• Title/Summary/Keyword: yellowfin sole skin gelatin

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Effect of Gelation Condition on Physical Properties of Yellowfin Sole Gelatin Prepared by Ethanol Fractional Precipitation (에탄올처리 각시가자미껍질 젤라틴의 물리적 특성에 대한 겔화조건의 영향)

  • Kim, Jin-Soo;Cho, Soon-Yeong;Ha, Jin-Hwan;Lee, Eung-Ho
    • Korean Journal of Food Science and Technology
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    • v.27 no.4
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    • pp.483-486
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    • 1995
  • With a view to increase utility of ethanol fractionated fish skin gelatin as a food source, the effect of gelation condition on physical properties of the gelatin was investigated. The physical properties of gelatins treated with or without ethanol were improved with a concentration of gelatin increased. The properties such as gel strength, melting point and gelling point of 10% gelatin sol or gel were reached to maximum at pH 6.0 in ethanol treated gelatin and pH 5.0 in non treated one, respectively. Gel strength and melting point of both gelatin gels chilled for long time at low temperature were superior to those of both gelatin gels chilled for short time at high temperature. Gel strength, melting point and gelling point of ethanol treated gelatin gel or sol prepared under optimized gelation conditioning were superior to those of non treated one.

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Enzymatic Hydrolysis of Yellowfin Sole Skin Gelatin in a Continuous Hollow Fiber Membrane Reactor (연속식 중공사막 반응기를 이용한 각시가자미피 젤라틴의 가수분해)

  • KIM Se-Kwon;BYUN Hee-Guk;KANG Tae-Jung;SONG Dae-Jin
    • Korean Journal of Fisheries and Aquatic Sciences
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    • v.26 no.2
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    • pp.120-132
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    • 1993
  • A continuous hollow fiber membrane reactor(CHFMR) was developed and optimized for the production of yellowfin sole(Limanda aspera) skin gelatin hydrolysates using trypsin. The results were summerized as follows: The $K_m$ value of the CHFMR was 2.4 times higher than that of the batch reactor, indicating reduced enzyme affinity for the substrate. The $K_2$ value of the CHFMR was 8.5 times lower than that of the batch process, showing a significant reduction in trypsin activity in the CHFMR. The optimum operating conditions for the CHFMR process were $55^{\circ}C$, pH 9.0, flux 7.79 ml/min, residence time 77min, and trypsin to substrate ratio, 0.01(w/w) After operating for 60min under the above conditions, $79\%$ of the total amount of initial gelatin was hydrolysed. Enzyme leakage was observed through the 10,000 MWCO membrane after the 20min of reactor operation, while none occurred after 5hr. Total enzyme leakage was about $12.95\%$ at $55^{\circ}C$ for 5hrs. However, there was no apparent correlation between enzyme leakage and substrate hydrolysis. The membrane has a significant effect on trypsin activity loss for 60min of the CHFMR operation. The CHFMR operating with the membrane lost $34\%$ of the initial activity versus a $23\%$ loss of activity after 3hr in the continuous reactor lacking the hollow fiber membrane. The measurement of fouling property showed that relative flux reduction was $91\%$ and flux recover rate was $92\%$ at $10\%$ substrate solution. The productivity(378.85mg product/mg enzyme) of the CHFMR was more than 4 times higher than that of the batch reactor at $55^{\circ}C$.

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