METHOD OF OPERATING INTERMEDIATE-FRACTION HYDROFINING REACTOR AND INTERMEDIATE-FRACTION HYDROFINING REACTOR
There is provided an operation method of a middle distillate hydrotreating reactor which hydrotreats and hydroisomerizes a middle distillate including components of a boiling point range equivalent to gas oil among FT synthesis hydrocarbons synthesized by the Fisher-Tropsch synthesis reaction, the o...
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Format | Patent |
Language | English French German |
Published |
07.12.2011
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Online Access | Get full text |
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Abstract | There is provided an operation method of a middle distillate hydrotreating reactor which hydrotreats and hydroisomerizes a middle distillate including components of a boiling point range equivalent to gas oil among FT synthesis hydrocarbons synthesized by the Fisher-Tropsch synthesis reaction, the operation method comprising the steps of: bringing the middle distillate into contact with a catalyst to hydrotreat and hydroisomerize the middle distillate to produce hydrotreated middle distillate; measuring the cloud point of the hydrotreated middle distillate flowing out from the middle distillate hydrotreating reactor; and controlling the operating conditions of the middle distillate hydrotreating reactor so that the cloud point comes to a predetermined target value. |
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AbstractList | There is provided an operation method of a middle distillate hydrotreating reactor which hydrotreats and hydroisomerizes a middle distillate including components of a boiling point range equivalent to gas oil among FT synthesis hydrocarbons synthesized by the Fisher-Tropsch synthesis reaction, the operation method comprising the steps of: bringing the middle distillate into contact with a catalyst to hydrotreat and hydroisomerize the middle distillate to produce hydrotreated middle distillate; measuring the cloud point of the hydrotreated middle distillate flowing out from the middle distillate hydrotreating reactor; and controlling the operating conditions of the middle distillate hydrotreating reactor so that the cloud point comes to a predetermined target value. |
Author | NASUNO, KAZUYA |
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DocumentTitleAlternate | PROCÉDÉ DE FONCTIONNEMENT D'UN RÉACTEUR D'HYDRORAFFINAGE D'UNE FRACTION INTERMÉDIAIRE ET RÉACTEUR D'HYDRORAFFINAGE D'UNE FRACTION INTERMÉDIAIRE BETRIEBSVERFAHREN FÜR EINEN REAKTOR ZUR HYDROVERFEINERUNG VON ZWISCHENPRODUKTFRAKTIONEN SOWIE REAKTOR ZUR HYDROVERFEINERUNG VON ZWISCHENPRODUKTFRAKTIONEN |
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RelatedCompanies | JAPAN OIL, GAS AND METALS NATIONAL CORPORATION COSMO OIL CO., LTD INPEX CORPORATION JX NIPPON OIL & ENERGY CORPORATION JAPAN PETROLEUM EXPLORATION CO., LTD NIPPON STEEL ENGINEERING CO., LTD |
RelatedCompanies_xml | – name: JAPAN PETROLEUM EXPLORATION CO., LTD – name: INPEX CORPORATION – name: JX NIPPON OIL & ENERGY CORPORATION – name: JAPAN OIL, GAS AND METALS NATIONAL CORPORATION – name: NIPPON STEEL ENGINEERING CO., LTD – name: COSMO OIL CO., LTD |
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Snippet | There is provided an operation method of a middle distillate hydrotreating reactor which hydrotreats and hydroisomerizes a middle distillate including... |
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SubjectTerms | CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PETROLEUM, GAS OR COKE INDUSTRIES PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA TECHNICAL GASES CONTAINING CARBON MONOXIDE |
Title | METHOD OF OPERATING INTERMEDIATE-FRACTION HYDROFINING REACTOR AND INTERMEDIATE-FRACTION HYDROFINING REACTOR |
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