• Proceedings of the Korean Environmental Sciences Society Conference
• /
• 1999.10a
• /
• pp.67-68
• /
• 1999

포말분리법을 이용하여 해수 중의 단백질 제거 실험을 수행한 결과 유입 단백질의 농도가38.0g/m일 때 제거 속도가 최대였으며 0.48min의 수력학적 체류시간에서 9.65g protein/m3.min의 가장 높은 단백질 제거속도를 얻을 수 있었다.

• Journal of Life Science
• /
• v.8 no.5
• /
• pp.504-508
• /
• 1998

A study was conducted to evaluate a protein removal characteristics by foam separation. The foam separator was operated in well-mixed tank which would be considered as a completely mixed condition. The feasibility of foam separation to remove protein from fresh and sea water was investigated. Protein removal characteristics of the foam separator were obtained by batch reactor operations. To find the effect of the operating parameter to protein removal rate, the foam separation was carried with variation of initial protein concentration and foam height. The results indicated that the protein removal efficiency was increased with increasing protein concentration and decreased with increasing foam height. The relationship between protein concentration and protein removal rate was evaluated by linear regression.

• Journal of Korean Ophthalmic Optics Society
• /
• v.10 no.2
• /
• pp.91-97
• /
• 2005

We investigated the question whether protein removing activities of enzyme cleaner - protein remover for soft contact lens - are associated with the material of soft contact lens as well as action time, temperature and pH of enzyme solution. We used a subtilisin cleaner as protein remover and estimated the protein amount remained on soft contact lens after using the subtilisin cleaner under the different conditions. The remained protein in soft contact lens was greatly decreased until treatment for 60min, but no significant differences were found from 60min to 24hr. The cleaning effect of the enzymatic treatment in the range of $15{\sim}30^{\circ}C$ was constant. however, there was a significant decline of the protein removing effect at $10^{\circ}C$ and less. The pH of the solution was also important for the efficacy of the enzymatic treatment. The activity of the enzyme cleaner was highest in pH 8.0 and significantly decreased a pH below 7. The pH dependence was found to be related to the conformational change of subtilisin. Furthermore, significant differences in the protein deposit removing efficacy of the subtilisin cleaner were found among the soft contact lens materials.

• Journal of Korean Ophthalmic Optics Society
• /
• v.19 no.1
• /
• pp.51-57
• /
• 2014

Purpose: The present study was conducted to establish the experimental condition for the proper evaluation of protein removal efficacy when developing protein removal agents. Its protein removal efficacy was further analyzed and compared with the result from protein removal efficacy against protein deposition on contact lens to suggest the evaluation method for efficacy of protein removal agents. Methods: Protein digestibility assay presented in the Korean pharmacopoeia was selected to establish the evaluation method for efficacy of papain, pancreatin, subtilisin A and protease itself as a ingredient and protein removal tablets or solution containing those enzymes and find a suitable test conditions. Furthermore, the cleaning efficacy of commercially available protein removal tablets and solution on balafilcon A lens deposited with protein artificially was measured and the correlation between two evaluation methods was further analyzed. Results: When pancreatin itself and the product containing pancreatin was evaluated by protein digestibility assay, both reached 28 IU/mg, the standard value of protein digestibility suggested by the Korean pharmacopoeia. In case of protease and subtilisin A tested with trichloroacetic acid B solution, both of them met the enzyme activity level proposed by the manufacturers when they were evaluated by protein digestibility assay however, papain and subtilisin A tested with trichloroacetic acid A solution were not reached the enzyme activity level. Among protein removal agents, three products except a product containing pancreatin did not meet the enzyme activity value specified by the manufacturer when they were evaluated by protein digestibility assay. However, actual protein removal efficacy of three products except a papain-containing product on the lens was greater than 90% protein removal. In the case of papain-containing protein removal product, its effect was not measured by protein digestibility assay however, its actual protein removal efficacy on the lens reached 73.72%. Conclusions: From the results, it was confirmed that the efficacy of protein removal agents for contact lens should be evaluated by different method according to the type of proteolytic enzyme contained. That is, the protein removal agents containing pancreatin, protease and subtilisin A can be evaluated by protein digestibility assay and protein removal efficiency evaluation and the products containing papain can be effectively evaluated by only the evaluation method for protein removal efficiency employing the lens.

• KSBB Journal
• /
• v.11 no.1
• /
• pp.15-21
• /
• 1996

Purification of hyaluronic acid produced by Streptococcus equi was carried out to obtain clinical grade hyaluronic acid. The removal method of the bacteria was selected as filtration because filtration was the most effective method in removing impurities such as protein and nucleic acid of the fermentation broth. The removal efficiencies of protein and nucleic acid of hyaluronic acid solution were increased to 75% and 67%, respectively, by filtration with adding 0.6% of activatied carbon and 1.0% colite. Hyaluronic acid solution was precipitated by mixing with 2 volumes of ethanol. Effects of pH and conductivity on ethanol preciptation of hyaluronic acid were investigated. Protein and nucleic acid of hyaluronic acid were remained almost constant regardless of pH and conductivity, and the recovery of hyaluronic acid was optimum as about 85% at pH 7 and l00mS of conductivity Protein of hyaluronic acid was completly removed by three serial filtration and ethanol precipitation, however, nucleic acid was not removed. Hyaluronic acid solution was passed through a column of Duolite A7 to remove its nucleic acid, where 65% of nucleic acid was removed at pH 7 and 40mS of conductivity. The residual nucleic acid of hyaluronic acid solution was completly removed by treatment of 0.2% hydroxyapatite and the clinical grade hylauronic acid could be obtained.

• Korean Journal of Fisheries and Aquatic Sciences
• /
• v.28 no.5
• /
• pp.599-606
• /
• 1995

The feasibility of foam separation to remove protein produced from fish culture water was investigated, By assuming foam separation column as a single well-mixed pool, a simplified model for foam separator conditions was alse studied under the batch operation. The model indicated that the protein removal could be described as a first-order reaction whose rate increases with both superficial air velocity and protein concentration in the bulk solution. from ,the results of an experimental study on the effects of superficial air velocity, the protein concentration, temperature, and pH on protein removal, the superficial air velocity and initial protein concentration in bulk solution were found to be important operational factors. Other experimental results important that foam separator operated under batch conditions would be considered as a completely mixed reactor. The protein removal rate by foam separation process was increased proportionally with the superficial air velocity, and the adsorptive removal rate of protein was found to obey Langmuir adsorption formula. The preposed simplified model was verified with the experimental data obtained from this study. Under the experimental range used, both temperature and pH did not affect the protein removal.

• KOREAN JOURNAL OF CROP SCIENCE
• /
• v.40 no.6
• /
• pp.723-730
• /
• 1995

Effects of leaf and pod removal on changes in dry weight and protein content of soybean [Glycine max (L.) Merr.] cultivar 'Hwangkeumkong' were measured at the research farm of Korea University in 1992. The upper 40% and lower 60% of leaves and pods were subjected to treatments at the growth stage of beginning pod(R3). Leaf dry weight of lower part was increased by upper leaf-lower pod removal, but seed dry weight of upper part was decreased. The upper leaf-lower pod removal also increased stem dry weight and decreased upper pod dry weight. Protein content was higher in lower leaves than upper leaves. Seed protein contents were decreased both upper leaf-lower pod removal and lower leaf-upper pod removal treatments. The upper leaf-lower pod removal showed the highest leaf and the lowest seed protein quantities among the five treatments. These results indicated that protein sources were moved from lower to upper parts but weak in remobilization from leaves for the long distance translocation during the reproductive growth period of soybean plants.an plants.

• Proceedings of the Membrane Society of Korea Conference
• /
• 2004.05b
• /
• pp.49-52
• /
• 2004

생체 내에서의 요소 형성은 단백질이 아미노산으로 분해되어 인체에 남은 요소는 오줌으로 배출된다. 그러나 고농도의 urea의 경우 단백질을 변형시키게 된다[1-2]. 이러한 고 농도의 urea를 단백질 공정을 통해서 제거시키는 기술이 최근의 투석 과학이다. 그러나 이러한 방법은 urea의 제거와 함께 많은 양의 단백질과 양이온이 유출 및 오염의 문제가 많이 발생하고 있다[3].(중략)

• Korean Journal of Food Science and Technology
• /
• v.27 no.3
• /
• pp.313-317
• /
• 1995

Ion exchange process was optimized to purify ultrafiltrated bean cooking water(BCW) for the production of soy-oligosaccharides. The ultrafiltrated BCW with cutoff MW(COMW) 20,000 membrane was treated with various ion exchange resins. Protein and ash were mostly removed by anion and cation exchange resins, respectively. Based upon removing capabilities for ash and protein, a cation exchange resin(SK1B) and an anion exchange resin(WA30) were selected. Protein and ash were more efficiently removed at low extract/resin ratios(ERR), but part of the oligosaccharides were concomitantly lost. When 2-step-ultrafiltrated BCW first with COMW 20,000 membrane and successively with COMW 5,000 membrane was treated with a mixed resin(SK1B : WA30 =1 : 2) at ERR 5.0, most oligosaccharides were recovered in a clear protein- and ash-free liquid.

• KSBB Journal
• /
• v.9 no.2
• /
• pp.174-179
• /
• 1994

Chitin was isolated from crab shell wastes and characterized for its chemical and physical properties. White powdered chitin was obtained through demineralizaticn, deproteinization and decoloration process. The contents of inorganics was less than 0.5%, whereas protein and lipid were almost removed. The results of IR spectroscopic analysis for the isolated chitin showed similar characteristics with that of Sigma product. Degree of deacetylation of purified chitin was significantly higher than Sigma product and viscosity average molecular weights was $2.3{\times}10^5~3.2{\times}10^5$. SEM analysis showed that the obtained chitin had the fibril shaped morphology.