• Title/Summary/Keyword: CFC-Alternatives

Search Result 33, Processing Time 0.02 seconds

Comparison of Cleaning Performance of CFC 113 and the Alternatives (CFC 113과 대체세정제의 세정성능 비교)

  • Row, Kyung Ho;Choi, Dai-Ki;Lee, Youn Yong
    • Analytical Science and Technology
    • /
    • v.6 no.5
    • /
    • pp.521-530
    • /
    • 1993
  • According to the Montreal Protocol, CFC 113, one of the ozone-depleting substances, will be prohibited to use as a cleaning solvent essentially in the electronic industry. Therefore, the development of the alternative cleaning solvents to CFC 113 is being accelerated. A number of the alternative cleaning solvents are avialable on the market. The alternatives of Axarel 32(DuPont), Cleanthru 750H(KAO Chemical), and EC-Ultra(Petroferm) are chosen for the comparison of cleaning performance with CFC 113. The test methods for measuring the cleaning performance were composed of the measurement of the physical properties, the experiments on the material compatibility with cleaning solvents, the measurement of the evaporation rate, and finally the experiments of the removal efficiency. Normally the basic physical properties of the alternatives had higher boiling points, viscosity and surface tension, which were quite different to those of CFC 113. In terms of solubility of rosin-based flux, the solubilities of abietic acid (nonpolar organic) were similar, but those of the activator (polar organic) in the alternatives were better than CFC 113. The evaporation of the alternatives was very slow, compared to CFC 113, which had much lower boiling point. All the cleaning solvents showed the good material compatibility with FR4 and Cu-coated PCB. The better removal efficiencies of abietic acid were obtained when using the ultrasonic mechanical energy over the dipping method. The experiments also indicated the very slow-eavaporating solvent was not desirable with the dipping cleaning method, and the differences in the removal efficiency of the alternatives with the ultrasonic cleaning method were negligible. Among the alternatives, the overall cleaning performances were obsorved as almost similar. Before selecting the ultimate cleaning solvent, the application of cleaning machine, environmental issues, and economics are simultaneously considered with the cleaning performance.

  • PDF

A Study on the Fluorination of Pentachloroethane (Pentachloroethane의 불소화 반응에 관한 연구)

  • Park, Kun-You;Kwon, Young-Soo;Kim, Hoon-Sik;Lee, Sang-Deuk;Lee, Byung-Gwon
    • Applied Chemistry for Engineering
    • /
    • v.4 no.2
    • /
    • pp.318-323
    • /
    • 1993
  • Pentachloroethane($CHCl_2CCl_3$) was synthesized and reacted with hydrogen fluoride using antimony pentahalide catalyst($SbCl_xF_y$) in order to manufacture HCFC-123$(CF_3CHCl_2)$, a potential CFC-11$(CFCl_3$) substitute candidate. Products analyses showed the fluorination proceeds through fluorine-chlorine exchanges between $HF/SbCl_xF_y$ and $SbCl_xF_y/CCl_3CHCl_2$ respectively. The degree of fluorination of $CCl_3$ group in pentachloroethane was greatly affected on the reaction temperature, but the effect of catalyst concentration was relatively small. Mechanistic study was also performed to elucidate the pathway to the formation of side-products such as $CCl_3CFCl_2$, $CFCl_2CFCl_2$ and $CF_2ClCFCl_2$.

  • PDF

Separation of EPA and DHA from Fatty Acid of Fish Oil by Supercritical Fluid Rectification (초임계유체 정류법에 의한 어유지방산으로부터 EPA와 DHA의 분리)

  • Kim, Jae-Duck;Lim, Jong-Sung;Lee, Youn-Woo
    • Journal of the Korean Applied Science and Technology
    • /
    • v.14 no.2
    • /
    • pp.49-55
    • /
    • 1997
  • It was tested the possibility that EPA and DHA could be separated from fish oil fatty acid ethyl ester(FAEE) in the supercritical carbon dioxide rectification method. Experiments were carried out in the 1800mm tall and temperature gradient packed rectification column at the pressure of 100bar and carbon dioxide flow rate of 52.43NL/min. Experimental results showed that this method was useful to separate the FAEE by the relative volatility of the components. The maximum attainable concentration of EPA, DHA and both of them in product were 41%, 43% and 57% respectively in this rectification column using raw fish oil feed.