• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1996.04a
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• pp.136-143
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• 1996

본 연구에서는 정유공정의 한 부부인 demethanizer의 core exchanger 주위 열교환기들에 대해 핀치설계법(pinch desgin method)을 이용하여 새로운 열교환망 합성을 수행하였다. 이로부터 초기에 설정했던 최소접근온도차가 총비용, 즉, 장치비와 에너지 비용에 결정적인 역할을 하는 것으로 확인되었다. 따라서, 본 연구에서는 이 총비용의 목표값이 최소가 되는 최적 최소접근온도차가 존재하고, 이로부터 열교환망 합성이 수행되어져야 최적의 열교환망 합성이 이루어져야 한다는 결론을 얻었다.

• Journal of Energy Engineering
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• v.1 no.1
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• pp.87-96
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• 1992

Two major difficulties with finding an optimal solution to the heat exchanger network synthesis problems are the large solutionspace and the uncertainty in the formulation of the annual cost function. In this work, to overcome the first difficulty a problem reduction technique was developed. The second difficulty was also removed by dividing the annual cost function into four cost items. The optimal network structure for minimum equipment cost is then obtained by repeatedly applying the problem reduction technique and the heuristics in turn. The efficiency and the superiority of the method is demonstrated by examining two selected example problems.

• Journal of Energy Engineering
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• v.4 no.1
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• pp.13-22
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• 1995

공정산업에서 열교환망의 최적화를 통한 에너지 회수 및 절감 기술의 개발을 목적으로, 여러 개의 핀치를 갖거나 또는 안전 및 배열 등과 같은 제약조건들이 주어진 계를 대상으로, 계의 분리법(system separation method)을 적용하여 신뢰도가 높은 목표값(target)을 설정하는 연구의 일환이다. 본 연구에서는 그 목표값의 10% 이내에 도달할 수 있도록 실제적인 열교환망 합성을 수행하는 프로그램 개발에 중점을 두었으며, 조업 중인 기존 공정에 적용해 본 결과, 연간 총비용의 15% 정도를 절감할 수 있는 결과를 얻을 수가 있었다.

• Journal of Energy Engineering
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• v.2 no.2
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• pp.215-224
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• 1993

Heat exchanger network synthesis is very useful to aspects of energy recovery and saving. In order to obtain the optimal network structure for minimum utility cost, multiple utilities were used. In this study, the practical matches of process streams were not considered, but only evaluation of targets was demonstrated. The program developed in this work was applied to the alcohol production process and it was possible to find the optimal cost targets.

• Journal of the Korean Institute of Gas
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• v.28 no.1
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• pp.1-10
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• 2024

In this study, we constructed a process simulation model for an agricultural by-products based Solid Oxide Fuel Cell (SOFC) combined heat and power generation system as part of the introduction of technology for energy self-sufficiency in the agricultural sector. The aim was to reduce the burden of increasing fuel and electricity consumption due to rapid fluctuations in international oil prices and the expansion of smart farming in domestic farms, while contributing to the national greenhouse gas reduction goals. Based on the experimental results of 0.3 ton/day torrefied agricultural by-product gasification experiment, a model for an agricultural by-product-based SOFC cogeneration system was constructed, and optimization of the heat exchange network was conducted for SOFC capacities ranging from 4 to 20 kW. The results indicated that an 8 kW agricultural by-product-based SOFC cogeneration system was optimal under the current system conditions. It is anticipated that these research findings can serve as foundational data for future commercial facility design.

• Proceedings of the Korea Information Processing Society Conference
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• 2000.10b
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• pp.1129-1132
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• 2000

최근 인터넷 수요의 증가로 통신망에서 음성, 영상 및 데이터(data)를 복합적으로 지원할 수 있는 멀티서비스(multiservice)의 교환 기술이 필수적이다. 또한 망 사업자들이 여러 벤더(vendor)들로부터 최적의 장비를 선택하여 망을 구축할 수 있도록 통신 장비들의 상호 운용성을 지원하는 개방형 구조의 망 및 스위치 시스템(switch system)을 정의하는 작업이 필요하다. 페트리 넷(Petri Nets)은 시스템(system)을 분석하기 위한 도구로서, 시스템은 페트리 넷 이론에 의해 시스템의 수학적 표현인 페트리 넷으로 설계될 수 있다. CPN(Colored Petri Nets)은 페트리넷의 확장형으로서, 토근(token)에 칼라를 부여하여 다양한 특성을 지닌 시스템을 표현하기에 적합하다. Design/CPN은 CPN의 사용을 지원하는 소프트웨어 패키지(software package)이다. 본 논문에서는 개방형 멀티서비스 교환 시스템의 핵심으로 스위치와 제어기(Controller) 사이의 표준 프로토콜인 GSMP(General Switch Management Protocol) 프로토콜을 Design/CPN 으로 변환하고, 이로부터 시험열을 생성한다.

• 한국신재생에너지학회:학술대회논문집
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• 2009.11a
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• pp.207-207
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• 2009

Aspen plus는 Aspentech사에서 개발한 공정모사용 프로그램으로서 다양한 화학종의 열역학적 자료를 기반으로 공정설계, 공정최적화, 공정모니터링 등 공정개발에 활용되고 있다. 연료개질기는 수증기 개질반응, 수성가스전이반응, 선택적화학반응으로 구성된 소규모 수소생산공정에 해당된다. 따라서 Aspen 전산모사를 통해 다양한 조건에서의 운전결과를 모사하여 개질기에 미치는 영향을 분석함으로써 운전조건을 최적화 할 수 있다. 연료개질기의 성능에 영향을 미치는 주요인자는 주로 수증기개질 촉매층 출구온도 및 수증기/탄소 비이다. 수증기개질 촉매층의 출구온도를 $660{\sim}740^{\circ}C$로 변화시키면서 개질가스의 조성, 카본 전환율, 개질효율 등을 비교 분석하였다. 또한 수증기/탄소 비를 3~5의 범위에서 변화시키면서 영향을 살펴보았다. 수증기개질 촉매층의 온도가 높을수록 수소생산량이 증가에 따른 효율 증가가 나타났으며 수증기/탄소 비가 증가할 경우에도 개질효율에 긍정적인 영향을 미치는 것을 확인하였다. 하지만 실제 개질기의 운전에서는 소재의 제약에 따라 운전 온도에 제약이 있으며 수증기/탄소비의 증가 역시 개질기의 부피 증가로 이어지는 단점이 있다는 것을 고려해야 한다. 따라서 반응기 재질, 크기, 운전온도와 개질효율과의 상관관계를 파악하여 개질기의 특성을 최적화 하여야 한다.

• Journal of the Korea Society of Computer and Information
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• v.1 no.1
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• pp.25-36
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• 1996

We have analyzed the reliability of failure models In grid topology circuit switched networks. These models are grid topology circuit_ switched networks. and each node transmits packets to object node using flooding search routing method. We hypothesized that the failure of each link Is Independent. We have analyzed for the performance estimation of failure models It using joint probability method to the reliability of a small grid topology circuit switched network. and compared analytic output with simulated output. Also. We have evaluated the reliability of networks using call blocking Probability occurred in circuit switched networks.

• Plant Journal
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• v.12 no.2
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• pp.24-30
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• 2016

The membrane separation processes have received attention due to advantages such as compactness, modularity, ease of installation, flexibility of operation, lower capital cost and lower energy consumption. In this study, we evaluated accuracy of cross-flow, co-current and counter-current models. With the most accurate model, we identified the operating conditions of the two-stage membrane separation and examined the effects of permeance and selectivity of the membrane by simulation. Futhermore, power requirements and operating cost savings due to the introduction of the heat exchanger were investigated by applying heat exchanger network synthesis technique in the two-stage membrane separation using vapor sweep.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.31 no.6B
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• pp.507-514
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• 2011

A numerical model has been developed by employing a finite element method to simulate the depth-averaged 2-D dispersion of the heat pollutant, which is an important pollutant material in natural streams. Among the finite element methods, the Streamline Upwind/Petrov Galerkin (SUPG) method was applied. Also both linear and quadratic elements can be applied so that irregular river boundaries can be easily represented. To show the movement of heat pollutants, the reaction term describing heat transfer was represented as an equation in which sink/source term is proportional to the difference between the equilibrium temperature and water surface temperature. The equation was expressed so that the water surface temperature changes according to the temperature transfer coefficient and the equilibrium temperature. For the calibration of the model developed, analytic and numerical results from a case of rectangular channel with full width continuous injection have been compared in a steady state. The comparisons showed that the numerical results were in good agreement with analytical solutions. The application site was selected from the downstream of Paldang dam to Jamsil submerged weir, and overall length of this site is about 22.5 km. The change of water temperature caused by the discharge from the Guri sewage treatment plant has been simulated, and results were similar to the observed data. Overall it is concluded that the developed model can represent the water temperature changes due to heat transport accurately. But the verification using observed data will further enhance the validity of the model.