• Journal of Energy Engineering
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• v.21 no.2
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• pp.179-186
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• 2012

A climate change by increase of greenhouse gas is coming to the front by a large issue, and oxy-combustion demonstration project is coming to the attention to one plans for the reduction of carbon dioxide in power generation sector that used a fossil energy in points of time. This paper estimates benefit of electric generation, benefit of greenhouse gas reduction, benefit of environmental pollutant decreasing and domestic and foreign market value-added benefit caused by oxy-combustion demonstration project. Furthermore, this paper attempts to cost-benefit analysis, using NPV, B/C ratio, IRR techniques for oxy-combustion demonstration project. The results indicate that NPV is 681,620million KRW, B/C ratio 1.69 and IRR 21.4%. Accordingly, oxy-combustion demonstration project ensures economic feasibility that the three indicators have exceeded 0, 1.0 and 5.5%. Moreover, uses of the result is useful for the reduction of carbon dioxide in thermal power generation sector of policy decision.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.34 no.11
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• pp.957-964
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• 2010

The deflagration-to-detonation transition (DDT) causes a strong pressure wave that can adversely affect surrounding structures. The pressure generated by multiple detonative pulses is strong enough to cause metal surface erosion and chipping of the edges of bulk structures. In this study, we investigate the damage caused by the DDT phenomenon and perform hydrocode simulations to evaluate the structural damage caused to a metallic pulverized-coal injector used in a pulverized-coal-oxygen combustion furnace. The experimental conditions are selected in order to accurately model the damage caused to metal injectors that are exposed to multiple DDT pulses.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.34 no.1
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• pp.35-43
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• 2010

In this study, an ideal water-recirculated oxy-fuel power generation system is proposed. The results of parametric studies of the performance characteristics of the system are discussed. For a given choice of the turbine inlet temperature, the turbine, which produces power, can be either a gas or a steam turbine. For maximum efficiency, the turbine inlet temperature is selected as the level of state-of-the-art gas turbines and the reheat cycle may be adopted not only to enhance the turbine power but also to maintain dryness of the water with a turbine exhaust temperature that is as high as possible. To obtain a low condensation temperature for a high purity of $CO_2$, a relatively low pressure expansion process may be added. Finally, the performance of the water-recirculated oxy-fuel power generation system is discussed with reference to various operating parameters and system configurations. The optimal operating conditions for high performance and a high purity of $CO_2$ are proposed.

• JOURNAL OF ELECTRICAL WORLD
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• s.425
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• pp.44-49
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• 2012

• Proceedings of the KIEE Conference
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• 2011.07a
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• pp.1848-1849
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• 2011

Oxy-PC 발전시스템은 화석 연료를 연소하는 과정에서 발생하는 다량의 이산화탄소를 회수처리 하기위해 고려되고 있는 방법 중 하나이며, 신규 발전 시스템은 물론이며 기존 발전시스템에도 개조 과정을 거쳐 적용이 용이한 장점이 있다. 하지만 현재 국내에 해당 시스템의 적용 사례는 없을 뿐만 아니라 설계 기술의 확보도 부족한 실정이다. 따라서 순산소 연소 시 발생하는 복합적인 문제를 사전에 예측하고 시스템 구현 과정에서 발생되는 시행착오를 최소화하기 위해서는 순산소 연소 공정모델을 반영한 Dynamic Engineering Simulator 개발이 요구된다. 본 논문에서는 Oxy-PC 발전 시스템의 특징을 기존 공기 연소 발전 시스템과 비교하여 설명하고 Oxy-PC 발전 플랜트용 Dynamic Engineering Simulator 개발 절차에 대해 기술한다.

• Journal of the Korean Society of Combustion
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• v.17 no.3
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• pp.30-45
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• 2012

An existing unit of power plant is considered to refurbish it for possible application of carbon capture and storage(CCS). Conceptual design of the plant includes basic considerations on the national and international situation of energy use, environmental concerns, required budget, and time schedule as well as the engineering concept of the plant. While major equipment of the recently upgraded power plant is going to be reused, a new boiler for air-oxy fired dual mode operation is to be designed. Cryogenic air separation unit is considered for optimized capacity, and combustion system accommodates flue gas recirculation with multiple cleaning and humidity removal units. The flue gas is purified for carbon dioxide separation and treatment. This paper presents the background of the project, participants, and industrial background. Proposed concept of the plant operation is discussed for the possible considerations on the engineering designs.

• Korean Chemical Engineering Research
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• v.56 no.5
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• pp.647-654
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• 2018

In order to solve the global warming and reduce greenhouse gas emissions, it has been developed the $CO_2$ capture technology by oxy-fuel combustion. But there is a problem that the economic efficiency is low because the oxygen production cost is high. ASU (Air Separation Unit) is known to be most suitable method for producing large capacity of oxygen (>2,000 tpd). But most of them are optimized for high purity (>99.5%) oxygen production. If the ASU process is optimized for low purity(90~97%) oxygen producing, it is possible to reduce the production cost of oxygen by improving the process efficiency. In this study, the process analysis and comparative evaluation was conducted for developing large capacity ASU for oxy-fuel combustion. The process efficiency was evaluated by calculating the recovery rate and power consumption according to the oxygen purity using the AspenHysys. As a result, it confirmed that the optimal purity of oxygen for oxyfuel combustion is 95%, and the power consumption can be reduced by process optimization to 12~18%.

• Korean Chemical Engineering Research
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• v.59 no.1
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• pp.60-67
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• 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 KSME Conference
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• 2008.11b
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• pp.3169-3174
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• 2008

Future power plants will be required to adopt some type of carbon capture and storage (CCS) technologies to reduce their CO2 emissions. One of distinguished CCS techniques expected to resolve the green house effect is to apply the oxy-fuel combustion technique to power plant, and a lot of research/demonstration programs have been going on in the world. In this paper, CO2-capturing power plants based on gas turbine and oxy-fuel combustion are investigated over several types of configurations. As a prior step, simulation model for 500 MW-class combined cycle power plant was set and was used as a reference case. The efficiencies of several power plants was compared and the advantages and disadvanteges was investigated.

• Proceedings of the SAREK Conference
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• 2006.11a
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• pp.81-81
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• 2006