EA201170972A1 - METHOD OF MANAGING THE REACTOR OF HYDROGENING OF MEDIUM DISTILLATE AND THE REACTOR OF HYDROGENING OF MEDIUM DISTILLATE - Google Patents

METHOD OF MANAGING THE REACTOR OF HYDROGENING OF MEDIUM DISTILLATE AND THE REACTOR OF HYDROGENING OF MEDIUM DISTILLATE

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Publication number
EA201170972A1
EA201170972A1 EA201170972A EA201170972A EA201170972A1 EA 201170972 A1 EA201170972 A1 EA 201170972A1 EA 201170972 A EA201170972 A EA 201170972A EA 201170972 A EA201170972 A EA 201170972A EA 201170972 A1 EA201170972 A1 EA 201170972A1
Authority
EA
Eurasian Patent Office
Prior art keywords
middle distillate
reactor
hydrogening
hydrogenation
medium distillate
Prior art date
Application number
EA201170972A
Other languages
Russian (ru)
Other versions
EA020717B1 (en
Inventor
Кадзуя Насуно
Original Assignee
Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Инпекс Корпорейшн
ДжейЭкс НИППОН ОЙЛ ЭНД ЭНЕРДЖИ КОРПОРЕЙШН
Джапан Петролеум Эксплорейшн Ко., Лтд.
Космо Ойл Ко., Лтд.
Ниппон Стил Инджиниринг Ко., Лтд.
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 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн, Инпекс Корпорейшн, ДжейЭкс НИППОН ОЙЛ ЭНД ЭНЕРДЖИ КОРПОРЕЙШН, Джапан Петролеум Эксплорейшн Ко., Лтд., Космо Ойл Ко., Лтд., Ниппон Стил Инджиниринг Ко., Лтд. filed Critical Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Publication of EA201170972A1 publication Critical patent/EA201170972A1/en
Publication of EA020717B1 publication Critical patent/EA020717B1/en

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
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • 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
    • C10G45/72—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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • 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
    • C10G2300/1048—Middle distillates
    • C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/304—Pour point, cloud point, cold flow properties
    • 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
    • C10G2400/06—Gasoil

Abstract

Предложен способ управления реактором гидрирования среднего дистиллята, в котором протекает гидрирование и гидроизомеризация среднего дистиллята, включающего компоненты с интервалом температур кипения, соответствующим газойлю, помимо углеводородов ФТ синтеза, полученных по реакции синтеза Фишера-Тропша, способ управления включает стадии приведения в контакт среднего дистиллята с катализатором с гидрированием и гидроизомеризацией среднего дистиллята с получением гидрированного среднего дистиллята, измерения температуры помутнения гидрированного среднего дистиллята, вытекающего из реактора гидрирования среднего дистиллята, и регулирование параметров управления реактором гидрирования среднего дистиллята так, чтобы температура помутнения совпала с заранее определенной заданной величиной.A method is proposed for controlling a middle distillate hydrogenation reactor, in which hydrogenation and hydroisomerization of a middle distillate, including components with a boiling range corresponding to gas oil, takes place, in addition to FT synthesis hydrocarbons obtained by the Fischer-Tropsch synthesis reaction, the control method includes the steps of bringing the middle distillate into contact with a catalyst with hydrogenation and hydroisomerization of the middle distillate to obtain a hydrogenated middle distillate, the temperature measurement is cloudy yielding the hydrogenated middle distillate flowing out from the middle distillate hydrogenation reactor, and adjusting the control parameters of the middle distillate hydrogenation reactor so that the cloud point coincides with a predetermined predetermined value.

EA201170972A 2009-01-30 2010-01-21 Operation method of middle distillate hydrotreating reactor, and middle distillate hydrotreating reactor EA020717B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2009020855 2009-01-30
PCT/JP2010/000340 WO2010087135A1 (en) 2009-01-30 2010-01-21 Method of operating intermediate-fraction hydrofining reactor and intermediate-fraction hydrofining reactor

Publications (2)

Publication Number Publication Date
EA201170972A1 true EA201170972A1 (en) 2012-02-28
EA020717B1 EA020717B1 (en) 2015-01-30

Family

ID=42395400

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201170972A EA020717B1 (en) 2009-01-30 2010-01-21 Operation method of middle distillate hydrotreating reactor, and middle distillate hydrotreating reactor

Country Status (10)

Country Link
US (1) US20120006721A1 (en)
EP (1) EP2392635A4 (en)
JP (1) JP5367727B2 (en)
CN (1) CN102300961B (en)
BR (1) BRPI1007530A2 (en)
CA (1) CA2750088C (en)
EA (1) EA020717B1 (en)
MY (1) MY162602A (en)
WO (1) WO2010087135A1 (en)
ZA (1) ZA201105353B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9476000B2 (en) * 2013-07-10 2016-10-25 Uop Llc Hydrotreating process and apparatus
EP3624918A4 (en) 2017-05-17 2021-01-27 Entegris, Inc. Fluidized granular absorbent bed filter

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1417250A (en) * 1964-09-28 1965-11-12 Cie De Raffinage Shell Berre Method and apparatus for measuring the cloud point of liquids
US4347577A (en) * 1980-12-15 1982-08-31 Texaco Inc. Feedstock temperature control system
US4855530A (en) * 1982-05-18 1989-08-08 Mobil Oil Corporation Isomerization process
US4519717A (en) * 1982-06-07 1985-05-28 Gca Corporation On-stream cloud point analyzer
US4428819A (en) * 1982-07-22 1984-01-31 Mobil Oil Corporation Hydroisomerization of catalytically dewaxed lubricating oils
FR2565689B1 (en) * 1984-06-12 1987-11-20 Elf France METHOD AND DEVICE FOR DETERMINING THE POINT OF DISORDER OF A DIESEL
IT1223151B (en) * 1987-11-18 1990-09-12 Agip Petroli PROCESS PERFECTED FOR THE PRODUCTION OF HIGH QUALITY DIESEL FLEXIBLE
WO1994024544A1 (en) * 1993-04-15 1994-10-27 Japan Energy Corporation Method and instrument for measuring cloud point
JP2000235420A (en) * 1998-12-18 2000-08-29 Idemitsu Kosan Co Ltd Controller for petroleum product manufacturing process and its method
EP1284281B1 (en) * 1999-04-06 2009-02-25 Sasol Technology (Proprietary) Limited Synthetic Naphtha Fuel
JP4694126B2 (en) * 2001-08-08 2011-06-08 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ Process for producing hydrocarbon products having a sulfur content of less than 0.05% by weight
US6702937B2 (en) * 2002-02-08 2004-03-09 Chevron U.S.A. Inc. Process for upgrading Fischer-Tropsch products using dewaxing and hydrofinishing
JP2006502306A (en) * 2002-10-08 2006-01-19 エクソンモービル　リサーチ　アンド　エンジニアリング　カンパニー Increase in lubricating oil yield by low hydrogen pressure catalytic dewaxing of paraffin wax
JP3945773B2 (en) 2003-04-23 2007-07-18 株式会社ジャパンエナジー Eco-friendly fuel oil and its manufacturing method
JP4848191B2 (en) * 2006-02-13 2011-12-28 Ｊｘ日鉱日石エネルギー株式会社 Method for hydrotreating synthetic oil
JP5004785B2 (en) 2007-06-12 2012-08-22 キヤノン株式会社 Job log management system, job log management method, and computer program

Also Published As

Publication number Publication date
CN102300961A (en) 2011-12-28
MY162602A (en) 2017-06-30
EP2392635A4 (en) 2012-06-27
CA2750088A1 (en) 2010-08-05
ZA201105353B (en) 2012-09-26
JP5367727B2 (en) 2013-12-11
CN102300961B (en) 2014-10-15
US20120006721A1 (en) 2012-01-12
BRPI1007530A2 (en) 2016-02-16
EA020717B1 (en) 2015-01-30
AU2010209217A1 (en) 2011-09-08
WO2010087135A1 (en) 2010-08-05
EP2392635A1 (en) 2011-12-07
CA2750088C (en) 2014-03-11
JPWO2010087135A1 (en) 2012-08-02

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MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ BY KG MD TJ

MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): KZ TM RU