KR101717327B1 - 최적 예방보전 주기 계산 시스템 - Google Patents
최적 예방보전 주기 계산 시스템 Download PDFInfo
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- KR101717327B1 KR101717327B1 KR1020140049750A KR20140049750A KR101717327B1 KR 101717327 B1 KR101717327 B1 KR 101717327B1 KR 1020140049750 A KR1020140049750 A KR 1020140049750A KR 20140049750 A KR20140049750 A KR 20140049750A KR 101717327 B1 KR101717327 B1 KR 101717327B1
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- preventive maintenance
- natural gas
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- liquefied natural
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- 238000004364 calculation method Methods 0.000 title claims abstract description 61
- 238000012423 maintenance Methods 0.000 title claims abstract description 61
- 230000003449 preventive effect Effects 0.000 title claims abstract description 58
- 238000004519 manufacturing process Methods 0.000 claims abstract description 83
- 239000003949 liquefied natural gas Substances 0.000 claims abstract description 52
- 238000000034 method Methods 0.000 claims abstract description 19
- 230000008569 process Effects 0.000 claims abstract description 17
- 238000003860 storage Methods 0.000 claims description 32
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 claims description 4
- 238000000342 Monte Carlo simulation Methods 0.000 claims description 4
- 238000004422 calculation algorithm Methods 0.000 claims description 4
- 229940112112 capex Drugs 0.000 claims description 4
- 230000009194 climbing Effects 0.000 claims description 4
- FEBLZLNTKCEFIT-VSXGLTOVSA-N fluocinolone acetonide Chemical compound C1([C@@H](F)C2)=CC(=O)C=C[C@]1(C)[C@]1(F)[C@@H]2[C@@H]2C[C@H]3OC(C)(C)O[C@@]3(C(=O)CO)[C@@]2(C)C[C@@H]1O FEBLZLNTKCEFIT-VSXGLTOVSA-N 0.000 claims description 4
- 238000005457 optimization Methods 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- 238000009826 distribution Methods 0.000 description 7
- 239000003345 natural gas Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000008439 repair process Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/30—Computing systems specially adapted for manufacturing
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Abstract
Description
도 2는 장비의 시간에 따른 신뢰도 분포를 결정하는 Weibull Reliability Function.
도 3은 도 2의 Weibull Reliability Function에 따라 산출된 장비의 시간에 따른 신뢰도 분포곡선.
도 4는 액화천연가스 부유식 생산저장설비 탑사이드 전체 시스템의 생산가용도를 계산하는 개념도.
도 5는 예방보전 주기에 따른 생산가용도 변화를 나타내는 그래프.
도 6은 일반적인 LNG FPSO 다이어그램.
2 : 최적 예방보전 주기 계산 모듈
3 : 비교 모듈
Claims (2)
- 액화천연가스 부유식 생산저장설비 탑사이드 공정의 장비별 고장률 데이터 및 운영비용을 바탕으로 최적의 예방보전 주기를 찾는 시스템으로서,
액화천연가스 부유식 생산저장설비 탑사이드에 설치되는 각 장비의 생산가용도를 계산한 후, 각 장비의 생산가용도를 몬테 카를로 시뮬레이션을 통해 종합하여 액화천연가스 부유식 생산저장설비 탑사이드 공정의 목표 수명 기간 대비 전체 시스템의 생산가용도를 계산하고, 비용 예측 모델을 통해 액화천연가스 부유식 생산저장설비 탑사이드 전체 시스템의 수익을 계산하는, 기본 계산 모듈(1);
최적 예방보전 주기 계산을 수행할 시간구간 범위 및 계산 간격을 설정하고, 설정된 시간구간 범위 및 계산 간격에 따라 전체 시스템의 생산가용도 및 수익을 1차 계산한 후, 1차 계산 결과 중 수익이 최대가 되는 시간구간을 선정하고 힐 클라이밍 최적화 알고리즘을 적용하여 해당 시간구간 중에서도 수익이 최대가 되는 하나의 지점, 즉 최적 예방보전 주기를 찾는, 최적 예방보전 주기 계산 모듈(2) 및;
상기 기본 계산 모듈(1)과 상기 최적 예방보전 주기 계산 모듈(2)의 계산 결과 값을 출력하여 비교하는, 비교 모듈(3);
을 포함하되,
상기 비용 예측 모델은,
(Net Profit) = (LNG Production Rate) × (LNG Price) × (Lifespan) × (Availability) - ∑(CAPEX + OPEX)
의 형태로 이루어지는바, 여기서,
Net Profit : 액화천연가스 부유식 생산저장설비 탑사이드 전체 시스템의 수익,
LNG Production Rate : 연간 LNG 생산량,
LNG Price : LNG 가격,
Lifespan : 액화천연가스 부유식 생산저장설비 탑사이드 공정의 목표 수명 기간,
Availability : 액화천연가스 부유식 생산저장설비 탑사이드 공정의 목표 수명 기간 대비 전체 시스템의 생산가용도,
CAPEX : 투자비용(CAPital EXpenditures),
OPEX : 운영비용(OPerating EXpenditures)
를 의미하는 것을 특징으로 하는, 최적 예방보전 주기 계산 시스템. - 삭제
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KR20240126295A (ko) | 2023-02-13 | 2024-08-20 | 이상선 | 스마트 그리드 자동제어반 예방보전 시스템 |
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WO2012157040A1 (ja) | 2011-05-13 | 2012-11-22 | 株式会社日立製作所 | 保守部品寿命予測システムおよび保守部品寿命予測方法 |
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KR100897595B1 (ko) | 2007-08-14 | 2009-05-14 | 한국광기술원 | 인듐주석산화물 투명전극 직접 접촉층을 포함하는 발광다이오드 및 그의 제조방법 |
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WO2012157040A1 (ja) | 2011-05-13 | 2012-11-22 | 株式会社日立製作所 | 保守部品寿命予測システムおよび保守部品寿命予測方法 |
Non-Patent Citations (2)
Title |
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이순섭 외 1인, 'LNG-FPSO Topside 장비를 위한 보전시스템 개발을 위한 사례 연구', 한국해양공학회지 제28권 제6호, 2014, pp.533-539 |
조상제 외 3인, 'A Study on Estimating the Next Failure Time of a Compressor in LNG FPSO', J. Soc. Korea Ind. Syst. Eng. Vol. 37, No. 4 : 12-23, December 2014. |
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