• Title/Summary/Keyword: Stepwise Dilution Gas

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The Study on the Production Method of Stepwise Dilution Gas for Odor Analysis with Orifice Tubes (오리피스 튜브에 의한 단계별 냄새 분석용 희석가스의 제조방법에 관한 연구)

  • Kim, Han-Soo;Lee, Seok-Jun;Kim, Sun-Tae
    • Journal of Korean Society of Environmental Engineers
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    • v.35 no.2
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    • pp.137-143
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    • 2013
  • This study is to develop the production method of stepwise dilution gas for the evaluation of complex odor concentration by orifice tube. The basic orifice tube for 10 and 30 times of dilution sample was made at first, and with the combination of the basic orifice tubes we can continuously manufacture the stepwise dilution sample gas for air dilution sensory test ; 10, 30, 100, 300, 1,000, 3,000 times etc. The hole size of orifice tube was 0.84 mm for 10 times of dilution sample, and was 0.34 mm for 30 times. Dilution sample gas made with the basic orifice tube have an excellent reproducibility, 2%RSD. In addition, over 90% of correlation was shown between the sample made by the orifice tube and the sample by the syringe dilution method. Because there was no concentration drift of dilution gas with changes of connected pump flow, the basic orifice tube could be mounted directly with a vacuum suction box, and could be used simply as a tool for the evaluation of odor, especially on site.

Production of Single Cell Protein on Petroleum Hydrocarbon -IV. On the Continuous Fermentation and Some Cultivation Conditions for Candida tropicalis KIST 351- (석유탄화수소를 이용한 단세포단백질의 생산에 관한 연구 -IV. Candida tropicalis KIST 351의 연속배양 및 몇가지 조건에 관하여-)

  • Lee, Yong-Hyun;Pyun, Yoo-Ryang;Kwon, Tai-Wan
    • Korean Journal of Food Science and Technology
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    • v.4 no.3
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    • pp.200-205
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    • 1972
  • Effects of several different petroleum fractions (LGO, HGO, VGO, Diesel oil, SP(E), HGO-wax, L/M-wax), stepwise addition of calculated amounts of HGO at defined intervals, recycling of spent media on cell growth of Candida tropicalis KIST 351 were studied using $2.5{\ell}$ fermenter by batch process. In addition, continuous cultivation of the yeast was also performed in the light of biomass production using $28{\ell}$ fermenter with LGO. 1) Cell concentration, yield on the basis of gas oil and n-paraffin with the petroleum fractions were in the range of $11{\sim}15g/{\ell}$, $10{\sim}12%$ and $77{\sim}82%$, respectively. 2) By stepwise addition of the gas oil, cell concentration and yield on the oil were increased up to 18.9 g/land 13%, respectively. 3) Spent medium slowed emulsifying ability of hydrocarbon and stimulating effect on the cell growth. Without additional supplementation of $Mg^{++}$ up to 20% of spent medium could be reused, while by adding of the $Mg^{++}$, 50% of medium could be recycled. 4) Optimum condition of continuous cultivation for biomass production was attained at the dilution rate of $D=0.1{\sim}0.125\;hr^{-1}$. Maximum yield coefficient on consumed n-paraffin was 0.94 at $D=0.1\;hr^{-1}$, however, 24% of supplied n-paraffin in the media was not utilized at this dilution rate.

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