• Journal of Microbiology and Biotechnology
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• 제31권3호
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• pp.349-357
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• 2021

Monoclonal antibodies are widely used as diagnostic reagents and for therapeutic purposes, and their demand is increasing extensively. To produce these proteins in sufficient quantities for commercial use, it is necessary to raise the output by scaling up the production processes. This review describes recent trends in high-density cell culture systems established for monoclonal antibody production that are excellent methods to scale up from the lab-scale cell culture. Among the reactors, hollow fiber bioreactors contribute to a major part of high-density cell culture as they can provide a tremendous amount of surface area in a small volume for cell growth. As an alternative to hollow fiber reactors, a novel disposable bioreactor has been developed, which consists of a polymer-based supermacroporous material, cryogel, as a matrix for cell growth. Packed bed systems and disposable wave bioreactors have also been introduced for high cell density culture. These developments in high-density cell culture systems have led to the monoclonal antibody production in an economically favourable manner and made monoclonal antibodies one of the dominant therapeutic and diagnostic proteins in biopharmaceutical industry.

• 한국산업융합학회 논문집
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• 제27권2_2호
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• pp.357-361
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• 2024

Halloysite nanotube (HNT) has a nanotube structure with the chemical formula of Al₂Si₂O₅(OH)₄·nH₂O and is a natural sediment of aluminosilicate. HNT has been used as additive to improve the mechanical properties of epoxy composites with exchange of amine group as a terminal functional group using huge amount of organic solvents. In order to save time and simplify complicated procedures, a dry coating machine was designed and used for amine group exchange in previous research. For better applications, it was conducted with different parameters and with scale up settings. Best condition was found to reduce usage of solvent, time and man power.

• 한국식물생명공학회:학술대회논문집
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• 한국식물생명공학회 2002년도 추계학술대회
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• pp.27-31
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• 2002

Samyang Genex succeeded in commercialization of anticancer agent-paclitaxel by plant cell culture technology. The core technology of Samyang Genex relating paclitaxel production includes cell line development, cell line preservation, cell culture, scale-up technology, and purification technology. On the basis of the research, Samyang Genex built the factory operated by CGMP (current good manufacturing practice). The $paclitaxel-Genexol^{TM}$ is commercially available in Korea, and it will be launched to world market including USA after approval US FDA.

• 한국식물생명공학회:학술대회논문집
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• 한국식물생명공학회 2002년도 춘계학술대회
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• pp.27-31
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• 2002

Samyang Genex succeeded in commercialization of anticancer agent-paclitaxel by plant cell culture technology. The core technology of Samyang Genex relating paclitaxel production includes cell line development, cell line preservation, cell culture, scale-up technology, and purification technology. On the basis of the research, Samyang Genex built the factory operated by CGMP (current good manufacturing practice). The $paclitaxel-Cenexol^{TH}-is$ commercially available in Korea, and it will be launched to world market including USA after approval of US FDA.

• Journal of Plant Biotechnology
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• 제29권1호
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• pp.59-62
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• 2002

Samyang Genex succeeded in commercialization of anticancer agent-paclitaxel by plant cell culture technology. The core technology of Samyang Genex relating paclitaxel production includes cell line development, cell line preservation, cell culture, scale-up technology, and purification technology. On the basis of the research, Samyang Genex built the factory operated by CGMP (current good manufacturing practice). The paclitaxel-Genexol$^{TM}$-is commercially available in Korea, and it will be launched to world market including USA after approval of US FDA.

• 한국미생물·생명공학회지
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• 제48권3호
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• pp.344-357
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• 2020

Streptococcus zooepidemicus 유래의 세포외 고분자물질인 히알루론산(hyaluronic acid) (HA)을 대량 생산하기 위해, 균주 개량, 생산배지 및 배양공정 개발에 관한 연구를 수행하였다. HA 고생산성 변이주를 선별하기 위해 약 99%의 사멸률을 보이는 ethylmethane sulfonate (EMS) 처리조건을 적용해서, 지속적인 random screening 방법으로 고생산성, 고안정성의 변이주들을 선별할 수 있었다. HA를 고농도로 생산하기 위해서는, 이 균주의 생화학 및 배양생리적 특성에 기반한 최적 배지개발이 필수적이라고 판단하여, one-factor-at-a-time (OFAT), full factorial design (FFD), steepest ascent method (SAM) 및 response surface method (RSM) (반응표면분석법)을 순차적으로 적용하여 통계적 배지 최적화 실험을 수행하였다. 최적 배지조성에서 플라스크 배양에 의한 HA 생산성은 5.38 g/l로서, 이전 배지(3.54 g/l)에 비해 약 52% 향상된 생산량을 얻을 수 있었다. 또한 선별된 우량균주와 최적화된 생산배지를 이용하여 5 L 발효조에서 배양공정 최적화 연구를 수행하였다. 이 균주의 생리학적 특성을 고려할 때, HA 생산성을 높이기 위해서는 (배양 중 HA 축적으로 인해 고점도를 띠는) 배양액으로의 충분한 용존산소 공급이 매우 중요한 요인인 것으로 판단되었다. 따라서 용존산소 공급과 밀접하게 관련있는 발효조의 교반시스템(교반 날개 종류, 크기 및 배치 등) 및 교반속도에 대한 최적화 연구를 수행하였다. 그 결과, 교반축 하부에는 Rushton turbine-type, 상부에는 marine-type의 확장된 교반날개(기존 대비 직경 1.3배 확장)가 설치된 경우, 450 rpm에서 강화된 혼합력과 충분한 용존산소 공급으로 인해 HA 생산성이 기존 플라스크 배양 대비 약 1.8배(9.79 vs. 5.38 g/l) 더 높은 것으로 확인되었다. 최종적으로 HA 배양공정의 scale-up 가능성을 확인하기 위해, pilot 규모의 50 L 발효조 배양을 최대 300 rpm의 교반속도에서 수행하였다. 처음으로 시도한 50 L 배양임에도 불구하고, HA 최대 생산성 면에서 볼 때, 5 L 발효조 결과와 거의 동일한 수준(98.5%) (9.11 vs 9.25 g/l)의 생산량을 얻을 수 있었다. 반면 지수기 성장단계인 배양 15시간까지의 50 L 배양의 HA 평균생산속도(r_p)는 0.46 g/l/hr로서 0.62 g/l/hr인 5 L 배양 대비 약 74% 정도에 머무는 것으로 나타났다. 따라서 생산 발효조의 scale-up 시, 생산균주의 전단응력 민감성(shear damage)을 함께 고려하면서, 산소전달계수(k_La)를 기반으로 하는 교반시스템에 대한 체계적인 연구가 진행된다면, HA 생산속도도 증가될 수 있는 긍정적인 결과를 얻을 수 있을 것으로 기대된다.

• KSBB Journal
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• 제22권2호
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• pp.91-96
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• 2007

본 연구에서는 음식폐기물 효소당화액을 BC생산 배지원으로 이용하여, flask정치배양과 50 L로 규모확대한 공기순환배양기에서 BC생산성을 검토하고, 생산된 BC의 제반물성을 조사하였다. 전단력을 낮추기 위해 당화액배지에 agar를 첨가하여 10 L, 50 L 공기순환배양기에서 배양한 결과, 50 L 규모로 scale-up한 반응기에서 5.64 g/L로 10 L 공기순환배양기 (5.84 g/L)에서와 동등한 BC 농도가 얻어져 BC 대량생산에 효과적인 배양방법임이 입증되었다. 50 L 규모로 확대된 공기순환배양기를 이용하는 본 배양 방법은 BC의 저비용 대량생산을 위한 효율적인 생산 방법 중 하나가 되리라 사료된다. 또한, 당화액을 배지로 하여 공기순환 방법으로 제조한 BC의 물성을 정치배양 방법으로 제조한 BC의 물성과 비교 검토한 결과, 공기순환법으로 제조하였을 때 중합도 및 역학적 성질이 약간 저하하였으나 결정성은 비슷하였으며, 배양기 용량의 대소에 따른 물성의 변화는 거의 없었다.

• Environmental Engineering Research
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• 제17권1호
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• pp.3-8
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• 2012

A scaled-up bioconversion of fishmeal wastewater (FMW) into liquid fertilizer was performed five times in a $1m^3$ reactor in order to examine the feasibility of commercialization. The importance of aeration was marked. Analyses indicated that dissolved oxygen (DO) level was closely related to the value of oxidation-reduction potential (ORP) and it was crucial to achieve high-quality liquid fertilizer. When pure oxygen was supplied through four diffusers into the reactor, DO levels and ORP values were maintained over 1.2 mg/L and 0.2 mV, respectively all the time during 52 hr of bioconversion. The pH changed from 6.8 to 5.9. The average removal percentages of chemical oxygen demand ($COD_{Cr}$) and total nitrogen (TN) were 75.0% and 71.6%, respectively. Compared to the result acquired in a 5-L reactor, bioconversion of FMW into liquid fertilizer was achieved in a shorter time under the same removal percentages of $COD_{Cr}$ and TN. The 52-hr culture of inoculated FMW was phytotoxic-free and it possessed comparable fertilizing ability to a liquid fertilizer made from the fish waste in hydroponic culture with amino acid contents of 5.93 g/ 100 g sample. From all the above results, transferring lab-scale data to large-scale production appeared to be successful. As a result, the commercialization of a liquid fertilizer made from FMW was feasible.

• Journal of Microbiology and Biotechnology
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• 제23권9호
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• pp.1308-1321
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• 2013

The emergence of microcarrier technology has brought a renewed interest in anchorage-dependent cell culture for high-yield processes. Well-known in vaccine production, microcarrier culture also has potential for application in other fields. In this work, two types of microcarriers were evaluated for small-scale monoclonal antibody (mAb) production by CHO-K1 cells. Cultures (5 ml) of microporous Cytodex 3 and macroporous CultiSpher-S carriers were performed in vented conical tubes and subsequently scaled-up (20 ml) to shake-flasks, testing combinations of different culture conditions (cell concentration, microcarrier concentration, rocking methodology, rocking speed, and initial culture volume). Culture performance was evaluated by considering the mAb production and cell growth at the phases of initial adhesion and proliferation. The best culture performances were obtained with Cytodex 3, regarding cell proliferation (average $1.85{\pm}0.11{\times}10^6$ cells/ml against $0.60{\pm}0.08{\times}10^6$ cells/ml for CultiSpher-S), mAb production ($2.04{\pm}0.41{\mu}g/ml$ against $0.99{\pm}0.35{\mu}g/ml$ for CultiSpher-S), and culture longevity (30 days against 10-15 days for CultiSpher-S), probably due to the collagen-coated dextran matrix that potentiates adhesion and prevents detachment. The culture conditions of greater influence were rocking mechanism (Cytodex 3, pulse followed by continuous) and initial cell concentration (CultiSpher-S, $4{\times}10^5$ cells/ml). Microcarriers proved to be a viable and favorable alternative to standard adherent and suspended cultures for mAb production by CHO-K1 cells, with simple operation, easy scale-up, and significantly higher levels of mAb production. However, variations of microcarrier culture performance in different vessels reiterate the need for optimization at each step of the scale-up process.

• 한국수소및신에너지학회논문집
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• 제18권4호
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• pp.458-463
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• 2007

An experimental study on scale-up of Electro-electrodialysis(EED) to increase the efficiency of HI decomposition section in the IS(Iodine-Sulfur) process was carried out. The EED stack extends the effective area of the membrane to 20 times of that formerly used in a single EED unit cell. The experiment was carried out using HIx solution($HI:H_2O:I_2=1:8.4{\sim}9:1.85{\sim}1.9$) at $100^{\circ}C$ and various solution flow rates of 20, 30, 40 and 50 cc/min. The increased HI molality in catholyte after one-pass throughout from the EED stack was 3 mol/kg-$H_2O$, 2.2 mol/kg-$H_2O$, 2 mol/kg-$H_2O$ and 1.37 mol/kg-$H_2O$ at 20, 30, 40 and 50 cc/min, respectively. These values satisfied the target of HI molality(the increase of HI molality: 2 mol/kg-$H_2O$) in the IS process for hydrogen production of 20 L/hr.