JP2010095574A5 - - Google Patents

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JP2010095574A5
JP2010095574A5 JP2008265611A JP2008265611A JP2010095574A5 JP 2010095574 A5 JP2010095574 A5 JP 2010095574A5 JP 2008265611 A JP2008265611 A JP 2008265611A JP 2008265611 A JP2008265611 A JP 2008265611A JP 2010095574 A5 JP2010095574 A5 JP 2010095574A5
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Japan
Prior art keywords
catalytic cracking
fluid catalytic
catalyst
vacuum gas
temperature
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JP2008265611A
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JP2010095574A (ja
JP5339845B2 (ja
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Priority to JP2008265611A priority Critical patent/JP5339845B2/ja
Priority claimed from JP2008265611A external-priority patent/JP5339845B2/ja
Priority to EP09171103.6A priority patent/EP2177588B1/en
Priority to US12/575,503 priority patent/US9567531B2/en
Priority to CN200910177877.7A priority patent/CN101724452B/zh
Publication of JP2010095574A publication Critical patent/JP2010095574A/ja
Publication of JP2010095574A5 publication Critical patent/JP2010095574A5/ja
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Description

［実施例２］
脱硫減圧軽油を第１の流動接触分解装置を供給し、一段目の流動接触分解を行った（第１工程）。原料油として使用した脱硫減圧軽油の性状を表１に示す。第１の流動接触分解装置における流動接触分解を経て得られたＬＣＯを第２の流動接触分解装置を供給し、二段目の流動接触分解を行った（第２工程）。
原料油として脱硫減圧軽油を使用したこと、並びに、流動接触分解の反応条件を以下のように設定したことの他は、上記実施例１と同様にして一段目及び二段目の流動接触分解を行った。
（第１工程）
反応帯域出口温度：５１０℃、
接触時間２．０秒、
触媒／原料油比：５．２ｗｔ／ｗｔ、
再生帯域の触媒濃厚相の温度：６９５℃。
（第２工程）
反応帯域出口温度：６００℃、
接触時間：０．４秒、
触媒／原料油比：３０ｗｔ／ｗｔ、
再生帯域の触媒濃厚相の温度：６８０℃。
JP2008265611A 2008-10-14 2008-10-14 流動接触分解方法 Active JP5339845B2 (ja)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP2008265611A JP5339845B2 (ja) 2008-10-14 2008-10-14 流動接触分解方法
EP09171103.6A EP2177588B1 (en) 2008-10-14 2009-09-23 Fluid catalytic cracking process
US12/575,503 US9567531B2 (en) 2008-10-14 2009-10-08 Fluid catalytic cracking process, and gasoline and liquefied petroleum gas obtained by the process
CN200910177877.7A CN101724452B (zh) 2008-10-14 2009-10-14 流化催化裂化方法、以及由此获得的汽油和液化石油气

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008265611A JP5339845B2 (ja) 2008-10-14 2008-10-14 流動接触分解方法

Publications (3)

Publication Number Publication Date
JP2010095574A JP2010095574A (ja) 2010-04-30
JP2010095574A5 true JP2010095574A5 (ja) 2011-03-31
JP5339845B2 JP5339845B2 (ja) 2013-11-13

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Family Applications (1)

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JP2008265611A Active JP5339845B2 (ja) 2008-10-14 2008-10-14 流動接触分解方法

Country Status (4)

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US (1) US9567531B2 (ja)
EP (1) EP2177588B1 (ja)
JP (1) JP5339845B2 (ja)
CN (1) CN101724452B (ja)

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US11492255B2 (en) 2020-04-03 2022-11-08 Saudi Arabian Oil Company Steam methane reforming with steam regeneration
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US11583824B2 (en) 2020-06-18 2023-02-21 Saudi Arabian Oil Company Hydrogen production with membrane reformer
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US11814289B2 (en) 2021-01-04 2023-11-14 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via steam reforming
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US11427519B2 (en) 2021-01-04 2022-08-30 Saudi Arabian Oil Company Acid modified red mud as a catalyst for olefin isomerization
US11724943B2 (en) 2021-01-04 2023-08-15 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via dry reforming
US11820658B2 (en) 2021-01-04 2023-11-21 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via autothermal reforming
US11578016B1 (en) 2021-08-12 2023-02-14 Saudi Arabian Oil Company Olefin production via dry reforming and olefin synthesis in a vessel
US11787759B2 (en) 2021-08-12 2023-10-17 Saudi Arabian Oil Company Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel
US11718575B2 (en) 2021-08-12 2023-08-08 Saudi Arabian Oil Company Methanol production via dry reforming and methanol synthesis in a vessel
US11617981B1 (en) 2022-01-03 2023-04-04 Saudi Arabian Oil Company Method for capturing CO2 with assisted vapor compression

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