• 한국식품과학회지
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• 제38권4호
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• pp.488-494
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• 2006

두부 순물을 UF막으로 농축시켜 제조한 UF 분리농축분말의 일반성분 및 이들 분말을 식품에 첨가할 경우 반드시 고려해야 할 용해도, 유화력, 거품형성능에 대해 살펴보았다. 그 결과 일반 성분에 있어서, UF 분리농축분말의 수분함량과 탄수화물 함량은 순물과 큰 차이가 없었으며 단백질 함량은 순물분말보다 2배가량 높았으나 회분함량은 2배 낮았다. 유지흡착력을 비교 시 ISP>UF 농축분말>순물 순으로 높게 나타났으며 UF 분리농축 분말의 용해도가 ISP와 순물에 비해 높기 때문에 수분흡착력은 매우 미약하였다 UF 분리농축분말의 단백질의 용해도는 등전점 부근인 pH 4.0에서 가장 낮았으며 산성 또는 알칼리성으로 갈수록 증가하는 전형적인 단백질 용해도 곡선을 나타내었다. 유화력은 ISP와는 달리 pH에 따른 현화를 보이지 않으며 150-200 정도의 EAI 값을 나타내었고, 유화안전성은 pH 6.0 이하의 산성에서 더 높은 값을 나타내며 대체로 75-92%의 높은 유화안정성을 보였다. UF 분리농축분말의 거품형성능은 증류수 처리구간에서 ISP와는 달리 pH 4.0-6.0에서 가장 우수하였으며 NaCl 농도가 높을수록 약간 감소하는 경향을 나타내었고, 거품안정성을 측정한 결과 ISP에 비해 대두 단백질의 등전점인 pH 4.0 부근에서 5-7배 높은 거품안정성을 나타내었으나 pH 4.0을 제외한 모든 pH 구간에서 20분 안에 거품이 소멸되었다 UF 분리농축분말은 isoflavone 등 여러가지 기능적 성분을 함유하는 것으로 알려져 있을 뿐만 아니라 용해도, 유화력, 유화안정성, 거품형성능 등이 ISP보다 우수하여 식품가공에서 다양하게 활용될 수 있을 것으로 기대된다.

• 한국미생물·생명공학회지
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• 제22권1호
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• pp.99-105
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• 1994

In this study we compared traditional cheesemaking process with the process utilizing ultrafiltration(UF) system. The whole milk retentates were prepared by ultrafiltration to volume concentration ratio(VCR) of 2.00:1, 2.25:1 and 2.50:1. Along with the untreated whole milk, there were studies in terms of the change of pH, titratable acidity and Soxhlet-Henkel($\circ $SH) value by mesophilic lactic starter and curd formation by rennet during Gouda cheese manufacture. Due to the increase of buffering effect titratable acidity and $\circ $SH value increased with the higher concentration ratio. When inoculated with the same volume of mesophilic lactic starter, less pH change occurred in UF retentates than in control milk. When added 0.0025% rennet, UF retentates coagulated 16~ 17 minutes ealier then the control milk. Gouda cheese yield from raw milk and UF retentates was 12.5~13.1% equally, but yield efficiency of UF retentate cheese was slightly higher than that of the raw milk cheese. Quantity of whey from retentate cheese was inversely related to VCR. But whey from retentate cheese contained higher percentage of amjor components than that from control milk cheese. In early ripening, the concentrations of lactose and soluble nitrogen compound were higher in retentate cheeses. Lactose content of control milk cheese was 3.49% and that of 2.00:1. 2.25:1, 2.50:1 VCR retentate was 3.77%, 4.89%, 7.03%, respectively. Thus, the more concentrated cheese contained a higher amount of lactose and all the lactose was hyerolyzed durion 35-day ripenion period. Soluble nitrogen compound of control milk cheese was 1.22% and that of UF cheeses was 1.82~2.06%. After 20-day ripening, soluble nitrogen compound increased starply in UF cheese.

• Food Science and Biotechnology
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• 제14권3호
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• pp.380-386
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• 2005

Optimal conditions of ultrafiltration (UF) and nanofiltration (NF) were investigated for separation and concentration of isoflavones and oligosaccharides from Sunmul. Levels of COD, BOD, and suspended solids (SS) in UF and NF permeates were also determined to evaluate effectiveness of these processes for reducing water pollution. Optimal UF operation conditions to achieve minimal fouling and maximal flux were $33-34^{\circ}C$ operating temperature and 2.3-2.4 bar trans-membrane pressure. Recovery yields of isoflavones and oligosaccharides in UF retentate were 11.49-28.16% and 12.77-27.57%, respectively. Increase in volumetric concentration factor (VCF) resulted in more functional compounds of isoflavones and oligosaccharides passing through UF membrane. Total isoflavone and oligosaccharide yields decreased by 3% as VCF increased from 6.0 to 8.0 and from 8.0 to 10.0, while decreased significantly by 10% as VCF decreased from 4.0 to 6.0. Optimal NF operating conditions were 192-195 psig operating pressure at $30-33^{\circ}C$. Total yields of isoflavones and oligosaccharides significantly decreased at VCF 8.0, whereas did not decrease up to VCF 6.0 during NF operation. Therefore, VCF 6.0 was recommended for economical process. COD and BOD decreased by more than 98% after NF process, and SS were not detected after UF process. These results indicated sequential filtration process was useful for separation of isoflavones and oligosaccharides from Sunmul and for reducing water contaminants.

• 한국식품과학회지
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• 제28권2호
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• pp.378-383
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• 1996

감귤과피로부터 다양한 생리활성 효과와 기능적 특성을 갖는 식이섬유(dietary fibers, DF)를 생산하기 위한 회분식 다단계 한외여과 공정에서 최적 분리 조건은 막횡단압력 7.5 psi,막분리 온도 $35^{\circ}C$, 과피추출즙 pH 3.0으로 결정하였으며, MWCO 단계별 flux 측정에서는 YM10이 가장 높은 값을 나타내었으나 retentate 회수율과 DF 함량면에 있어서는 YM100 단계가 더 효율적인 것으로 나타났다. 각 단계별 총식이섬유 (total dietary fiber, TDF) 함량 비교 결과 본래 과피의 TDF 함량은 33.4%, 170 mesh retentate의 TDF 함량은 18.5%, YM100 retentate에서의 TDF 함량은 8.4%로 나타나 거의 대부분의 DF가 예비여과와 YM100단계에서 회수됨을 알 수 있었다.

• Membrane and Water Treatment
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• 제9권1호
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• pp.17-21
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• 2018

A series of laboratory scale experiments were performed to investigate the feasibility of membrane separation technology for natural rubber (NR) wastewater treatment and reuse. Three types of spiral wound membranes were employed in the cross-flow experiments. The NR wastewater pretreated by sand filtration and cartridge filtration was forced to pass through the ultrafiltration (UF), nanofiltration (NF) and reverse osmosis (RO) membranes successively. The UF retentate, which containing abundant proteins, can be used to produce fertilizer, while the NF retentate is rich in quebrachitol and can be used to extract quebrachitol. The permeate produced by the RO module was reused in the NR processing. Furthermore, about 0.1wt% quebrachitol was extracted from the NR wastewater. Besides, the effluent quality treated by the membrane processes was much better than that of the biological treatment. Especially for total dissolved solids (TDS) and total phosphorus (T-P), the removal efficiency improved 53.11% and 49.83% respectively. In addition, the removal efficiencies of biological oxygen demand (BOD) and chemical oxygen demand (COD) exceeded 99%. The total nitrogen (T-N) and ammonia nitrogen (NH4-N) had approximately similar removal efficiency (93%). It was also found that there was a significant decrease in the T-P concentration in the effluent, the T-P was reduced from 200 mg/L to 0.34 mg/L. Generally, it was considered to be a challenging problem to solve for the biological processes. In brief, highly resource utilization and zero discharge was obtained by membrane separation system in the NR wastewater treatment.

• 생명과학회지
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• 제15권1호
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• pp.9-14
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• 2005

난황 단백질의 효소에 의한 가수분해에서 에탄올의 농도가 증가할수록 고형물과 단백질의 회수가 증가함을 알 수 있었다. 이것은 유화층을 에탄올의 증가가 감소시켰기 때문이다. 그러나 가수분해물에서 단백질 함량이나 sialic acid의 함량은 에탄을 농도와는 관계없이 일정하였다. 한외여과 후에 retentate에 대한 에탄올의 영향을 조사하였다. 마찬가지로 고형물의 회수는 에탄을 농도의 증가와 함께 증가하였다. 그리고 retentate에서 sialic acid의 함량은 대략 $2.5\%$정도로 일정하고 에탄올의 농도에 영향을 받지 않았다 이상의 결과로부터 난황 단백질의 효소 가수분해를 통해 sialic acid가 함유된 제품을 얻고자 할 때는 원료 난황단백질에 포함된 에탄올의 함량을 증가시킬수록 높은 수율의 제품을 얻을 수 있다. 본 실험에서는 원료 난황 단백질 중에서 $40\%$의 에탄을 함량까지는 제품 수율이 계속 증가하는 경향을 보였다. 난황 단백질 가수분해물의 한외여과에서 농축단계에서는 막 모듈의 MWCO의 차이에도 불구하고 retentate에서 총 고형물의 회수율은 비슷함을 나타내었으며, 투석에서 회수율은 MWCO가 작을수록 높아지지는 않았다. 제품에서의 sialic acid의 함량은 사용한 모듈에서 약 $2.0\%$를 나타내었다. 이것은 단백질 가수분해물에 비해 5배정도 상승한 결과이다. 본 연구에서 사용된 막 모듈 가운데서 Amicon 모듈이 제품의 회수율과 함량면에서 가장 우수한 특성을 보였다. 결론적으로 난황 단백질의 protease에 의한 가수분해에서 한외여과에 의해 순도를 높일 때 MWCO, 막 모듈의 type 그리고 운전조건 등을 잘 고려해 줄 때 최적의 조업조건을 얻을 수 있었다.

• 한국식품과학회지
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• 제35권1호
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• pp.72-76
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• 2003

회분처리법으로 박층류식 평막 test cell에 의한 재래간장의 한외시험을 실시한 결과 공급액 주입속도별 투과유속의 감소는 용량감소율의 대수값에 비례하여 감소하였고 본 연구에서 사용한 분획분자량 200,000 dalton의 막에 의한 재래간장의 한외여과에서는 1.5L/min의 유속으로 공급액을 주입하는 것이 농도분극화현상을 최소화하면서 장시간 작업할 수 있음을 알 수 있었다. 간장의 한외여과시험에서 간장내의 총질소와 소금성분은 투과유속이 빠를수록 막에 의한 저지율이 더 높아졌고 따라서 500 nm에서의 간장의 흡광도는 더 낮아졌으며 Cu, Mn 및 Mg와 같은 무기성분도 다소 저지되었다. 미생물 균체는 공급간장의 유속에 상관없이 분획분자량 200,000 dalton의 한외여과막으로 100% 저지되었으나 유리아미노산은 거의 저지되지 않아 투과됨을 알 수 있었다.

• Preventive Nutrition and Food Science
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• 제11권2호
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• pp.155-159
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• 2006

Models capable of predicting the product quality of mixed apple and carrot retentates (MACR) have been developed using response surface methodology and used to characterize the effects of processing conditions including average transmembrane pressure (ATP), temperature, and blend ratio. Color, soluble solids, total sugar, vitamin C, acidity, turbidity, and viscosity were used to assess the product quality following the ultrafiltration (UF) process. $L^*-value$ decreased with increased ATP, but the value was not affected by changes in temperature. Blend ratio also greatly influenced the $L^*-value$. Redness ($a^*-value$), on the other hand, was less affected by temperature and ATP. As the ATP and temperature increased, yellowness increased gradually. Soluble solids contents appeared to decrease gradually as the ATP increased for all blend samples, but the effect of temperature seemed to be less. Total sugar content was more affected by temperature than ATP. In general, samples containing 75% carrot had higher amounts of vitamin C regardless of processing conditions. Changes in acidity were also complex and appeared to respond to interactions among ATP, temperature, and blend ratio. Turbidity increased for all samples as both ATP and temperature increased. The higher the amount of carrot in the blend samples, the higher values for turbidity. Although the changes were small, viscosity appeared to increase as the ATP and temperature increased during UF.

• Journal of Dairy Science and Biotechnology
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• 제29권2호
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• pp.1-15
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• 2011

Mozzarella cheese is recently the most consumed cheese in USA, European, South Korea, etc., and also a various different-type Mozzarella cheese could have great market appeal. However, many consumers would be more concerned about the nutritional aspects and physicochemical properties of Mozzarella cheese. Hence, ultrafiltration (UF) as a best tool of solving those concerns has been recognized. The objective of this review's paper would be suggested that the ultrafiltration (UF) techniques could be directly applied for manufacturing various different-type Mozzarella cheese with high physicochemical properties on fulfilling the consumers' various needs and desires for health.

• 한국축산식품학회지
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• 제21권1호
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• pp.32-37
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• 2001

The study investigated the effects of protein concentration, EGTA and strength of hydrostatic pressure on pH, viscosity and turbidity for ultra filtrated skim milk retentates. The results showed that hydrostatic pressure treatments up to 600 MPa did not affect the viscosity of skim milk, while the turbidity of skim milk increased at higher than 200 MPa. Addition of EGTA caused reduction in turbidity of skim milk, two times (2SR) and three times (3SR) concentrated skim milk retentates. Viscosity for 2SR and 3SR increased proportionally to the amount of EGTA, but viscosity of skim milk was not influenced by EGTA. High pressure treatment also did not cause any difference in viscosity and turbidity of skim milk. However, this treatment decreased viscosity and turbidity for 2SR and 3SR. In particular, 200 MPa treatment showed to induce a higher decrease in turbidity compared with 400 MPa.