• Title/Summary/Keyword: agitation speed

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Production of Alkaline Protease by Entrapped Bacillus licheniformis Cells in Repeated Batch Process

  • Mashhadi-Karim, Mohammad;Azin, Mehrdad;Gargari, Seyyed Latif Mousavi
    • Journal of Microbiology and Biotechnology
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    • v.21 no.12
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    • pp.1250-1256
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    • 2011
  • In this study, Bacillus licheniformis cells were immobilized by entrapment in calcium alginate beads and were used for production of alkaline protease by repeated batch process. In order to increase the stability of the beads, the immobilization procedure was optimized by statistical full factorial method, by which three factors including alginate type, calcium chloride concentration, and agitation speed were studied. Optimization of the enzyme production medium, by the Taguchi method, was also studied. The obtained results showed that optimization of the cell immobilization procedure and medium constituents significantly enhanced the production of alkaline protease. In comparison with the free-cell culture in pre-optimized medium, about 7.3-fold higher productivity was resulted after optimization of the overall procedure. Repeated batch mode of operation, using optimized conditions, resulted in continuous production of the alkaline protease for 13 batches in 19 days.

Scale-up of Melting Chamber for a Pyrolysis Melting Incinemtion System (폐기물 열분해/용융 소각 시스템의 용융로 Scale-up 연구)

  • Yang, Won;Kim, Bong-Keun;Yu, Tae-U;Jeun, Keum-Ha
    • 한국연소학회:학술대회논문집
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    • 2007.05a
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    • pp.168-175
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    • 2007
  • Ash melting chamber is one of the key facility of the pyrolysis-melting incineration system, and it should be designed and operated very carefully for avoiding solidification of slag. In this study, an example of numerical and experimental scale-up process of the melting chamber, in which high speed air is injected to the molten slag and generates bubbles, which enhances agitation of the slag and char combustion, is presented. Cold flow test, combustion and melting test in a lab-scale (30 kg/hr) chamber and a pilot scale (200 kg/hr) chamber. Minimum energy for maintaining molten slag is derived, and it was found that the molten slag can be maintained efficiently by concentrating heat into the bubbling slag.

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A study on the wear resistance of Ni-SiC composite plating (Ni-SiC 복합도금층의 내마모성에 관한 연구)

  • 김성호;한혜원;장현구
    • Journal of the Korean institute of surface engineering
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    • v.29 no.1
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    • pp.26-35
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    • 1996
  • The Ni-SiC composite plating was performed in a Watt nickel solution and the wear resistance of the composite layer was studied on a pin-on-flat type wear tester. The volume losses and friction coefficients were measured. It was found that the quantity of SiC powder in the composite layers was affected by SiC concentration, pH, temperature, and agitation speed in the Watt nickel solution. The hardness and wear resistance of the coatings increased with SiC content. The quantity of SiC powder in the coating from a nickel sulfamate solution is larger than that of the Watt nickel solution, because the amount of nickel ions absorbed on the SiC powder in the nickel sulfamate solution is greater than that in the Watt's solution.

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A Fundermental Study Color Removal of Dyeing Wastewater using Low Cost Adsorbents (저가흡착제를 이용한 염색폐수의 색도제거에 관한 기초 연구)

  • 김은호;장성호
    • Journal of environmental and Sanitary engineering
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    • v.14 no.2
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    • pp.40-45
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    • 1999
  • This study deals with an investigation on low cost adsorbents locally available n dyeing wastewater treatment of color removal. Peat, bentonite, slag and fly ash were utilized for this study. Considering that low cost adsorbents contained in $SiO_2$, $Fe_2O_3$ and $Al_2O_3$ compositions, and coagulants were mainly used aluminate and ferrate in color removal. Color of dyeing wastewater was high removed in peat, berntonite and slag except for fly ash with passed time. It could be known that color removal of peat and slag were increased to pH 4, but was hardly changed with advancing to alkaline. Color intended to be high removed with increasing of agitation speed but to be almost slow after 150rpm. As a result on the experiment of Freundlich adsorption isotherms, adsorption intensity(l/n) appeared to be peat>fly ash>slag>bentonite and adsorption capacity(k) came out peat>bentonite>slag>fly ash. Therefore, if low cost adsorbents substituted for existing adsorbents, peat, bentonite and slag could look forward to an expected economical effect.

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Recycling of Casts as an Adsorbent for Phosphorous Removal (인제거를 위한 흡착제로써 분변토 재활용)

  • 손희정;김은호;이용희
    • Journal of environmental and Sanitary engineering
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    • v.13 no.2
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    • pp.76-81
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    • 1998
  • The technology of removing phosphorous, considered as one of the most important control nutrients causing eutrophication in various water bodies, have been investigated by many researchers. In this study, casts which can be obtained from the vermicomposting of mixing sewage sludge and cow manure, were used as an adsorbent, and their effects of several physical/chemical factors on the efficiencies of phosphorous adsorption were examined by batch tests. Generally, it could be showed that the efficiencies of phosphorous adsorption were very influenced by cast dosage, temperature and agitation speed. If we reflected the adsorption capacity(k) and adsorption intensity(1/n) of Freundlich isotherm, we couldn't consider casts as a good adsorbent for removing phosphorous. But, because casts were relatively excellent in cation exchange, in point of waste recycling, we could know that they were capable of removing phosphorous. The SEM observation revealed that the evident variations were hardly seen, but particle sizes of cast were relatively bigger and showed forms of smaller plate than before.

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공동캡슐화를 이용한 키토산 분해반응에서 alginate 막의 특성 및 크기에 따른 올리고당의 분자량 내외 분포

  • Lee, Gi-Seon;Choe, Myeong-Rak;Song, Sang-Ho;Im, Hyeon-Su
    • 한국생물공학회:학술대회논문집
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    • 2000.11a
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    • pp.608-611
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    • 2000
  • To separate chitosanoligosaccharides easily by size exclusion, an coencapsulating technology of substrate and enzyme was developed. Chitosan and chitosanase were enveloped in this membrane and the product released to medium by size exclusion. The lower limit of the alginate concentration and the agitation speed were 0.5% and 40 rpm, respectively. Membrane thickness and capsules diameter were $10{\mu}m$ and approx. 3.0mm, 1.5mm, respectively. The molecular weight difference by concentration and cps of alginate were of little significance. And also, the molecular weight of distribution according to enzyme concentration was low concentration of enzyme produced high molecular weight of oligosaccharides. At 1.5mm size of capsule, product diffusion rate to outer part was higher than other capsules. The molecular weight distribution of the released oligosaccharides ranged from 1000 to 6000 Da.

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Optimal Growth Conditions for Carotenoid Pigment Production from marine Microorganism (해양미생물로부터 카로테노이드 색소의 생산을 위한 최적조건)

  • 정영기;김태수;정명주;류병호;주우홍;박정욱
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.28 no.6
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    • pp.1239-1243
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    • 1999
  • The optimal medium composition for the production of carotenoid pigment from Haloarcular sp. EH 1 as a dietary for fishes were 1.0% sucrose, 1.0% yeast extract, 25% sodium chloride, 0.3% sodium citrate, 0.2% potassium chloride, 2.0% magnesium sulphate, 0.002% ferric sulphate(pH 7.0). The incubation temperate, aeration rate and agitation speed were 40oC, 100ml medium/500ml vol. shaking flask, and 180 rpm/min. The carotenoid pigment production was highest after 5 days of incubation with the light.

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Removal of Cl from the Incineration Ash of Domestic Municipal Solid Waste

  • Han, Gi-Chun;Kim, Hyung-Seok;Ahn, Ji-Whan;Kim, Hwan
    • Proceedings of the IEEK Conference
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    • 2001.10a
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    • pp.628-632
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    • 2001
  • The removal rate of Cl from municipal solid waste incineration(MSWI) ash(bottom ash and fly ash) by washing was investigated. The Cl contents in the bottom ash and fly ash were 2.6-3.0% and 25-30% respectively, and KCl, NaCl, CaCIOH and friedel's salt were main components. From the results on the effects of washing time and temperature, the Cl contents in the bottom ash and fly ash were decreased up to 0.3% and 2.0% respectively by using of water as a solvent within 30 min at 2$0^{\circ}C$, 300 rpm of agitation speed and 10 of liquid/solid ratio. It is expected that the removal of Cl from the incineration ash by washing could make use of the ash for a cement raw material and so on.

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Study on Semi-Solid Processing of Al-Si Alloys by Rotation of Permanent Magnets (영구자석의 회전을 이용한 Al-Si합금계의 반응고합금 제조공정 연구)

  • Song, In-Hyuck;Hahn, Yoo-Dong;Yun, Jung-Yeul;Ahn, Jung-Ho
    • Journal of Korea Foundry Society
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    • v.17 no.1
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    • pp.67-75
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    • 1997
  • The semisolid processing of two Al-Si alloys, A356 and Al-25wt%Si, was studied with using the rotor composed of permanent magnets. The semisolid slurry was agitated by the electromagnetic force induced from the rotating permant magnets. The round shaped primary ${\alpha}$ phases were formed in A356 alloy as a result of agitation. In Al25wt%Si alloy, spherodization of primary Si particles was not observed with the rotation of the magnets. The primary Si particles were segregated to the outer surface area of sample, which became pronounced with increasing the rotating speed of magnets.

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Optimization of Lipase Pretreatment Prior to Lipase Immobilization to Prevent Loss of Activity

  • Lee, Dong-Hwan;Kim, Jung-Mo;Shin, Hyun-Yong;Kim, Seung-Woo
    • Journal of Microbiology and Biotechnology
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    • v.17 no.4
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    • pp.650-654
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    • 2007
  • In our previous work, a method of pretreating lipase was developed to prevent loss of its activity during covalent immobilization. In this study, Rhizopus oryzae lipase was pretreated before immobilization and then immobilized on a silica gel surface. The effects of the various materials and conditions used in the pretreatment stage on the activity of immobilized lipase were investigated. Immobilized lipase pretreated with 0.1% of soybean oil had better activity than those pretreated with other materials. The optimal temperature, agitation speed, and pretreating time for lipase pretreatment were determined to be $40^{\circ}C$, 200rpm, and 45min, respectively. The activity of immobilized soybean oil pretreated lipase was 630U/g matrix, which is 20 times higher than that of immobilized non-pretreated lipase. In addition, immobilized lipase activity was maintained at levels exceeding 90% of its original activity after 10 reuses.