• Proceedings of the Korea Society for Energy Engineering kosee Conference
• /
• 1996.04a
• /
• pp.136-143
• /
• 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
• /
• v.1 no.1
• /
• pp.87-96
• /
• 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
• /
• v.2 no.2
• /
• pp.215-224
• /
• 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.

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

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

• Journal of Institute of Control, Robotics and Systems
• /
• v.1 no.2
• /
• pp.119-126
• /
• 1995

The purpose of this study is to develop the technique of energy recovery and energy saving by using the optimization of heat exchanger network synthesis. This article proposes a new method of determining the optimal target of a heat exchanger network synthesis problem of which data feature multiple pinch points. The system separation method we suggest here is to subdivide the original system into independent subsystems with one pinch point. The optimal cost target was evaluated and the original pinch rules at each subsystem were employed. The software developed in this study was applied to the Alko prosess, which is an alcohol production process, for the synthesis of heat exchanger network. It was possible to save about 15% of the total annual cost.

• Journal of Energy Engineering
• /
• v.9 no.1
• /
• pp.1-9
• /
• 2000

공정연계를 최소호하는 IGCC 시스템에 대한 개념설계를 수행하였다. 공정분석은 상용코드인 ASPEN PLUS를 이용하였다. 가스화기의 적절한 운전조건을 찾기위하여 가스화기를 경계조건으로 하는 액서지 민감도분석을 통하여 투입되는 슬러리와 산소의 조건을 결정하였다. 또한 , 생성가스 냉각시 현열을 최대한 회수학 ldn하여 , 열교환망을 통하여 급수를 에열하고 가스화플랜트의 각 부분에 공급하도록 공정을 구성하였다. 여분의 가열된 급수는 갑압증발시켜 복합사이클에서 동력을 생성시키는데 사용되어진다. 이와 같은 시스템은 , 가스터빈 -ASU-가스화플랜트의 공기에 의한 공정연계와, HRSG-가스냉각 및 정제시스템 간의 증기연계를 가능한 적게함으로써 공정의 운전성과 경제성을 최적으로 유지할 수 있다. 본 연구에서 제시하는 공정의 경우에, 열효율이 약 39%(고위발열량 기준)으로 나타났으며, 단위 기기 및 단위공정들의 최적화를 통하여 40%의 효율달성이 가능할 것이다.

• Korean Chemical Engineering Research
• /
• v.59 no.1
• /
• pp.60-67
• /
• 2021

This study presented techno-economic analysis of a 500 MWe oxy-coal power plant with CO2 capture. The power plant included a circulating fluidized-bed (CFB), ultra-supercritical steam turbine, flue gas conditioning (FGC), air separation unit (ASU), and CO2 processing unit (CPU). The dry flue gas recirculation (FGR) was used to control the combustion temperature of CFB. One FGR heat exchanger, one heat exchanger for N2 stream exiting ASU, and a heat recovery from CPU compressor were considered to enhance heat efficiency. The decrease in the temperature difference (ΔT) of the FGR heat exchanger that means the increase in heat recovery from flue gas enhanced the electricity and exergy efficiencies. The annual cost including the FGR heat exchanger and FGC cooling water was minimized at ΔT = 10 ℃, where the electricity efficiency, total capital cost, total production cost, and return on investment were 39%, 1371 M$, 90 M$, and 7%/y, respectively.

• Proceedings of the Korea Information Processing Society Conference
• /
• 2021.05a
• /
• pp.474-476
• /
• 2021

전용회선은 두 지역을 독점적으로 사용하는 구조이기 때문에 안정된 품질수준과 보안성이 확보되어 교환 회선의 급격한 증가에도 불구하고 지속적으로 많이 사용하는 회선 방식이다. 하지만 비용이 상대적으로 고가이기 때문에 네트워크 전용회선의 자원을 적절히 배치하고 활용하여 최적의 상태를 유지하는 것이 중요한 요소이다. 이에 본 연구에서는 기업 네트워크에서 사용하는 전용회선의 실제 사용률 데이터를 기반으로 다양한 시계열 데이터 예측 모델을 적용하고 성능을 평가하였다. 일반적으로 통계적인 방법으로 많이 사용하는 평활화 모형 및 ARIMA 모형과 요즘 많은 연구가 되고 있는 인공신경망에 기반한 딥러닝의 대표적인 모델들을 적용하여 각각의 예측에 대한 성능을 측정하고 비교하였다.

• 한국신재생에너지학회:학술대회논문집
• /
• 2009.06a
• /
• pp.731-734
• /
• 2009

KIER has been developed a compact and highly efficient fuel processor which is one of the key component of the residential PEM fuel cells system. The fuel processor uses methane steam reforming to convert natural gas to a mixture of water, hydrogen, carbon dioxide, carbon monoxide and unreacted methane. Then carbon monoxide is converted to carbon dioxide in water-gas-shift reactor and preferential oxidation reactor. A start-up time of the fuel processor is about 1h and CO concentration among the final product is maintained less than 5 vol. ppm. To achieve high thermal efficiency of 80% on a LHV basis, an optimal thermal network was designed. Internal heat exchange of the fuel processor is so efficient that the temperature of the reformed gas and the flue gas at the exit of the fuel processor remains less than $100^{\circ}C$. A compact design considering a mixing and distribution of the feed was applied to reduce the reactor volume. The current volume of the fuel processor is 17L with insulation.