2. The use of Supercritical Fluid Extraction Technology in Food Processing
3. Permeatıon Of Supercrıtıcal Carbon Dıoxıde Across Polymerıc Hollow Fıber Membranes
4. Regeneratıon Of Gac-F400 By Scco2: Effect Of System Condıtıons On Desorptıon Studıes
4. 1. The operation rig
4. 2. Adsorption studies
4. 3. Solubility studies
4. 4. Desorption Studies:
4. 4. 1. The rate of desorption
4. 5. The effect of temperature and pressure
4. 6. The effect of SCF flow rate
4. 7. The effect of initial carbon loading
5. Separatıon Of Flurbıprofen And Ibuprofen Enantıomers On A Chıral Statıonary Phase Usıng Supercrıtıcal Fluıds
5. 1. Effect of temperature and pressure using isopropanol as a modifier
5. 2. Effect of various solvents as modifier
5. 3. Effect of Modifier Content v/v % on Peak Resolution and Separation Factor in SFC
6. Supercrıtıcal Fluıd Chromatography As Successful Separatıon Tool In Chemıcal And Pharmaceutıcal Industry
7. Contınuous Supercrıtıcal Extractıon Of Solıds In An Extruder
8. Purıfıcatıon Of Isocyanates By Supercrıtıcal Fluıd Fractıonatıon Usıng Carbon Dıoxıde And Carbon Dıoxıde-Propane Mıxtures
8. 1. Separational analysis
8. 1. Separational analysis
8. 2. Counter-current experiments
9. Cfd Sımulatıon Of Partıcle-To-Fluıd Heat Transfer Under Supercrıtıcal Condıtıons: Prelımınary Results
9. 1. Geometrical model
9. 2. Mesh design and cfd modeling
9. 3. Model analysis
9. 3. 1. Velocity profiles
9. 3. 2. Temperature profiles
9. 3. 3. Transport properties estimation
10. Flow Velocıtıes Of Supercrıtıcal Carbon Dıoxıde Under Condıtıons Of Natural Convectıon
10. 1. External heater
10. 2. Internal heater
11. Mathematıcal Modelıng And Optımızatıon Of Technologıcal Schemes For Oxıdatıon Of Organıcs In Supercrıtıcal Water
11. 1. Chemical reactions proceeded in the system
11. 2. Thermodynamic calculations
12. Solıd Bed Propertıes In Supercrıtıcal Processıng
12. 1. Mechanical compaction
12. 2. Permeability
12. 3. Radial to axial pressure ratio, pressure propagation
12. 4. Modelling
13. Purıfıcatıon Of The Synthesıs Product Of Salıcylıc Acıd By Means Of Supercrıtıcal Carbon Dıoxıde
14. Supercrıtıcal Fluıd Extractıon And Fractıonatıon Of Essentıal Oıls And Related Products
15. Productıon Of Reference Soıls For Ecotoxıcologıcal Fıeld Studıes Usıng Supercrıtıcal Co2-Extractıon.
15. 1. Extraction efficiency
16. Heat Transfer And Hydrodynamıcs In Supercrıtıcal Carbon Dıoxıde
17. Supercritical Fluid Extraction Of Natural Products
17. 1. SFE of Essential Oils
17. 2. SFE of Black Pepper Essential Oil
17. 2. 2. Extended Lack’s Plug Flow Model
17. 2. 3. Mass balance and boundary conditions
17. 2. 4. Model with analytical solution
17. 2. 5. Analytical assumptions
17. 2. 6. Nomenclature
18. Solute-Solute And Solute-Matrıx Interactıons In The Supercrıtıcal Fluıd Extractıon From Plants
18. 1. Equilibrium Relationship
18. 2. Extraction Of Oleoresin
18. 3. Extraction of minor low-polar compounds
18. 4. Extraction of minor polar compounds
19. The Modellıng Of Fractıonatıon Of Frıed Oıl Wıth Supercrıtıcal Carbon Dıoxıde: A Fırst Step
20. Supercrıtıcal Fluıds As Envıronmentally Benıgn Solvents For The Chemıcal Industry
21. Is It Possıble To Enhance The Dıssolutıon Rate Of Poorly-Soluble Actıve Ingredıents By Supercrıtıcal Fluıd Processes ?
21. 1. Supercritical Fluid particle design
21. 2. Dissolution of SCF-micronized neat particles
21. 2. 1. Experimental issues:
21. 3. Dissolution of composite particles
21. 3. 1. SCF formulation
22. Productıon Of Mıcro-Partıcles Wıth Sc-Co2: Comparıson Of Pca And Gas Precıpıtatıon Technıques For Dıfferent Pharmaceutıcal Compounds
23. A Supercrıtıcal Process To Produce Cocoa Butter And Chocolate Partıcles For The Seedıng Of Chocolate
23. 1. Experimental apparatus
23. 2. Chocolate particle generation
24. Controlled Precıpıtatıon Of Actıve Pharmaceutıcal Ingredıents Employıng Supercrıtıcal Fluıds: Scale-Up Consıderatıons
25. Applıcatıon Of Supercrıtıcal Carbon Dıoxıde In The Preparatıon Of Bıodegradable Polylactıde Membranes
26. Semı-Batch Fractıonatıon Of Fatty Acıds Ethyl Esters By Means Of Supercrıtıcal Carbon Dıoxıde
26. 1. Modellization
27. Supercrıtıcal Co2-Extractıon Of Fatty Compounds Out Of Bıotechnologıcal Products
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28. 1. GC-MS analysis
29. Antıoxıdant Actıvıty Of Orıganum Majorana L. Herb And Extracts Obtaıned By Supercrıtıcal Co2 Extractıon
30. Lycopene Extractıon From Processed Tomatoes Usıng Supercrıtıcal Co2
31. Supercrıtıcal Carbon Dıoxıde Extractıon Of Glycyrrhızın From Lıcorıce Root
32. Supercrıtıcal Carbon Dıoxıde Fluıd Extractıon Of Seed Oıl For Hıppophae Rhamnoıdes L.
32. 1. Effect of Particle sizes
33. Effect Of Sample Preparatıon Method On Supercrıtıcal Fluıd Extractıon For Essentıal Oıls From Bıtter Orange (Var.Amara)
34. Alkylresorcınols Extracted From Rye Seeds By Supercrıtıcal Carbon Dıoxıde
35. Supercrıtıcal Fluıd Extractıon Of Lıpıd Compounds From Heather (Calluna Vulgarıs).
36. Supercrıtıcal Fluıd Extractıon Of Lıpophılıc Extractıves From Wheat Straw Trıtıcum Aestıvum
37. Kınetıcs Of Supercrıtıcal Fluıd Extractıon Of Oıl From Mıcroalga Nannochloropsis Sp
38. The Technology Of Extractıng Essence Oıl From The Purple Perılla Seeds By Supercrıtıcal Fluıds
39. Supercrıtıcal Fluıd Extractıon Of Antıoxıdants From Pepper (Capsicum Annuum L.)
39.1. Extraction of carotenoids
39. 2. Extraction of polyphenols
40. Supercrıtıcal Co2 Extractıon Of Turkısh Mountaın Tea (Sideritis arguta Boiss.et Heldr.)
40. 1. Supercritical CO2 extraction aparatus
41. Supercrıtıcal Fluıd Extractıon Of Mıcroalgae Spırulına Platensıs. Chemo-Functıonal Characterızatıon
42. Supercrıtıcal Fluıd Extractıon Of Carotenoıds From Tomato Industrıal Wastes
43. Extractıon Of Oıl Enrıched In A-Tocopherol From Grape Seeds (Vıtıs Vınıfera) Usıng Supercrıtıcal Carbon Dıoxıde
44. Identıfıcatıon And Removal Of Offflavors From Tuna Fısh Oıl Wıth Supercrıtıcal Co2
45. Upgradıng And Valorısatıon Of Food Wastes By Supercrıtıcal Carbon Dıoxıde Extractıo




As the development of the natural medicine, the glycyrrhizin extracted from the licorice root was found to have potential therapeutic value in the treatment of several diseases, especially available for anti-SARS virus. Therefore, an optimal method to extract and refine the glycyrrhizin can be found. In that case, the extraction of glycyrrhizin by means of organic solvents and supercritical carbon dioxide (SC-CO2) was investigated. The extraction of glycyrrhizin from licorice root with supercritical carbon dioxide was also compared with conventional extraction methods. Those methods include the extraction at room temperature (ERT), the traditional Soxhlet extraction, and the heat reflux extraction. The results show that the yield obtained by SC-CO2 extraction was similar to that obtained by conventional solvent extraction. But the quality of the production extracted by SC-CO2 was better than that of the production extracted by other methods. Subsequently, HPLC was used to analyze the chemical compositions of these productions.

Licorice is herbaceous triennial or perennial plant, with large roots. The roots and the stalks are used extensively fields, tobacco, food, flavoring, confectionery, perfumes, pharmaceutical industry, etc. Particularly in medicine licorice has a lot of virtue. Glycyrrhiza radix has been used as a Chinese traditional medicine for over 1000 years. It was used to relieve a cough, reduce phlegm, detoxifcation. At present, the medicine is frequently used to treat diseases such as contagious hepatitis, bronchitic asthma, canker, ague, antivirus, and improve immunity. Especially, glycyrrhizic acid was found to have the ability to restain HIV reproduce in 1980s. Subsequently, the flavonoids were also found to have this function. Glycyrrhizin, which is also called glycyrrhizic acid, could be used treatment for sudden acute respiratory syndrome (SARS). Glycyrrhizin may protect the target cell from the SARS virus to attach to and invade. It also hinders virus reproductions and spread from one cell to another cell. As the development of the medicine, the demand of glycyrrhizin, flavonoids and other availability enlarge widely. The application of supercritical fluid extraction (SFE), particularly the use of liquid and supercritical carbon dioxide, has received much attention in Glycyrrhiza radix extraction in the last few years. This separation technique offers extraction yields comparable with those obtained by conventional extraction methods using organic solvent, followed by column separation and purification, to obtain pure compounds. The conventional extraction consumed large amounts of solvent, required lots of time, and polluted the environment. Since carbon dioxide has some advantages: chemically inert, nontoxicity, nonflammable, no pollution problem, and shorter concentration time. These advantages attract the researchers’ interest in using supercritical carbon dioxide to extract Glycyrrhiza radix. For the extraction of polar or ionic compounds, organic solvents have been added as the cosolvent to increase the compounds’ solubility in SC-CO2. The extractions, which have been used extensively, have three components: glycyrrhizin, flavonoids, amylose. There are many methods to extract glycyrrhiza radix, such as traditional extraction, heat reflux extraction, ultrasonic extraction, microwave-assisted extraction, SC-CO2 extraction. These extraction methods have been compared.

SC-CO2 technology have been used to plant extract widely. SC-CO2 extraction was a very suitable method for licorice. Briefly, sample was accurately weighed, then extracted by the following methods. The pulverized sample was packed into a sample cartridge.

It is important that extraction pressure is one of the most parameters. Different material has different condition, which is been determinate by the polar of the material. Nonpolar material is extracted at lower pressure, but polar is extracted at higher pressure. Since glycyrrhizic acid and flavonoids are all polar materials, the experiment’s pressure is selected at higher pressure. Temperature is another important parameters. The effect of temperature is very complex. At a certain pressure, if the temperature is been enhanced the molecular distance is increased and the affects among the molecules are decreased which cause the solubility reduced. Another aspect, enhanced the temperature can cause the vapor pressure of the extraction increase and increase the combine between molecules, so the solubility increased. However, high temperature can make the production quality decrease. So the whole experiment at lower temperature.

The cosolvent is added in this experiment to increase the solubility of glycyrrhizin and flavonoids in SC-CO2. Because SC-CO2 is a nopolar solvent, so it makes glycyrrhizin and flavonoids hard to dissolve in it. The ethanol as cosolvent is added into SC-CO2 in order to increase the solubility of glycyrrhizin and flavonoids.

Fig. 63 Effect of ethanol concentration on the yield

Milling of the raw materials greatly improves the extraction efficiency. The smaller particle size should gain the greater yield. But too small particle size may be increase the flow resistance.

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