BRPI0717585B8 - processo para craqueamento térmico de óleo pesado de petróleo - Google Patents

processo para craqueamento térmico de óleo pesado de petróleo

Info

Publication number
BRPI0717585B8
BRPI0717585B8 BRPI0717585A BRPI0717585A BRPI0717585B8 BR PI0717585 B8 BRPI0717585 B8 BR PI0717585B8 BR PI0717585 A BRPI0717585 A BR PI0717585A BR PI0717585 A BRPI0717585 A BR PI0717585A BR PI0717585 B8 BRPI0717585 B8 BR PI0717585B8
Authority
BR
Brazil
Prior art keywords
petroleum oil
heavy petroleum
thermal cracking
installation
train
Prior art date
Application number
BRPI0717585A
Other languages
English (en)
Inventor
Tamagawa Atsushi
Takeuchi Hisao
Shibutani Isao
Maehara Keiji
Nomura Makoto
Original Assignee
Chiyoda Corp
Fuji Oil 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 Chiyoda Corp, Fuji Oil Co Ltd filed Critical Chiyoda Corp
Publication of BRPI0717585A2 publication Critical patent/BRPI0717585A2/pt
Publication of BRPI0717585B1 publication Critical patent/BRPI0717585B1/pt
Publication of BRPI0717585B8 publication Critical patent/BRPI0717585B8/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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
    • C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
    • 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
    • C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel 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
    • C10G7/00—Distillation of hydrocarbon oils
    • C10G7/12—Controlling or regulating
    • 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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
    • C10G9/18—Apparatus
    • C10G9/20—Tube furnaces
    • 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
    • C10G2300/80—Additives
    • C10G2300/805—Water
    • C10G2300/807—Steam

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)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

processo de craqueamento térmico e instalação para óleo pesado de petróleo. a presente invenção refere-se a um processo para craqueamento térmico de óleo pesado de petróleo, em que quando uma instalação de craqueamento térmico que tem um forno de craquea-mento, dois ou mais trens que compreendem dois vasos de reação e uma torre de destilação é operada, cada trem é operado repetindo-se um ciclo que compreende o desenho do óleo pesado de petróleo a partir do forno de craqueamento que alimenta o óleo pesado de petróleo extraído no primeiro vaso e reação e, então que alimenta o óleo pesado de petróleo extraído no segundo vaso de reação, o vapor é colocado diretamente em contato com o óleo pesado de petróleo a ser termicamente craqueado e as substâncias craqueadas gasosas produzidas e vapor são introduzi-dos na torre de destilação para serem destilados e separados, sendo que o atraso de fase é pro-porcionado para o ciclo repetido em cada trem, de modo que a instalação de craqueamento tér-mico seja operada com o tempo de iniciação diferente da alimentação no primeiro vaso de reação em cada trem. de acordo com a presente invenção, a instabilidade da quantidade de fluxo de entrada das substâncias gasosas na torre de destilação é aperfeiçoada e o aperfeiçoamento do desempenho de separação, o aumento da capacidade de processamento da instalação e simila-res podem ser obtidos.
BRPI0717585A 2006-09-28 2007-08-29 processo para craqueamento térmico de óleo pesado de petróleo BRPI0717585B8 (pt)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2006264138A JP5038674B2 (ja) 2006-09-28 2006-09-28 石油系重質油の熱分解処理方法および熱分解処理装置
JP2006-264138 2006-09-28
PCT/JP2007/066753 WO2008038490A1 (fr) 2006-09-28 2007-08-29 procÉdÉ de craquage thermique de l'huile lourde dÉrivÉe du pÉtrole et appareil de craquage thermique utilisable À cet effet

Publications (3)

Publication Number Publication Date
BRPI0717585A2 BRPI0717585A2 (pt) 2013-10-29
BRPI0717585B1 BRPI0717585B1 (pt) 2018-10-23
BRPI0717585B8 true BRPI0717585B8 (pt) 2020-10-06

Family

ID=39229929

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0717585A BRPI0717585B8 (pt) 2006-09-28 2007-08-29 processo para craqueamento térmico de óleo pesado de petróleo

Country Status (9)

Country Link
US (1) US8277640B2 (pt)
EP (1) EP2072602B1 (pt)
JP (1) JP5038674B2 (pt)
CN (1) CN101517039B (pt)
BR (1) BRPI0717585B8 (pt)
CA (1) CA2663630C (pt)
MX (1) MX2009002394A (pt)
RU (1) RU2423408C2 (pt)
WO (1) WO2008038490A1 (pt)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9101855B2 (en) 2012-01-20 2015-08-11 Fluor Technologies Corporation Optimum net wash oil flow rate in crude vacuum distillation units
US10469342B2 (en) * 2014-10-10 2019-11-05 Nicira, Inc. Logical network traffic analysis

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3928170A (en) 1971-04-01 1975-12-23 Kureha Chemical Ind Co Ltd Method for manufacturing petroleum pitch having high aromaticity
JPS5036441B1 (pt) * 1971-04-01 1975-11-25
JPS5247004A (en) 1975-10-14 1977-04-14 Kureha Chem Ind Co Ltd Cracking of petroleum heavy oil
JPS5397003A (en) 1977-02-04 1978-08-24 Chiyoda Chem Eng & Constr Co Ltd Thermal cracking treatment of petroleum heavy oil
US4242196A (en) * 1978-10-27 1980-12-30 Kureha Kagaku Kogyo Kabushiki Kaisha Mass production system of highly aromatic petroleum pitch
US4522703A (en) * 1981-07-08 1985-06-11 Mobil Oil Corporation Thermal treatment of heavy hydrocarbon oil
FI65274C (fi) 1982-06-14 1984-04-10 Neste Oy Foerfarande foer termisk krackning av kolvaeteolja
DE3335777A1 (de) * 1982-11-17 1984-05-17 VEB "Otto Grotewohl" Böhlen, DDR 7202 Böhlen Verfahren zur erzeugung von olefinen in roehrenpyrolysereaktoren
JPS59109590A (ja) 1982-12-15 1984-06-25 Kureha Chem Ind Co Ltd 石油系重質油の熱分解処理方法
JPH07116450B2 (ja) * 1987-05-30 1995-12-13 富士石油株式会社 重質油の熱分解処理方法
JP2861031B2 (ja) 1988-04-26 1999-02-24 三菱化学株式会社 反応器の制御方法
JPH0816450B2 (ja) 1992-04-21 1996-02-21 川崎重工業株式会社 ２サイクルエンジンの排気装置
JP3415227B2 (ja) 1993-10-28 2003-06-09 敏夫 淡路 有害物除去装置
JPH11263982A (ja) * 1998-03-17 1999-09-28 Yokogawa Electric Corp スタートアップ／シャットダウンの運転制御装置

Also Published As

Publication number Publication date
US20100018897A1 (en) 2010-01-28
EP2072602A1 (en) 2009-06-24
CA2663630A1 (en) 2008-04-03
EP2072602B1 (en) 2018-05-02
CN101517039A (zh) 2009-08-26
JP5038674B2 (ja) 2012-10-03
EP2072602A4 (en) 2014-03-05
BRPI0717585A2 (pt) 2013-10-29
MX2009002394A (es) 2009-05-15
JP2008081628A (ja) 2008-04-10
CA2663630C (en) 2013-12-24
RU2009109852A (ru) 2010-09-27
US8277640B2 (en) 2012-10-02
RU2423408C2 (ru) 2011-07-10
WO2008038490A1 (fr) 2008-04-03
BRPI0717585B1 (pt) 2018-10-23
CN101517039B (zh) 2012-10-03

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Legal Events

Date Code Title Description
B06A Patent application procedure suspended [chapter 6.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 10 (DEZ) ANOS CONTADOS A PARTIR DE 23/10/2018, OBSERVADAS AS CONDICOES LEGAIS.

B16C Correction of notification of the grant [chapter 16.3 patent gazette]

Free format text: REF. RPI 2494 DE 23/10/2018 QUANTO AO ENDERECO.

B21F Lapse acc. art. 78, item iv - on non-payment of the annual fees in time

Free format text: REFERENTE A 16A ANUIDADE.

B24J Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)

Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2737 DE 20-06-2023 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013.