• Korean Chemical Engineering Research
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• 제55권1호
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• pp.54-59
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• 2017

ABS 중합공정 중 잔류 모노머 회수 공정의 유틸리티 사용량 절감을 위한 공정의 개선을 수행하였다. ABS 폴리머 생산 과정 중 잔류 모노머 회수 공정은 제품의 품질 향상을 위해 반드시 필요하다. 잔류 모노머의 회수를 위한 다양한 방식이 있으나, 본 연구에서 대상으로 한 것은 스팀 스트리핑 공정이다. 기존의 스팀 스트리핑은 많은 양의 스팀과 냉각수가 사용되고 있으나, 본 연구를 통해 유틸리티 사용을 절감하는 새로운 방안을 찾고자 하였다. 스트리핑 후 모노머와 함께 배출되는 스팀의 잠열을 진공상태의 수증기로 회수하고, 압축으로 온도를 상승시켜 스트리핑 스팀으로 재사용하도록 함으로써 스팀의 사용을 획기적으로 절감하였다. 또한 모노머 최종 회수 과정에서 발생되는 물을 모노머 응축에 냉각수로 활용함으로써 용수에 대한 사용량도 감소 시킬 수 있었다.

• 농업과학연구
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• 제36권2호
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• pp.225-232
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• 2009

The ratio of saccharification and formation of furans during the acid hydrolysis of agar with oxalic acid and sulfuric acid were examined base on the contents of the agar and acids. The ratio of saccharification in oxalic acid appeared to be 51~59% somewhat higher than 49~61% of sulfuric acid. Formation of the furans during the acid hydrolysis increased proportional to the contents of agar and acid. The relative formation ratio was high 10~47% for furfural (FUR) and 15~29% for hydroxy-methyl furfural (HMF) in 0.5~1.25% sulfuric acid rather than those of oxalic acid. When comparing the removal efficiency of the furans using an alkali treatment, steam stripping and hydrophobic resins, FUR was eliminated 60% by the alkali treatment, 62~90% by steam stripping and 71~75% by Amberlite XAD4 and 7HP, while HMF was removed to low levels of 10.5%, 4~17% and 13~25%, respectively. The loss of reducing sugar was also observed in process of the removal of furans, and the loss rate was the level of 2~4% in alkali treatment, 11~16% in steam stripping and 7~9% in Amberlite resins.

• 한국식품영양학회지
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• 제11권3호
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• pp.272-277
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• 1998

탈취온도를 상이하게 처리한 옥수수기름들로부터 정유성분을 추출하여 이의 favor 성분을 GC로 분리 정량하였다. Flavor성분으로는 8종의 aldehydes를 포함하여 총 16종이 검출되었으며, 주요 flavor성분은 propane, pentane, hexanal 등으로 이는 전체의 70~75%를 차지하였다. 탈취온도가 상승할수록 ethane 및 8종의 propane, pentane, hexane, octane, pentyl furna 함량은 뚜렷한 감소현상을 나타내었다. 한편, 총 flavor 성분함량은 245$^{\circ}C$ 처리군에서 가장 낮아 특이성을 나타내었으며, 탈취온도의 상승에 따라 aldehydes 함량이 비례적으로 증가하였는데, 이는 탈취과정 중 stripping steam, 진공도 등의 영향으로 인한 부분인 자동산화, 분해, 중합, 가수분해 등의 부반응에 기인하는 것으로 사료된다. 따라서, 이취물질의 극소화를 위하여는 지나친 고온탈취를 억제하는 것이 바람직하다는 결론을 얻었다.

• 한국식생활문화학회지
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• 제21권2호
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• pp.166-170
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• 2006

대두유의 탈취과정에서 탈취온도, 진공도, cycle time 및 stripping steam 주입량의 4대 요소를 조정하여 탈취를 행한 후 탈취유의 산가, 과산화물가 및 trans 지방산 함량을 측정한 결과는 다음과 같았다. 즉, 탈취온도가 높을수록 AV, POV는 하락하였으나 trans 지방산 함량이 비례적으로 증가하였다. 진공도는 4torr 수준이 적정하였으며, CT는 길어질수록 효과가 우수하였다. SS주입량은 2.0%(w/w) 수준이 가장 적절한 조건이었다. 이러한 결과를 종합적으로 볼 때, 대두유에서 trans 지방산 함량을 상대적으로 낮게 할 수 있는 탈취조건은 최고 탈취온도 $235^{\circ}C$, 진공도 4torr, CT $14{\sim}15$분 및 SS주입량 2.0%(w/w)내외의 조건에서 trans 지방산 함량 0.31% 내외의 우수한 탈취유의 생산이 가능하였다. 결과적으로 탈취과정에서 trans 지방산 생성량을 극소화하기 위하여는 탈취온도가 가장 중요하였는데, AV, POV 등 다른 품질 요인들을 동시에 고려할 때, 더 이상의 탈취온도 하락은 어려운 것으로 판단된다.

• 한국식생활문화학회지
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• 제20권5호
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• pp.627-631
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• 2005

대두유를 정제하는 과정에서 대두원유를 탈검-탈산-탈색-탈취의 일반적인 정제공정을 모두 거친 것과 이들 정제공정을 생략하고 협잡물만 제거한 후 그대로 탈취하여 고유의 색상을 갖는 독특한 대두유를 얻었다. 이 때의 차이는 Sample 1은 정상 탈취유, Sample 2, 3는 협잡물만을 제거한 다음 batch type deodorizer에 주입하여 진공도, 최고온도, stripping steam 주입량, 탈취시간 등을 차등화하여 3단계 탈취를 행하였다. 얻어진 탈취유의 이화학적 특성은 Sampl 1의 경우 산가 0.034, Lovibond color 9.1Y/0.9R, 과산화물가 0의 엷은 노란색 대두유였다. 그러나 Sample 2는 산가 0.078, Lovibond color 65.0Y/18.39R/4.2B/0.1N, 과산화물가 0.7의 밝고 투명한 녹색을 나타내었다. Sample 3은 산가 0.072, Lovibond color 37.3Y/3.8R/0.1B/0.1N, 과산화물가 1.6의 짙은 검붉은 갈색을 나타내어 차이를 보였다. 이러한 착색 탈취대두유는 앞으로 솔잎향미유, 들깻잎향미유 등의 다양한 향미유 제조의 원료유로 각광 받을 것으로 판단된다.

• Journal of Advanced Marine Engineering and Technology
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• 제10권1호
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• pp.74-84
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• 1986

Ejectors, having no moving, lubricating and leaking parats, are widely used as marine pumps because of its high working confidence. For instance, uses in ships are stripping in crude oil tank, bilge discharge in engine room, ballast water pumping on are carrier, and brine discharge from fresh water generator. And it is also used as cooling water recirculating pump in boiling water type nuclear reactor and deep-well pump. It is not easy to determine the optimal dimension for designing each ejector agreed with its suggested performance condition, because complicated calculations must be repeated to obtain the maximum efficiency affected by flowrate ratio, head ratio, area ratio and so on. Therefore, it is considered that the CAD (Computer-Aided Design) for ejector is a powerful method for design according to the individual design condition. In this paper, a computer program for water ejector design is developed based on the previous paper on theoretical analysis and experimental results for water ejector. And from the theoretical approach, an equation for the working limit and an equation for determing the shape of throat are obtained. The validity of the present computer program is sufficiently confirmed through the comparison of the computed results with the main dimension of the previous manufactured water ejector. This program will be easily developed as the CAD for various kinds of ejectors, including steam ejector.

• 설비공학논문집
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• 제22권8호
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• pp.545-552
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• 2010

Research and development efforts to reduce $CO_2$ emission are in progress to cope with global warming. $CO_2$ emission from fossil fuel fired power plants is a major greenhouse gas source and the post-combustion $CO_2$ capture is considered as a short or medium term option to reduce $CO_2$ emissions. In this study, the application of the post-combustion $CO_2$ capture system, which is based on chemical absorption and stripping processes, to typical fossil fuel fired power plants was investigated. A coal fired plant and a natural gas fired combined cycle plant were selected. Performance of the MEA-based $CO_2$ capture system combined with power plants was analyzed and overall plant performance including the energy consumption of the $CO_2$ capture process was investigated.

• 한국물환경학회지
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• 제26권4호
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• pp.557-565
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• 2010

Recently, regulations on toxic compounds in aquatic environment have been strengthened in korea due to the increasing public awareness of the water quality. Typically, these regulations include introduction of emerging toxic compounds and stricter effluent limitations for the already regulated compounds. However, too strict regulations may cause excessive burden on the industry. Therefore it is also important to assess the economic impacts when the new effluent limitation guidelines are introduced. The estimation of the additional cost for the wastewater dischargers to meet the new guidelines are based on the selected treatment technology to handle the hazardous substances and the regulatory levels for effluent limitations. To explore the procedures for cost estimation in enforcing new effluent limitations, a case study was performed specially for 1,4-dichlorobenzene. The pollutants of concern are surveyed for different industrial categories and various treatment technologies. For a given pollutant, the general performances of the treatment technologies are surveyed and a representative technology is selected. For a given technology, the capital cost and annual Operation and Maintenance (O&M) cost was calculated. The calculation of baseline costs to operate ordinary treatment technologies is also important. The ratio between the cost for introducing new treatment process and the baseline cost required for conventional technology was used to evaluate the economic impact on the industry. For 1,4-dichlorobenzene, steam stripping and activated carbon processes were selected as the specific treatment technologies. The cost effects to the regulation of the compound were found to be 6.4% and 14.5% increase in capital cost and O&M cost, respectively, at the flow rate over $2,000m^3/d$ for the categories of synthetic resin and other plastics manufacturing industry. For the case of petrochemical basic compounds manufacturing industry, the cost increases were 5.8% and 12.4%, respectively. It was suggested that cost effect analysis to evaluate the economic impacts of new effluent limitations on the industry is crucial to establish more balanced and reasonable effluent limitations to manage the industrial wastewater containing emerging toxic compounds in the wastewater.