PL410700A1 - Sposób wytwarzania nierakotwórczego aromatycznego oleju technologicznego - Google Patents

Sposób wytwarzania nierakotwórczego aromatycznego oleju technologicznego

Info

Publication number
PL410700A1
PL410700A1 PL410700A PL41070012A PL410700A1 PL 410700 A1 PL410700 A1 PL 410700A1 PL 410700 A PL410700 A PL 410700A PL 41070012 A PL41070012 A PL 41070012A PL 410700 A1 PL410700 A1 PL 410700A1
Authority
PL
Poland
Prior art keywords
extract
polar solvent
solvent
ratio
production
Prior art date
Application number
PL410700A
Other languages
English (en)
Other versions
PL227839B1 (pl
Inventor
Victor Alekseevich Tsebulaev
Nikolay Vladimirovich Khodov
Andrey Federovich Kuimov
Arkadiy Benyumimovich Radbil
Taras Ivanovich Dolinsky
Oleg Anatolyevich Mazurin
Original Assignee
ORGKHIM Biochemical Holding Management Company Joint Stock Company (ORGKHIM BCH Managament Company, JSC)
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 ORGKHIM Biochemical Holding Management Company Joint Stock Company (ORGKHIM BCH Managament Company, JSC) filed Critical ORGKHIM Biochemical Holding Management Company Joint Stock Company (ORGKHIM BCH Managament Company, JSC)
Publication of PL410700A1 publication Critical patent/PL410700A1/pl
Publication of PL227839B1 publication Critical patent/PL227839B1/pl

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
    • C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20—Organic compounds not containing metal atoms
    • C10G29/28—Organic compounds not containing metal atoms containing sulfur as the only hetero atom, e.g. mercaptans, or sulfur and oxygen as the only hetero atoms
    • 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/02—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents with two or more solvents, which are introduced or withdrawn separately
    • 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12—Organic compounds only
    • C10G21/16—Oxygen-containing 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12—Organic compounds only
    • C10G21/20—Nitrogen-containing 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12—Organic compounds only
    • C10G21/22—Compounds containing sulfur, selenium, or tellurium
    • 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/28—Recovery of used solvent
    • 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
    • C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20—Organic compounds not containing metal atoms

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)
  • Extraction Or Liquid Replacement (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

Wynalazek dotyczy sposobu przetwarzania w przemyśle chemicznym lub naftowym, który może być stosowany do wytwarzania plastyfikatorów ropy naftowej w produkcji kauczuku syntetycznego i opon. Sposób wytwarzania nierakotwórczego aromatycznego oleju technologicznego, zawierającego ekstrakt z PCA mniej niż 3,0% obejmuje oczyszczanie frakcji olejowej ropy naftowej za pomocą selektywnych rozpuszczalników, oddzielenie ekstraktu, dodatkową obróbkę ekstraktu polarnym rozpuszczalnikiem i wytwarzanie rafinatu jako produktu końcowego, gdzie jako polarny rozpuszczalnik stosowana jest mieszanina dwumetylosulfotlenku i N-metylopirolidonu, która jest stosowana do wstępnej obróbki ekstraktu, w którym to sposobie po wstępnej obróbce, mieszanina ekstraktu i polarnego rozpuszczalnika jest odfiltrowywana, rozdzielana i faza lekka jest przesyłana do dodatkowej obróbki ekstraktu polarnym rozpuszczalnikiem, a faza ciężka jest przesyłana do etapu regeneracji polarnego rozpuszczalnika. Stosunek dimetylosulfotlenku do N-metylopirolidonu w mieszaninie mieści się w zakresie od 1 : 0,1 - 0,5. Stosunek polarnego rozpuszczalnika do ekstraktu w dodatkowym etapie obróbki mieści się w zakresie 1,5 - 2,5 : 1. Stosunek polarnego rozpuszczalnika do ekstraktu w etapie wstępnej obróbki mieści się w zakresie 0,1 - 0,3 : 1. Uzyskany techniczny rezultat, polega na zwiększeniu wydajności procesu poprzez zapobieganie tworzeniu się warstwy pośredniej w kolumnie ekstrakcyjnej, poprzez obniżenie proporcji rozpuszczalnik : ekstrakt i w konsekwencji zwiększenie wydajności instalacji, uproszczenie procesu osuszania rozpuszczalnika oraz usuwanie rozpuszczalnika parafino - naftenowego, co znacznie ułatwia regenerację ekstrahenta z roztworu rafinatu.
PL410700A 2012-10-09 2012-10-09 Sposób wytwarzania nie-rakotwórczego aromatycznego oleju technologicznego PL227839B1 (pl)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/RU2012/000815 WO2014058333A1 (ru) 2012-10-09 2012-10-09 Способ получения неканцерогенного ароматического технологического масла

Publications (2)

Publication Number Publication Date
PL410700A1 true PL410700A1 (pl) 2015-11-09
PL227839B1 PL227839B1 (pl) 2018-01-31

Family

ID=50477678

Family Applications (1)

Application Number Title Priority Date Filing Date
PL410700A PL227839B1 (pl) 2012-10-09 2012-10-09 Sposób wytwarzania nie-rakotwórczego aromatycznego oleju technologicznego

Country Status (6)

Country Link
US (1) US9567532B2 (pl)
DE (1) DE112012006987B4 (pl)
PL (1) PL227839B1 (pl)
RU (1) RU2581649C2 (pl)
SG (1) SG11201406859XA (pl)
WO (1) WO2014058333A1 (pl)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3733147A1 (en) 2014-04-21 2020-11-04 Becton Dickinson and Company Limited Fluid transfer device and packaging therefor
JP6952241B2 (ja) 2017-08-29 2021-10-20 パナソニックＩｐマネジメント株式会社 電動工具
RU2659794C1 (ru) * 2018-02-01 2018-07-04 Акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (АО "ВНИИ НП") Способ получения канцерогенно безопасных ароматических наполнителей и пластификаторов каучука и резины
RU2669936C1 (ru) * 2018-04-06 2018-10-17 Публичное акционерное общество "Нефтяная компания "Роснефть" (ПАО "НК "Роснефть") Способ получения пластификатора
RU2690926C1 (ru) * 2018-09-07 2019-06-06 Акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (АО "ВНИИ НП") Способ получения канцерогенно безопасных ароматических наполнителей и пластификаторов каучука и резины
RU2709514C1 (ru) * 2019-10-26 2019-12-18 Общество с ограниченной ответственностью «Компания Петромаруз» Способ получения пластификатора
RU2713156C1 (ru) * 2019-11-07 2020-02-04 Акционерное общество "Управляющая компания "Биохимического холдинга "Оргхим" Способ получения низковязского высоко-ароматического неканцерогенного нефтяного технологического масла

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US5045206A (en) 1990-12-05 1991-09-03 Exxon Research & Engineering Company Selective multi-ring aromatics extraction using a porous, non-selective partition membrane barrier
JP2000063849A (ja) 1998-08-18 2000-02-29 Fuji Kosan Kk 非発ガン性の芳香族炭化水素油の製造法
GB9904808D0 (en) 1999-03-02 1999-04-28 Bp Oil Int Oil treatment process
EP1106673B1 (en) 1999-12-06 2004-10-06 Shell Internationale Researchmaatschappij B.V. Removal of polycyclic aromatic compounds from extracts
BY7326C1 (en) * 2002-07-11 2005-09-30 Belorussky Gosudarstvenny Tekhnologichesky Universitet Method for purifying coal oils
JP2004323544A (ja) 2003-04-21 2004-11-18 Mitsubishi Materials Corp 油に含まれる硫黄化合物の分離方法、油に含まれる硫黄化合物および芳香族炭化水素の分離方法、高オクタン価の脱硫ガソリン基材の製造方法ならびに高オクタン価の脱硫および脱芳香族ガソリン基材の製造方法
RU2279466C1 (ru) 2005-03-14 2006-07-10 Закрытое акционерное общество "Торговый дом "Оргхим" Способ селективной очистки масляных фракций нефти от полициклических ароматических соединений
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Also Published As

Publication number Publication date
PL227839B1 (pl) 2018-01-31
WO2014058333A1 (ru) 2014-04-17
DE112012006987T8 (de) 2015-08-06
DE112012006987T5 (de) 2015-07-09
DE112012006987B4 (de) 2018-11-08
SG11201406859XA (en) 2015-03-30
RU2581649C2 (ru) 2016-04-20
RU2014138414A (ru) 2016-04-10
US9567532B2 (en) 2017-02-14
US20160002543A1 (en) 2016-01-07

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