• Title/Summary/Keyword: $CO_2$ solubility

Search Result 361, Processing Time 0.028 seconds

Continuous Cocurrent Extraction of Milk Fat by Supercritical Carbon Dioxide (초임계이산화탄소에 의한 유지방의 연속 병류식 추출)

  • Lim, Sang-Bin;Syed S.H.Rizvi
    • Journal of the Korean Society of Food Science and Nutrition
    • /
    • v.23 no.3
    • /
    • pp.459-465
    • /
    • 1994
  • Performance of a continuous cocurrent supercritical fluid extraction column for processing of anhydrous milk fat (AMF) was determined. The extract loading increased and the extraction yield decreased as the superficial velocity of AMF increased. The maximum solubility of AMF in $CO_2$ at 4$0^{\circ}C$/3,500 psig was 0.0195g/g. The increase of the carbon dioxide density enhanced the solubility of milk fat and decreased the cholesterol concentration in the extract. Three operation conditions, such as recycle , reflux, and temperature gradient of extraction column, were tested. More short-chain fatty acvids were extracted by the reflux operation . Longchain fatty acids and thehighest ratio fo long-chain unsaturated to saturated fatty acids were also obtained in the raffinate phase with refluex.

  • PDF

Effect of Fe Doping on Thermoelectric Properties of Mechanically Alloyed $CoSb_3$

  • Ur, Soon-Chul;Kwon, Joon-Chul;Kim, Il-Ho
    • Proceedings of the Korean Powder Metallurgy Institute Conference
    • /
    • 2006.09b
    • /
    • pp.957-958
    • /
    • 2006
  • Fe doped skutterudite $CoSb_3$ with a nominal composition of $Fe_xCo_{1-x}Sb_{12}(0{\leq}x{\leq}2.5)$ have been synthesized by mechanical alloying (MA) of elemental powders, followed by vacuum hot pressing. Phase transformations during mechanical alloying and vacuum hot pressing were systematically investigated using XRD. Single phase skutterudite was successfully produced by vacuum hot pressing using as-milled powders without subsequent annealing. However, second phase of $FeSb_2$ was found to exist in case of $x\geq2$, suggesting the solubility limit of Fe with Co in this system. Thermoelectric properties as functions of temperature and Fe contents were evaluated for the hot pressed specimens. Fe doping up to x=1.5 with Co in $Fe_xCo_{4-x}Sb_{12}$ appeared to increase thermoelectric figure of merit (ZT) and the maximum ZT was found to be 0.78 at 525K in this study.

  • PDF

Characteristics of iron powder formulation produced from porcine blood by enzymatic treatment (효소 처리한 돈혈 활용 철분분말제제 특성)

  • Kim, Mi-Yeon;Kim, MinA;Jeong, Yong-Jin
    • Food Science and Preservation
    • /
    • v.23 no.5
    • /
    • pp.753-757
    • /
    • 2016
  • In this study, enzyme (thermoase) hydrolysis was applied to the porcine blood order to increase the iron content and solubility. It was confirmed that content of iron was increase up to 158.11 mg/100 g porcine powders after 0.2% thermoase treatment at $60^{\circ}C$ during 4 hr. The solubility of porcine blood powders was higher than other enzyme (various protease), temperature, reaction time. This optimized conditions were also worked to the in vitro iron bioavailability rate increasement, the bioavailability of hydolyzed porcine powders was 3-fold higher than that of an iron supplement on the market. These results indicate the possibility of porcine blood powder in iron supplements market as natural material. Also utilizing of reduced porcine blood will be possible to improve environmental issues.

Supercritical CO2 Dyeing and Finishing Technology - A Review (초임계 이산화탄소 염색 및 가공 기술)

  • Lee, Gyoyoung;Chae, Juwon;Lee, Sang Oh;Kim, Sam Soo;Lee, Jaewoong
    • Textile Coloration and Finishing
    • /
    • v.31 no.1
    • /
    • pp.48-64
    • /
    • 2019
  • With evolution in the production environment of the textile industry, the need for non-water-based dyeing technologies and eco-friendly process facilities in the dyeing and processing stages has increased. In recent years, supercritical fluid dyes have been developed and commercialized in Europe, centering on this demand. However, so far, such dyes have been mainly applied in the processing of PET fibers. Basic research has mainly involved investigation of dyeing by supercritical carbon dioxide or solubility of such dyes, and more in-depth research should be continuously carried out. In this review, we describe the types and characteristics of supercritical fluids that exhibit specific properties at pressures and temperatures over the critical point. In addition, the state of the art in the dyeing and processing technology using supercritical fluids and associated, processing problems, environmental regulation, and wastewater treatment issues are described in detail. We hope this review can contribute to the supercritical fluid technology being further developed as an environment friendly dyeing processing method. Furthermore, we expect that the technique can be used as a means of ensuring different, high-quality dyed products.

Gas-Transport Properties through Various Cations Exchanged Sulfonated Poly(ether imide) Membranes

  • Rhim, Ji-Won
    • Korean Membrane Journal
    • /
    • v.3 no.1
    • /
    • pp.51-58
    • /
    • 2001
  • The surface of Poly(ether imide) (PEI) membranes has been sulfonated using CIS03H. The resulting membranes were characterized through the analysis of ESCA and contact angle measurements The sulfonated PEI membranes were exposed to gases of $O_2$, $N_2$, and $CO_2$ to measure the permeation rates and ideal separation factors. In addition, the diffusivities and solubilities of individual gases were measured. The diffusivity effect is more dominant than the solubility one on gas transports.

  • PDF

Selective Leaching of $LiCoO_2$in an Oxalic Acid Solution (Oxalic acid용액에서 $LiCoO_2$의 선택침출)

  • 이철경;양동효;김낙형
    • Resources Recycling
    • /
    • v.11 no.3
    • /
    • pp.10-16
    • /
    • 2002
  • In the leaching of $LiCoO_2$with a strong acid such as sulfuric and nitric acid, an additional step was needed to recover cobalt and lithium separately from spent lithium ion batteries (LIBs). The leaching of $LiCoO_2$in an oxalic acid solution was investigated to recover cobalt selectively using a low solubility of cobalt oxalate at low pH. Leaching efficiency of 95% of lithium and less than 1% of cobalt were obtained when pure $LiCoO_2$powder was leached in 3M oxalic acid at $80^{\circ}C$ and 50 g/L pulpdensity. Under the above leaching conditions, complete dissolution of lithium was accomplished with mere 0.25% of cobalt in the solution when the cathodic active material collected from spent LIBs was employed. The lithium in the leaching solution can be recovered as a form of carbonate or hydroxide depending on the addition of $Na_2$$CO_3$or LiOH.

Relationship of Hardness Components in Filature Water with Reelability Aid Reagent (제사용수의 경도성분과 해서촉진제와의 관계)

  • 최병희;이용우
    • Journal of Sericultural and Entomological Science
    • /
    • v.13 no.1
    • /
    • pp.49-59
    • /
    • 1971
  • This experiment was conducted, how making use of "Seracol 100", a kind of nonionic surface active reagent, during cocoon cooking and silk reeling process which is mainly used in Korea and developed by one of the authors since 1965. Main purpose of the experiment is to investigate the influence of the activity of the reelability aid reagent on various degree of hardness component and various salts which are contained in filature water being used by silk factories now. Specifically, it was tried to determine the effects of the reelability aid reagent added to each sample water of artificially differentiated the degree of hardness component upon sericin solubility. Some of the major findings are summarized as follows. 1. "Seracol 100", with below 5$^{\circ}$dH water, increased sericin solubility in each sample water, but above $10^{\circ}$dH the effect of it shows a significant relationship with the different degree of hardness component. Besides the component (MgCO$_3$)$_4$ㆍMg(OH)$_2$, generally, the higher the degree of hardness in the water, the less the amount of desolved sericin in the water showed. There is little or no difference between 1000 times diluted "Seracol 100" water and 2000 times diluted "Seracol 100" water in terms of sericin solubility. 2. The different kind of degree of hardness component shows a significant relationship with sericin solubility, In case use of "Seracol 100", Mg hardness component affected on the sericin solubility more than Ca hardness. But in the control, contrary to this, that is Ca hardness component did more than Mg hardness, 3. The different kind of salts in degree of hardness component show a significant relationship with sericin solubility. In the control water, nitrate is the greatest among salts affecting on sericin solubility, next chloride and sulfate are in order. In case of "Seracol 100" water, chloride is the least among salts, below $10^{\circ}$dH, next sulfate and nitrate are in order, and above 15$^{\circ}$dH, next nitrate and sulfate are in order. 4. In case of "Seracol 100" water, the more contained heavy metal salts (Fe, Al, Cu, Mn) in the water, the less sericin solubility showed. It is found that there is little or no difference among other salts in terms of sericin solubility. But alkaline metal salt remarkably increased sericin solubility. 5. In case of "Seracol 100" water, tinting of the water was affected by Ca salts more than by Mg salts. Among other salts, only Al and Fe affected on the tinting of the water, specifically, in view of the fact that "Seracol 100" water increase the tinting of Fe salt water, but decrease the tinting of raw silk. It is thought that "Seracol 100" deter Fe$^{+2}$ from absorbing to raw silk by deteriorating the activity of Fe$^{+2}$ . 6. "Seracol 100" have the effect on osmosis of the water, After treatment until 2hrs the osmosis of 1000 times diluted "Seracol 100" water is the greatest, next orders are 2000 times diluted "Seracol 100" and control. From 2 hrs to 6 hrs the osmosis of 2000 times diluted water is the greatest, next orders are 1000 times diluted water and control. After 6 hrs the osmosis of the water is the same order as above. 7. In view of tile fact that "Seracol 100" have the effect to control the degree of hardness during the treatment of cocoon layer in the water, it is thought that, in varying degree of hardness in the water, there is a significant relationship between "Seracol 100" and degree of hardness components in cocoon layer.

  • PDF

Absorption of Carbon Dioxide into Polar Solvents of 2-Amino-2-Methyl-1-Propanol (2-Amino-2-Methyl-1-Propanol이 용해한 극성 용매에서 이산화탄소의 흡수)

  • Son, Young-Sik;Heo, Nam-Hwan;Lee, Sung-Su;Park, Sang-Wook
    • Korean Chemical Engineering Research
    • /
    • v.47 no.3
    • /
    • pp.380-385
    • /
    • 2009
  • The absorption rate of carbon dioxide with 2-amino-2-methyl-1-propanol(AMP) was measured in such non-aqueous solvents as methanol, ethanol, n-propanol, n-butanol, ethylene glycol, propylene glycol, and propylene carbonate, and in water at 298 K and 101.3 kPa using a semi-batch stirred tank with a plane gas-liquid interface. The overall reaction rate constant, obtained under the condition of fast reaction regime, from the measured rate of absorption was used to get the elementary reaction rate constants in complicated reactions represented by reaction mechanism of carbamate formation and the order of overall reaction of $CO_2$ with amine. The correlation between the elementary reaction rate constant and the solubility parameter of the solvent was also presented.

Extraction and Separation of Eicosapentaenoic Acid from Sardine by using Supercritical $CO_2$ Extraction (초임계 추출에 의한 정어리에서 Eicosapentaenoic Acid의 추출 및 분리)

  • 이병호
    • Journal of the Korean Society of Food Science and Nutrition
    • /
    • v.22 no.5
    • /
    • pp.629-635
    • /
    • 1993
  • Full fat sardine oil is readily extracted with supercritical carbon dioxide($SC-CO_2$) at pressure of 5,000~8,000 psig. and temperature of 50~$80^{\circ}C$. Under these conditions $SC-CO_2$ has the density of fluid and diffusivity of gas. Therefore, equilibrium solubility is readily achieved in a column batch extractor which permits high gas flow rates. The results showed that extraction was higher at the pressure of 6,000 psig. and $60^{\circ}C$. Fish oil extracted with $SC-CO_2$ is lighter in color, smells less and contains less iron and phosphorus than hexane-extracted crude oil from the same sardine oil. Eicosapentaenoic acid($C_{20-5}$) in sardine oil was fractionated at 90.5% by the $SC-CO_2$ extractor with heat exchange.

  • PDF