JP2016173184A - 船舶の液化ガス処理システム - Google Patents
船舶の液化ガス処理システム Download PDFInfo
- Publication number
- JP2016173184A JP2016173184A JP2016114893A JP2016114893A JP2016173184A JP 2016173184 A JP2016173184 A JP 2016173184A JP 2016114893 A JP2016114893 A JP 2016114893A JP 2016114893 A JP2016114893 A JP 2016114893A JP 2016173184 A JP2016173184 A JP 2016173184A
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- Prior art keywords
- gas
- boil
- engine
- liquefied
- stream
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- 239000003949 liquefied natural gas Substances 0.000 claims abstract description 193
- 238000003860 storage Methods 0.000 claims abstract description 146
- 239000000446 fuel Substances 0.000 claims abstract description 101
- 238000012545 processing Methods 0.000 claims description 81
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- 238000011144 upstream manufacturing Methods 0.000 claims description 7
- 239000002826 coolant Substances 0.000 abstract description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 152
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- 238000010586 diagram Methods 0.000 description 22
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- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 3
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 2
- 230000002730 additional effect Effects 0.000 description 2
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- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
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- 238000007667 floating Methods 0.000 description 2
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- 239000001294 propane Substances 0.000 description 2
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- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
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Images
Classifications
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Abstract
Description
とが混合された状態の燃料ガスは気液分離器46に供給され、気体と液体とに分離される。発熱量の高い重炭化水素(HHC)成分の気化温度が相対的に高いため、部分的に気化された燃料ガスで気化されないまま残っている液体状態のLNGには重炭化水素成分の比率が相対的に高くなる。したがって、気液分離器46で液体成分を分離することによって、すなわち重炭化水素成分を分離することによって、燃料ガスのメタン価は高くなることができる。
Claims (13)
- 液化天然ガスを貯蔵する貯蔵タンクと、前記貯蔵タンクに貯蔵されている液化天然ガスを燃料として使用するエンジンとを備えた船舶の液化ガス処理システムであって、
前記貯蔵タンク内で液化天然ガスから発生した後、前記貯蔵タンクから排出されるボイルオフガスの第1ストリームと、
前記第1ストリームのうち燃料として前記エンジンに供給されるボイルオフガスの第2ストリームと、
前記第1ストリームのうち前記エンジンに供給されないボイルオフガスの第3ストリームとを含み、
前記第1ストリームは、圧縮装置で圧縮された後、前記第2ストリームと前記第3ストリームとに分岐し、
前記第3ストリームを熱交換器で前記第1ストリームと熱交換させて液化させることによって、別途の冷媒を用いた再液化装置を使用することなくボイルオフガスを処理できることを特徴とする船舶のボイルオフガス処理システム。 - 前記熱交換器で液化された前記第3ストリームは、減圧手段によって圧力が下げられることを特徴とする請求項1に記載の船舶の液化ガス処理システム。
- 減圧されて気液混合状態になった前記第3ストリームは、前記貯蔵タンクに戻ることを特徴とする請求項2に記載の船舶のボイルオフガス処理システム。
- 減圧されて気液混合状態になった前記第3ストリームのうち、気体成分は前記貯蔵タンクから排出されるボイルオフガスの前記第1ストリームに合流されることを特徴とする請求項2に記載の船舶のボイルオフガス処理システム。
- 前記減圧手段に供給される前記第3ストリームは、前記減圧手段を通過しながら減圧されて気液混合状態になった前記第3ストリームのうち気体成分と共に、前記減圧手段の上流側に設置された冷却器で熱交換されて冷却されることを特徴とする請求項4に記載の船舶の液化ガス処理システム。
- 減圧されて気液混合状態になった前記第3ストリームのうち、液体成分のみを分離して前記貯蔵タンクに戻すために気液分離器が設置されることを特徴とする請求項2に記載の船舶の液化ガス処理システム。
- 前記圧縮装置は、複数個の圧縮シリンダを含むことを特徴とする請求項2に記載の船舶の液化ガス処理システム。
- 前記圧縮装置に含まれた複数個の前記圧縮シリンダのうち一部の圧縮シリンダを通過して圧縮されたボイルオフガスを供給されて使用するボイルオフガス消費手段をさらに含むことを特徴とする請求項7に記載の船舶の液化ガス処理システム。
- 前記熱交換器に送られるボイルオフガスは、前記圧縮装置に含まれた複数個の前記圧縮シリンダのうち一部又は全部を通過して圧縮されたボイルオフガスであることを特徴とする請求項7に記載の船舶の液化ガス処理システム。
- 前記貯蔵タンクに貯蔵された液化天然ガスを強制的に気化させて前記圧縮装置に供給するための強制気化器をさらに含むことを特徴とする請求項1に記載の船舶の液化ガス処理システム。
- 前記貯蔵タンク内のボイルオフガスを前記圧縮装置によって圧縮して前記エンジンに燃料として供給する圧縮機ラインと、
前記貯蔵タンク内のLNGを高圧ポンプによって圧縮して前記エンジンに燃料として供給する高圧ポンプラインとを含むことを特徴とする請求項1に記載の船舶の液化ガス処理システム。 - 前記エンジンは、MEGIエンジン及びDFエンジンを含むことを特徴とする請求項1に記載の船舶の液化ガス処理システム。
- 前記減圧手段は、膨脹バルブ又は膨脹機であることを特徴とする請求項1に記載の船舶の液化ガス処理システム。
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2016
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2018
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