• Title/Summary/Keyword: 환기기 운전전력

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A study on the ventilation control method of road tunnel for small vehicles (소형차 전용 도로터널의 환기기 제어방안에 대한 연구)

  • Ryu, Ji-Oh;Lee, Hu-Young;Chang, Ji-Don
    • Journal of Korean Tunnelling and Underground Space Association
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    • v.21 no.6
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    • pp.749-762
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    • 2019
  • In recent years, in urban areas, underground of roads are being promoted in order to resolve traffic congestion and to secure green spaces, and due to the low ratio of large vehicles, they are planned or constructed as road tunnels for small cars only. In addition, the tunnels being built in the city is a tendency to be enlarged to play the role of main roads. Accordingly, the capacity of the ventilation system is increasing and various ventilation methods are required, and the importance of maintenance after the completion of the tunnel such as the operating cost of the ventilation system is emphasized. Therefore, the need for optimization of the operation stage for reducing the power consumption of the ventilation system and the study of the ventilation system operation control logic is increasing. In this study, the study on the necessity of the optimization of operation stage and control logic of the ventilation system was carried out to realize the energy-saving operation for the small car only passing through tunnels which is applied of ① jet fan and combination ventilation system (② jet fan + air purifying equipment, ③ jet fan + vertical shaft, ④ jet fan + supply air semi-transverse). As a result of this study, there can be various operating combinations in the case of the combined ventilation system, and even though the amount of ventilation air is the same, the operating power varies greatly according to the operating combinations. It was found that operating the axial fan first rather than the jet fan first operation method has an effect on power saving.

전력계통용 파워일렉트로닉스 기기

  • 대한전기협회
    • JOURNAL OF ELECTRICAL WORLD
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    • s.277
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    • pp.69-77
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    • 2000
  • 최근 전력설비 운용상의 여러 가지 과제에 대한 유망한 해결책으로서 파워일렉트로닉스 기기를 사용한 FACTS(Flexible AC Transmission System)가 주목을 받고 있다. 그 중에서도 자려식 변환기를 사용한 FACTS기기는 계통의 유효전력$\cdot$무효전력을 계통의 상태에 의존하지 않고 자유롭게 제어할 수 있어, 계통운용의 유연성을 비약적으로 확대할 수 있는 가능성이 있다. 미쓰비시전기는 전력기기간 계통에서의 자려식 변환기 응용의 파이어니어로서 1991년 간사이전력(주) 태산개폐소에 80Mvar SVG(전지형 무효전력발생장치)를 납품하였으며 또한 자원에너지청의 ''연계강화기술개발'' 보조사업으로 도쿄전력(주)을 비롯하여 전력회사 각사, 전원개발(주)와 (재)전력중앙연구소의 지도 하에 3단자 BTB(Back to Back) 실증시스템용으로 세계 최초의 6인치 GTO(Gate Turn-off Thyristor)를 사용한 53MVA의 자려식 변환기를 제작납품하여 수백MVA 클래스의 자려식변환기 제작기술을 확립하였다. 또한 최근에는 동사가 개발한 신소자 GCT(Gate Commutated Turn-off Thyristor)는 지금까지 대용량 자려식 변환기의 커다란 과제였던 운전손실을 반감할 수 있을 것으로 기대되고 있다. 한편 배전 분야에서는 전압변동, 고조파, 순간전압강하 등의 과제가 증가하고 있어, 미쓰비시전기는 이에 응할 수 있는 파워일렉트로닉스 기기로서 콤팩트 SVG(Static Var Generator), SSTS(Solid-state Transfer Switch), 액티브필너를 다수 납품하여 전력품질문제 해결에 공헌하고 있다.

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Steam Generator Chemical Cleaning (특집_제25회 한국원자력연차대회 - 증기발생기 화학 세정)

  • D'Annucci, Filippo;Mutius, Bernard
    • Nuclear industry
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    • v.30 no.3
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    • pp.52-56
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    • 2010
  • 증기발생기 2차측 상태는 발전소 운영에 있어 중요한 역할을 수행한다. 기기, 배관 및 열교환기에서 발생되는 침적물은 증기발생기 튜브의 부식 원인이 될 수 있으며, 튜브와 튜브 지지판 사이의 공간을 차단한다. 2차측 침적물에 의한 튜브 파손으로 인해 일부 발전소에서는 강제적으로 발전을 정지하는 사례가 발생하였다. 또한 튜브 지지판의 침적물 축적으로 인해 정상 운전 동안 전력 생산을 감소하게 되는 결과를 초래한 발전소도 있었다. 따라서 증기발생기 2차측 상태 감시와 더불어 증기발생기 부품의 청결 유지는 필수 항목이라 할 수 있다. 웨스팅하우스에서는 증기발생기를 초기 제작 상태로 복구하고 2차측 침적물을 제거하기 위해 EPRI SGOG 증기발생기 화학 세정을 수 년간 이용하고 있다. 본고는 35개 이상의 발전소에서 성공적으로 이용하고 있는 화학 세정 프로세스 개요 및 프로세스를 적용하면서 취득한 경험을 요약한 것이다.

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Performance Evaluation of K-based Solid Sorbents Depending on the Internal Structure of the Carbonator in the Bench-scale CO2 Capture Process (벤치급 CO2 포집공정에서 흡수반응기의 내부구조에 따른 K-계열 고체흡수제의 성능평가)

  • Kim, Jae-Young;Lim, Ho;Woo, Je Min;Jo, Sung-Ho;Moon, Jong-Ho;Lee, Seung-Yong;Lee, Hyojin;Yi, Chang-Keun;Lee, Jong-Seop;Min, Byoung-Moo;Park, Young Cheol
    • Korean Chemical Engineering Research
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    • v.55 no.3
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    • pp.419-425
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    • 2017
  • In this study, the performance characteristics of the K-based sorbents (KEP-CO2P2, KEPCO RI, Korea) has been studied in relation with the heat exchanger structure and shape in a mixing zone of the carbonator in the bench-scale dry $CO_2$ capture process. Two types of heat exchangers (different structure and shape) were used in the carbonator as CASE 1 and CASE 2, in which the experiment has been continuously performed under the same operating conditions. During the continuous operation, working temperature of carbonator was 75 to $80^{\circ}C$, that of regenerator was 190 to $200^{\circ}C$, and $CO_2$ inlet concentration of the feed gas was 12 to 14 vol%. Especially, to compare the dynamic sorption capacity of sorbents, the differential pressure of the mixing zone in the carbonator was maintained around 400 to 500 mm $H_2O$. Also, solid samples from the carbonator and the regenerator were collected and weight variation of those samples was evaluated by TGA. The $CO_2$ removal efficiency and the dynamic sorption capacity were 64.3% and 2.40 wt%, respectively for CASE 1 while they were 81.0% and 4.66 wt%, respectively for CASE 2. Also, the dynamic sorption capacity of the sorbent in CASE 1 and CASE 2 was 2.51 wt% and 4.89 wt%, respectively, based on the weight loss of the TGA measurement results. Therefore, It was concluded that there could be a difference in the performance characteristics of the same sorbents according to the structure and type of heat exchanger inserted in the carbonator under the same operating conditions.

Techno-economic Analysis and Environmental Impact Assessment of a Green Ammonia Synthesis Process Under Various Ammonia Liquefaction Scenarios (암모니아 액화 시나리오에 따른 그린암모니아 합성 공정의 경제성 및 환경 영향도 평가)

  • Gunyoung Kim;Yinseo Song;Boram Gu;Kiho Park
    • Korean Chemical Engineering Research
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    • v.62 no.2
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    • pp.163-172
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    • 2024
  • In this study, two different scenarios for ammonia liquefaction in the green ammonia manufacturing process were proposed, and the economic-feasibility and environmental impact of each scenario were analyzed. The two liquefaction processes involved gas-liquid separation before cooling at high pressure (high pressure cooling process) or after decompression without the gas-liquid separation (low pressure cooling process). The high-pressure cooling process requires higher capital costs due to the required installation of separation units and heat exchangers, but it offers relatively lower total utility costs of 91.03 $/hr and a reduced duty of 2.81 Gcal/hr. In contrast, although the low-pressure cooling process is simpler and cost-effective, it may encounter operational instability due to rapid pressure drops in the system. Environmental impact assessment revealed that the high-pressure cooling process is more environmentally friendly than the low-pressure cooling process, with an emission factor of 0.83 tCO2eq less than the low-pressure cooling process, calculated based on power usage. Consequently, the outcomes of this study provide relevant scenario and a database for green ammonia synthesis process adaptable to various process conditions.