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BRPI0919437A8 - processo para dar a partida em um reator de hidrotratamento de fração de nafta - Google Patents

processo para dar a partida em um reator de hidrotratamento de fração de nafta

Info

Publication number
BRPI0919437A8
BRPI0919437A8 BRPI0919437A BRPI0919437A BRPI0919437A8 BR PI0919437 A8 BRPI0919437 A8 BR PI0919437A8 BR PI0919437 A BRPI0919437 A BR PI0919437A BR PI0919437 A BRPI0919437 A BR PI0919437A BR PI0919437 A8 BRPI0919437 A8 BR PI0919437A8
Authority
BR
Brazil
Prior art keywords
naphtha
naphtha fraction
hydrotreating
reactor
starting
Prior art date
Application number
BRPI0919437A
Other languages
English (en)
Inventor
Honda Hidekatsu
Tanaka Yuichi
Original Assignee
Cosmo Oil Co Ltd
Inpex Corp
Jx Nippon Oil & Energy Corp
Japan Oil Gas & Metals Jogmec
Japan Petroleum Exploration Co Ltd
Nippon Steel Eng Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cosmo Oil Co Ltd, Inpex Corp, Jx Nippon Oil & Energy Corp, Japan Oil Gas & Metals Jogmec, Japan Petroleum Exploration Co Ltd, Nippon Steel Eng Co Ltd filed Critical Cosmo Oil Co Ltd
Publication of BRPI0919437A2 publication Critical patent/BRPI0919437A2/pt
Publication of BRPI0919437A8 publication Critical patent/BRPI0919437A8/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1022—Fischer-Tropsch products
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4031—Start up or shut down operations
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/44—Solvents
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

"processo para dar a partida em um reator de hidrotratamento de fração de nafta". a invenção refere-se a um processo para dar a partida em um reator para hidrotratamento de fração de nafta que sujeita a fração de nafta obtida em um fracionador por destilação fracionada de compostos hidrocarbonetos produzidos por uma reação de síntese de fischer-tropsch a hidrotratamento, o processo compreendendo: carregar com antecedência um composto hidrocarboneto inativo correspondente à fração de nafta em um separador de vapor-líquido ao qual é transferida nafta hidrogenada, que foi sujeita a hidrotratamento no reator para hidrotratamento de fração de nafta; misturar o composto hidrocarboneto inativo retirado do separador de vaporlíquido e as frações de nafta que são transferidas do fracionador para o reator para hidrotratamento de fração de nafta e fornecer a mistura das frações de nafta e o composto hidrocarboneto inativo para o reator para hidrotratamento de fração de nafta.
BRPI0919437A 2008-09-30 2009-09-25 processo para dar a partida em um reator de hidrotratamento de fração de nafta BRPI0919437A8 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2008254220A JP5296477B2 (ja) 2008-09-30 2008-09-30 ナフサ留分水素化処理反応器のスタートアップ方法
PCT/JP2009/004882 WO2010038394A1 (ja) 2008-09-30 2009-09-25 ナフサ留分水素化処理反応器のスタートアップ方法

Publications (2)

Publication Number Publication Date
BRPI0919437A2 BRPI0919437A2 (pt) 2015-12-15
BRPI0919437A8 true BRPI0919437A8 (pt) 2019-02-19

Family

ID=42073178

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0919437A BRPI0919437A8 (pt) 2008-09-30 2009-09-25 processo para dar a partida em um reator de hidrotratamento de fração de nafta

Country Status (10)

Country Link
US (1) US8951408B2 (pt)
EP (1) EP2351819A4 (pt)
JP (1) JP5296477B2 (pt)
CN (1) CN102165045B (pt)
AU (1) AU2009299341B2 (pt)
BR (1) BRPI0919437A8 (pt)
CA (1) CA2738054C (pt)
EA (1) EA018588B1 (pt)
MY (1) MY159506A (pt)
WO (1) WO2010038394A1 (pt)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5296478B2 (ja) * 2008-09-30 2013-09-25 Ｊｘ日鉱日石エネルギー株式会社 精留塔のスタートアップ方法
WO2011118442A1 (ja) * 2010-03-25 2011-09-29 独立行政法人石油天然ガス・金属鉱物資源機構 精留塔のスタートアップ方法
JP5904703B2 (ja) 2010-08-19 2016-04-20 独立行政法人石油天然ガス・金属鉱物資源機構 反応器の洗浄方法
JP5887063B2 (ja) * 2011-03-30 2016-03-16 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素合成反応装置及びそのスタートアップ方法、並びに炭化水素合成反応システム
FR3072683B1 (fr) * 2017-10-24 2019-10-04 IFP Energies Nouvelles Procede de demarrage d'un procede de production de kerosene et de gazole a partir de composes hydrocarbones produits par synthese fischer-tropsch.
CN114456831B (zh) * 2021-10-22 2023-08-25 宁波中金石化有限公司 一种石脑油加氢处理系统
CN116355650B (zh) * 2021-12-28 2024-10-29 中国石油天然气股份有限公司 有机液体储氢材料及其制备方法

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3257292A (en) * 1963-08-19 1966-06-21 Phillips Petroleum Co Separation of cyclohexane and benzene by distillation
US3253047A (en) * 1963-10-31 1966-05-24 Phillips Petroleum Co Startup procedure for a hydrogenation system
DE19719833A1 (de) * 1997-05-12 1998-11-19 Basf Ag Verfahren zur katalytischen Gasphasenhydrierung von Olefinen
EP1118651B1 (en) 2000-01-21 2005-09-28 BP Corporation North America Inc. Hydrocarbon conversion process
CA2405841C (en) 2000-04-11 2010-02-09 Akzo Nobel N.V. Process for sulphiding an additive-containing catalyst
US20030141221A1 (en) * 2002-01-31 2003-07-31 O'rear Dennis J. Upgrading Fischer-Tropsch and petroleum-derived naphthas and distillates
WO2003064022A1 (en) * 2002-01-31 2003-08-07 Chevron U.S.A. Inc. Upgrading fischer-tropsch and petroleum-derived naphthas and distillates
JP3945773B2 (ja) 2003-04-23 2007-07-18 株式会社ジャパンエナジー 環境対応燃料油とその製造方法
JP2007270063A (ja) 2006-03-31 2007-10-18 Nippon Oil Corp 軽質炭化水素組成物の処理方法、並びに、芳香族炭化水素組成物、芳香族炭化水素、ガソリン及びナフサ
JP4513823B2 (ja) 2007-03-30 2010-07-28 ブラザー工業株式会社 液体容器収容装置
EP2199370A4 (en) * 2007-09-28 2015-11-04 Japan Oil Gas & Metals Jogmec METHODS OF MANUFACTURING SYNTHETIC NAPHTHA

Also Published As

Publication number Publication date
JP2010083998A (ja) 2010-04-15
AU2009299341B2 (en) 2012-11-01
EP2351819A1 (en) 2011-08-03
CA2738054C (en) 2015-10-13
JP5296477B2 (ja) 2013-09-25
CA2738054A1 (en) 2010-04-08
EP2351819A4 (en) 2013-01-02
EA201170497A1 (ru) 2011-12-30
MY159506A (en) 2017-01-13
US8951408B2 (en) 2015-02-10
AU2009299341A1 (en) 2010-04-08
BRPI0919437A2 (pt) 2015-12-15
CN102165045B (zh) 2016-01-20
WO2010038394A1 (ja) 2010-04-08
CN102165045A (zh) 2011-08-24
EA018588B1 (ru) 2013-09-30
US20110207978A1 (en) 2011-08-25

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Legal Events

Date Code Title Description
B07A Technical examination (opinion): publication of technical examination (opinion)
B09B Decision: refusal
B09B Decision: refusal