Water
372℃, 221bar
Propane
97℃ , 42.5bar
Butane
152℃ , 38bar
Carbon dioxide
31℃ , 74bar
Ammonia
133℃ , 11bar
Ethanol
241℃ , 61bar
Supercritical
condition
depending
on solvent
Supercritical carbon dioxide system has application of extraction, drying, making nanoparticle, expansion, de-binding, etc.
SUPERCRITICAL CARBON DIOXIDE SYSTEM
Critical Point
Pressure
Temperature
Supercritical Fluid
Solid Phase
Liquid Phase
Gaseous Phase
Coexistence with
gas and liquid
Supercritical Fluid
increasing wake-density
decreasing liquefied-density
Low
temperature
Inflammable gas
Non-toxic
Separation
Supercritical
carbon
dioxide
H
N
Conventional
LC
Supercritical CO2
LC
0 0 2.5 5 7.5 10 12.5 15 17.5 min20 40 60 80 100 120
Minutes
OCH2-CHCH2NHCH(CH3)2
OH
pindolol
Water,
methanol,
LiCI solution
CO2 cylinder CO2 pump Thermostat bath Back-pressure
controller
Resin packed column
Cyclona separator
Fraction collector
Solvent
pump
Textile
Textile SCF Dyer Textile
Wet dyer Rinsing Drying Product
Dry Additive
Water
Liquid
SCF Dyeing Process
Conventional Wet Dyeing Process
Gas
SCF
Colored Wasterwater
No Wastewater
Wastewater Heat, Air Pollutant
Water Air Energy
Productant
Supercritical Flud Chromatography
Supercritical Foam
Ref. Korea Patent No. 10-0719487
Gas
injection
Two
system
Two-phase
polymer/CO2
Single-phase
polymer/CO2 solution
Foam Composite
Mixing,
Diffusion
Thermal dynamic
instability
Polypropylene
Rapid Pressure Drop
20
Intensity(arb.unit)
2θ (degree)
40 60 80
CeO2
(111)
(200)
(220)
(311)
(222)
(400)
(301)
(420)
CO2 Cylinder
Pump PumpHeater Nozzle
Vessel
Filtering Vessel
CO2 Gas
Solution
Synthesis of Nanoparticles
40
30
20
10
0
0 50 100
Time(min)
ExtractionRate(%)
150 200 250
500 bar
400 bar
300 bar
200 bar
Raw material
Grinding Supercritical
CO2 extraction
Before extraction After extraction
R1COOCH2
R2COOCH
R3COOCH2
Supercritical process
350℃, 400atm, few min
Alkall catalyst process
65℃, 1.5atm, few hours
No byproducts
No washing
No drying
Methyl EsterMethanol
Saponification reaction
Glycerin
3CH3OH
Water
R1COOCH3
R2COOCH3
R3COOCH3
CH2OH
CHOH
CH2OH
+ +
Wastewater
Soap
Methylesters(%)
Methylesters(%)
Water content(%) Free fatty acids content(%)
100
80
60
40
20
0
100
80
60
40
20
0
0 0 10 20 30 4002 4 6
Supercritical Process Supercritical Process
Alkaline-catalyzed
Alkaline-catalyzed
Alkaline-catalyzedAcid-catalyzed
Extraction & Degreasing (Corn Embryo)
Synthesis of Biodiesel (Supercritical MeOH)
Supercritical Fluid Dyeing
255,Techno 2-ro,Yuseong-gu, Daejeon, Korea (Daedeok techno valley) Tel: +82-42-931-6100 Fax: +82-42-935-6103 Homepage: www.suflux.com E-mail: webmaster@suflux.com

Supercritical carbon dioxide system Inforgraphic

  • 1.
    Water 372℃, 221bar Propane 97℃ ,42.5bar Butane 152℃ , 38bar Carbon dioxide 31℃ , 74bar Ammonia 133℃ , 11bar Ethanol 241℃ , 61bar Supercritical condition depending on solvent Supercritical carbon dioxide system has application of extraction, drying, making nanoparticle, expansion, de-binding, etc. SUPERCRITICAL CARBON DIOXIDE SYSTEM Critical Point Pressure Temperature Supercritical Fluid Solid Phase Liquid Phase Gaseous Phase Coexistence with gas and liquid Supercritical Fluid increasing wake-density decreasing liquefied-density Low temperature Inflammable gas Non-toxic Separation Supercritical carbon dioxide H N Conventional LC Supercritical CO2 LC 0 0 2.5 5 7.5 10 12.5 15 17.5 min20 40 60 80 100 120 Minutes OCH2-CHCH2NHCH(CH3)2 OH pindolol Water, methanol, LiCI solution CO2 cylinder CO2 pump Thermostat bath Back-pressure controller Resin packed column Cyclona separator Fraction collector Solvent pump Textile Textile SCF Dyer Textile Wet dyer Rinsing Drying Product Dry Additive Water Liquid SCF Dyeing Process Conventional Wet Dyeing Process Gas SCF Colored Wasterwater No Wastewater Wastewater Heat, Air Pollutant Water Air Energy Productant Supercritical Flud Chromatography Supercritical Foam Ref. Korea Patent No. 10-0719487 Gas injection Two system Two-phase polymer/CO2 Single-phase polymer/CO2 solution Foam Composite Mixing, Diffusion Thermal dynamic instability Polypropylene Rapid Pressure Drop 20 Intensity(arb.unit) 2θ (degree) 40 60 80 CeO2 (111) (200) (220) (311) (222) (400) (301) (420) CO2 Cylinder Pump PumpHeater Nozzle Vessel Filtering Vessel CO2 Gas Solution Synthesis of Nanoparticles 40 30 20 10 0 0 50 100 Time(min) ExtractionRate(%) 150 200 250 500 bar 400 bar 300 bar 200 bar Raw material Grinding Supercritical CO2 extraction Before extraction After extraction R1COOCH2 R2COOCH R3COOCH2 Supercritical process 350℃, 400atm, few min Alkall catalyst process 65℃, 1.5atm, few hours No byproducts No washing No drying Methyl EsterMethanol Saponification reaction Glycerin 3CH3OH Water R1COOCH3 R2COOCH3 R3COOCH3 CH2OH CHOH CH2OH + + Wastewater Soap Methylesters(%) Methylesters(%) Water content(%) Free fatty acids content(%) 100 80 60 40 20 0 100 80 60 40 20 0 0 0 10 20 30 4002 4 6 Supercritical Process Supercritical Process Alkaline-catalyzed Alkaline-catalyzed Alkaline-catalyzedAcid-catalyzed Extraction & Degreasing (Corn Embryo) Synthesis of Biodiesel (Supercritical MeOH) Supercritical Fluid Dyeing 255,Techno 2-ro,Yuseong-gu, Daejeon, Korea (Daedeok techno valley) Tel: +82-42-931-6100 Fax: +82-42-935-6103 Homepage: www.suflux.com E-mail: webmaster@suflux.com