• Title/Summary/Keyword: Scale-Up

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IPA Analysis of the Components of the Scale-up Entrepreneurial Ecosystem of Startups (스타트업의 스케일업 창업생태계 구성요소의 IPA 분석)

  • Hey-Mi, Yun;Jung-Min, Nam
    • Asia-Pacific Journal of Business Venturing and Entrepreneurship
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    • v.17 no.6
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    • pp.25-37
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    • 2022
  • The purpose of this study is to survey startup founders within 7 years of founding the importance and satisfaction of the components of the scale-up entrepreneurial ecosystem at the national level in Korea and analyze the direction of scale-up policy by component using IPA (importance-performance analysis). Since the perception of founders, who are the subjects of the entrepreneurial ecosystem, affects the quantity and quality of start-ups, research is needed to analyze and diagnose the perception of scale-up components. For the development of the national economy and entrepreneurial ecosystem, companies that emerge from startups to scale-up and unicorns must be produced, and for this, elements for the scale-up entrepreneurial ecosystem are needed. The results of this study are as follows. First, the importance ranking of the components of the scale-up entrepreneurial ecosystem recognized by founders was in the order of "Financial support by growth stage," "Support for customized scale-up for enterprises," "Improvement of regulations," "Funds dedicated to scale-up," "large-scale investment," and "nurturing technical talents." Second, the factors that should be intensively improved in the importance-satisfaction matrix in the future were 'Pan-Government Integration Promotion Plan', 'Scale-Up Specialized Organization Operation', 'Company Customized Scale-Up Support', 'Regulatory Improvement', and 'Building a Korean Scale-Up Model'. As a result, various and large financial capital for the scale-up entrepreneurial ecosystem, diversification of scale-up programs by business sector, linkage of start-ups and scale-up support, deregulation of new technologies and new industries, strengthening corporate-tailored scale-up growth capabilities, and providing overseas networking opportunities can be derived. In addition, it is expected to contribute to policy practice and academic work with research that derives the components of the domestic scale-up entrepreneurial ecosystem and diagnoses its perception.

A Study on Scale-Up Success Factors for ICT Startups: A Case Analysis Using ERIS Model (ICT 스타트업 스케일업 성공요인 연구: ERIS 모델 적용 사례연구)

  • Hwang, Jeong-Seop;Sim, Da-Hyun;Lee, Jungwoo
    • Journal of Digital Convergence
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    • v.19 no.4
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    • pp.89-101
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    • 2021
  • Scale-up of ICT startups is not easy because of limited capabilities, lack of resources, and immature networks for the business. Therefore, this research selected a representative startup succeeded in scale-up and applied the ERIS model in analyzing their scale-up process in the initial stages of scale-up. Analysis of qualitative data collected revealed that the entrepreneurs' experience, convergence of knowledge between diverse industries, participation in public-sector-led R&D, management of communication channels between customers and businesses, and utilization of project-oriented campaigns are found to be critical success factors in scaling up ICT startups. Academically, this study validates the utility of ERIS model in analyzing the scale-up process. For practitioners, this study will be used as a reference for strategic development in seucring the competitiveness of the initial market of ICT startups and scale-up.

Effect of Agitation, Aeration and Scale-up on Mycelial Morphology During Liquid Culture of Ganoderma lucidum (영지의 액체배양 중 균사형태에 미치는 통기.교반의 영향 및 Scale-up)

  • Lee, Hak-Su;Lee, Ki-Young;Choi, Sang-Yun;Lee, Shin-Young
    • KSBB Journal
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    • v.26 no.4
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    • pp.357-364
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    • 2011
  • This study was carried out to investigate the effects of agitation, aeration and scale-up on the mycelial growth, exo-polysaccharide (EPS) production, and mycelial morphology in the liquid culture of Ganoderma lucidum. A correlation between roughness and operating variables was also studied to scale-up the liquid culture of G. lucidum in a jar fermenter. When the agitation speed or aeration rate increased, the morphological form was changed from rough pellet to smooth pellet form. Increase of the agitation and aeration reduced the mycelial roughness. On the other hand, in the case of pellet size, it was not affected by aeration. The higher EPS production was obtained at approximately 17% of roughness and mycelial pellet size of 3~5 mm. The morphology at each fermenter was closely correlated with kLa value, and it was found that similarity of morphology would be used as a criteria of scale-up for liquid culture of G. lucidum.

알콜 발효공정의 scale-up 사례연구

  • 이상기
    • The Microorganisms and Industry
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    • v.16 no.2
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    • pp.53-57
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    • 1990
  • 본고에서는 이제까지 개발되어 현재 산업적으로 사용되고 있는 에탄올 생산공정을 살펴보고 scale-up의 사례로서 KIST 유전공학센터에서 Z.mobilis airlift 발효조에서 수행한 연구결과를 중심으로 에탄올 발효에 있어서 scale-up시 나타나는 문제점과 고려해야 할 제반사항에 대해 살펴 보기로 한다.

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Optimization and Scale-Up of Succinic Acid Production by Mannheimia succiniciproducens LPK7

  • Oh, In-Jae;Kim, Dong-Hyun;Oh, Eun-Kyoung;Lee, Sang-Yup;Lee, Jin-Won
    • Journal of Microbiology and Biotechnology
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    • v.19 no.2
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    • pp.167-171
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    • 2009
  • The effects of culture conditions on succinic acid production and its possible scale-up have been studied. Mannheimia succiniciproducens LPK7, engineered for enhanced production of succinic acid and reduced by-product secretion, was used for the experiments. Mannheimia succiniciproducens LPK7 is a knock-out strain of wild type deficient in the ldhA, pflB, and pta-ackA genes, and is derived from Mannheimia succiniciproducens MBEL55E. Process optimization of factors including optimal temperature, pH, carbon source, and nitrogen source was performed to enhance the production of succinic acid in flasks. To observe scale-up effects, batch fermentation was carried out at various working volumes. At a working volume of 7.0 l, the final succinic acid concentration and yield were 15.4g/l and 0.86g/g. This result shows similar amount of succinic acid obtained in lab-scale fermentation, and it is possible to scale up to larger fermentors without major problems.

Scale-up of Recombinant Hirudin Production from Saccharomyces cerevisiae

  • Kim, Chul-Ho;K. Jagannadha Rao;Youn, Duk-Joong;Rhee, Sang-Ki
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.8 no.5
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    • pp.303-305
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    • 2003
  • Scale-up of hirudin production from Saccharomyces cerevisiae from bench-scale to pilot-scale was carried out based on constant volumetric oxygen transfer coefficient (K$\sub$L/a). Fed-batch mode of cultivation using step-wise feeding strategy of galactose was employed for the production of hirudin in a 30-L and a 300-L pilot-scale fermentor. The final hirudin concentrations were achieved 390 mg/L and 286.1 mg/L, and the volumetric productivities were 80.4% and 90.7% with the 30-L and 300-L fermentors, respectively, compared to the productivity of the 5-L bench-scale fermentor.

Comparative Evaluation of Large-scale Circulating Fluidized Bed (CFB) Boiler Concepts (대용량 순환유동상 보일러 개념 비교평가 기준 정립)

  • Kim, Tae-Hyun;Choi, Sang-Min;Lee, Jong-Min
    • Journal of the Korean Society of Combustion
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    • v.14 no.3
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    • pp.1-15
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    • 2009
  • The circulating fluidized bed (CFB) boiler has some problems to scale up. Several engineering solutions have been proposed by a few suppliers which had advanced CFB technology. Large-scale CFB design concepts from different suppliers were reviewed and compared. Points of the hydrodynamic and heat recovery were summarized and discussed for developing the guideline of the large-scale circulating fluidized bed boilers.

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Scale-up of Flat Panel Photobioreactor considering Hydrodynamics (수력학을 고려한 평판형 광생물 반응기의 스케일업에 관한 연구)

  • Kim, Gwang-Ho;Lee, Dong-Woon;Jeong, Sang-Hwa
    • Journal of the Korean Society of Manufacturing Process Engineers
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    • v.17 no.1
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    • pp.48-56
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    • 2018
  • Due to the growing concerns of energy resource depletion and environmental destruction, the mass production of microalgae has been studied. The scale-up of a photobioreactor (PBR) is required for the mass production of biomass. In this paper, the geometric parameters and oxygen transfer rate (OTR) are considered, to scale up a flat panel photobioreactor (FP PBR). The PBR is designed using the goal-driven optimization (GDO) method to accomplish the scale-up. The local sensitivity of each output parameter with respect to the input parameter is analyzed through the design of experiment (DOE), and the design candidates are evaluated with the screening sampling method. The volumetric mass transfer coefficient is measured by the dynamic method.

An Experimental Study on the Warehouse Mock-up Fire Test (창고 모델 실물화재 특성에 대한 실험적 연구)

  • Kweon, Oh-Sang;Yoo, Yong-Ho;Kim, Heung-Youl
    • Fire Science and Engineering
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    • v.24 no.4
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    • pp.47-54
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    • 2010
  • This study is analyze the damage of warehouse fire accident be made through the fire characteristic database of combustibles and real scale fire test of warehouse mock-up. Combustibles fire tests are carried out for database using RCT (Room Corner Tester) to predict fire growth the goods. A mockup ($3m{\times}3m{\times}2.4m$) of clothes warehouse was built and real scale fire test by LSC (Large Scale Calorimeter) base on the fire characteristic DB. The mock-up of clothes warehouse is made of two type sandwich panels (Glass wool, EPS foam sandwich panel). As a mock-up test result, test 1 (Glass wool sandwich panel) and test 2 (EPS foam sandwich panel) indicating fire growth such as 5 MW, 11 MW of maximum HRR (Heat Release Rate).