluid film involves treating its surface with liquid carbon dioxide whilst continuously replenishing film thickness |
DE102005026424A1 (en) * | 2005-06-08 | 2006-12-14 | Terra Nostra Produkte Mit Naturextrakten Gmbh | Process for the preparation of a margosa extract |
US20080260852A1 (en) * | 2007-01-23 | 2008-10-23 | Ferro Pfanstiehl Laboratories, Inc. | Supercritical fluid extraction produced by in-line homogenization |
-
2013
- 2013-02-07 AT ATA101/2013A patent/AT513907B1/en active
-
2014
- 2014-01-14 EP EP14705694.9A patent/EP2953699A1/en not_active Withdrawn
- 2014-01-14 MX MX2015010196A patent/MX2015010196A/en unknown
- 2014-01-14 WO PCT/AT2014/000006 patent/WO2014121311A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
AT513907A1 (en) | 2014-08-15 |
WO2014121311A1 (en) | 2014-08-14 |
EP2953699A1 (en) | 2015-12-16 |
AT513907B1 (en) | 2015-01-15 |
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