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
Home Page
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




There is an increasing public awareness of the health, environment and safety hazards associated with the use of organic solvents in food processing and the possible solvent contamination of the final products. The high cost of organic solvents and the increasingly stringent environmental regulations together with the new requirements of the medical and food industries for ultra-pure and high added value products have pointed out the need for the development of new and clean technologies for the processing of food products. Supercritical fluid extraction using carbon dioxide as a solvent has provided an excellent alternative to the use of chemical solvents. Over the past three decades, supercritical CO2 has been used for the extraction and isolation of valuable compounds from natural products.

Supercritical CO2 was found to be selective in the separation of desired compounds without leaving toxic residues in extracts and without the risk of thermal degradation of processed products. Through the exploitation of the solvating power acquired by fluids near their critical points and the sensitivity of this power to small perturbations in temperature, pressure and modification of the solvent with the addition of entrainers, solvent-free extracts were readily obtained due principally to the high volatility of these solvents at ambient conditions. The favorable transport properties of fluids near their critical points also allows deeper penetration into solid plant matrix and more efficient and faster extraction than with conventional organic solvents.

For the past three decades, the commercial application of supercritical fluid technology remained restricted to few products due to high investment costs and for being new and unfamiliar operation. With advances in process, equipment and product design and realization of the potentially profitable opportunities in the production of high added value products, industries are becoming more and more interested in supercritical fluid technology. The extraction is carried out in high-pressure equipment in batch (Figure 1) or continuous manner (Figure 2). In both cases, the supercritical solvent is put in contact with the material from which a desirable product is to be separated.

Figure 1: A schematic diagram of a supercritical fluid batch extraction.

Figure 2: A schematic diagram of a supercritical fluid continuous extraction.

Figure 3: A schematic diagram of the Rapid Expansion of Supercritical Solutions (RESS) process.

Figure 4: A schematic diagram of the Solvent or Gas Anti-Solvent process.

Figure 5: A schematic diagram of Particle from Saturated Solutions process.

The supercritical solvent, now saturated with the extracted product, is expanded to atmospheric conditions and the solubilized product is recovered in the separation vessel permiting the recycle of the supercritical solvent for further use. Table 1 presents some of the existing commercial applications put in operation over the past few years. Supercritical fluid technology is now recognized as an effective analytical technique with favorable and comparable efficiencies to existing chemical analysis methods and when applied for the qualitative and quantitative identification of constituents of naturally occurring products and heat-labile compounds. In addition, the reduction of liquid solvent waste and the substitution of some undesirable organic substances is another advantage of supercritical fluid analytical techniques.

Table 1: Industrial Applications

Extraction with supercritical fluids is also a unit operation that could be employed for a variety of applications including the extraction and fractionation of edible fats and oils, purification of solid matrices, separation of tocopherols and other antioxidants, clean-up of herb medicines and food products from pesticides, detoxification of shellfish and concentration of fermentation broth, fruit juices, among others.

Supercritical fluid extraction has proved effective in the separation of essential oils and its derivatives for use in the food, cosmetics, pharmaceutical and other related industries, producing high-quality essential oils with commercially more satisfactory compositions (lower monoterpenes) than obtained with conventional hydro-distillation.

Alkaloids, organic compounds with bitter taste and toxic effects on animals and humans, but present therapeutic effects when applied in moderate doses, are found in many natural plants. Alkaloids such as caffeine, morphine, emetine, pilocarpine, among others, are the active components in a variety of stimulants and medicinal products and their recovery from natural plants is of great interest to the food, pharmaceutical, and cosmetic industries. Supercritical Carbon dioxide proved to be highly selective for caffeine prompting its use as the selected solvent in the commercial decaffeination of coffee and black tea. Recent investigations have demonstrated the potential exploration of solvent and anti-solvent properties of carbon dioxide in the recovery of alkaloids such as theophylline, theobromine and pilocarpine, among others.

The association of high blood cholesterol levels with heart diseases or cancer is the motivating factor in recent works on the reduction of cholesterol levels in consumed meals that include meats, dairy products and eggs. Several methods including supercritical extraction have been proposed for the reduction of fat and cholesterol content in dairy products. Cholesterol was shown to be soluble in supercritical carbon dioxide and even more soluble in supercritical ethane. Extraction with supercritical fluids requires higher investment but can be highly selective and more suitable for food products.

A summary of the main products containing cholesterol and their extraction with supercritical fluids is presented in Table 2. These results clearly indicate the great potential of supercritical fluid extraction in the recovery of meat products with acceptable cholesterol and fat contents. As ethane is much more expensive than CO2, the use of CO2/ethane and CO2/propane mixtures can be an attractive alternative for the removal of cholesterol from foods due to the compromise between higher ethane cost and better cholesterol removal efficiency. Cholesterol removal was also improved through the coupling of carbon dioxide extraction with an adsorption process operating at the same extraction conditions. Literature data also point to potential fractionation of fat simultaneously with the removal of cholesterol from dairy products. The extraction/fractionation operation was also coupled with an adsorption step that uses alumina as the adsorbent.

The combined extraction/adsorption operation resulted in the removal of more than 97% of the cholesterol in the original butter oil (Table 2). The operation has also resulted in the generation of butter oil fractions with characteristic properties that are distinctly different from those of the original oil.

Table 2: Supercritical fluid extraction of cholesterol with CO2 from products of animal

origin.

The carbon dioxide extraction has also proved effective for the production of high quality cocoa butter from cocoa beans. Recent investigation point to the potential use of supercritical CO2 for microbial inactivation of foods and the implementation of an innovative technique for the sterilization of thermally and pressuresensitive materials.

Supercritical water oxidation, an environmentally attractive technology through which organic materials can be oxidized to carbon dioxide, water and gaseous nitrogen, is one of the new potential applications of supercritical fluid technology. In analytical applications, it has the advantage over standard methods in providing consistent qualitative and quantitative analysis and the simultaneous oxidative decomposition of the material. In addition to the homogenization of the reaction mixture, high oxygen concentrations are attained in supercritical water. The application of supercritical water for the safe destruction of toxic materials is a viable alternative to incineration and land disposal.

The rapid expansion of supercritical solutions through small size orifices and nozzles has opened new opportunities for the formation of finely divided powders. This process has been applied for the formulation of drug particles, drug-containing polymeric particles and solute-containing liposomes. The ability of supercritical mixtures to fractionate polymers contributes to the beter control of drug release in formed polymeric delivery systems.

Supercritical or gas anti-solvent precipitation were proposed in the 1980s as a promising technology for the production of micron and submicron size particles with controlled particle size and particle size distribution. The principal features of this process is the use of supercritical carbon dioxide, the mild operating temperatures and the smaller particles (sizes down to 50 nm, 1-1.5µm and 0,1-20µm, have been reported for some operations) obtained with this process as compared to conventional milling and crystallization via liquid antisolvent precipitation. While particle morphologies that include spheres, rod-like and snowballs have been reported, the most commonly encountered is the formation of spherical particles. Supercritical CO2 was used for protein purification through the fractional precipitation of proteinalkaline phosphatase, insulin, lysozyme, ribonuclease, trypsin and their mixtures from dimethylsulphoxide. Other investigations focused on coatings, semi-conductors and pharmaceuticals. More recently this technique has been employed for the encapsulation of micron size particles and the selective precipitation of products from reaction media. Variations of this process include the aerosol solvent extraction system (ASES), which involves spraying the solution through an atomizing nozzle as fine droplets into supercritical carbon dioxide. The dissolution of carbon dioxide in the liquid droplets leads to large volume expansion of the liquid and consequently the reduction of the dissolution power of this liquid and the existence of large supersaturations and thereby the formation of small solute particles.

Another variation is the solution-enhanced dispersion by supercritical fluids. In this process, the supercritical fluid is first mixed with the solution and it is the mixture that is subsequently sprayed into a vessel controlled at the operating temperature and pressure and where particle formation takes place. Droplets formed are generally smaller than in the ASES with enhanced mixing between the supercritical fluid and the solution.

The Particles from gas-saturated solutions involves the dissolution of supercritical carbon dioxide in melted or liquid-suspended substance and thereby generating the denominated gas-saturated solution or suspension, which is subsequently expanded through an orifice or a nozzle to produce the desired fine solid particles or droplets. This process allows the formation of particles of substances insoluble in supercritical carbon dioxide.

Finally it is important to mention that supercritical fluids are known to provide good reaction media due to their capacity to homogenize a reaction mixture, high diffusivity and controlled phase separations and distribution of products.

In the following sections, several application areas of supercritical fluid extraction (SFE) is given abour variety of industrial areas.

Designed and Programmed ELECSUS