JP2019052134A5 - - Google Patents

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Publication number
JP2019052134A5
JP2019052134A5 JP2018120514A JP2018120514A JP2019052134A5 JP 2019052134 A5 JP2019052134 A5 JP 2019052134A5 JP 2018120514 A JP2018120514 A JP 2018120514A JP 2018120514 A JP2018120514 A JP 2018120514A JP 2019052134 A5 JP2019052134 A5 JP 2019052134A5
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JP
Japan
Prior art keywords
fatty acid
alcohol
base oil
oil composition
synthetic base
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
JP2018120514A
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Japanese (ja)
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JP2019052134A (en
Filing date
Publication date
Priority claimed from KR1020170116244A external-priority patent/KR101853036B1/en
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Publication of JP2019052134A publication Critical patent/JP2019052134A/en
Publication of JP2019052134A5 publication Critical patent/JP2019052134A5/ja
Pending legal-status Critical Current

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Claims (9)

758mmHG以下で150℃から250℃まで温度条件を変化させながら脂肪酸C8〜C12の含有量が0.3重量%以下に精製された脂肪酸を用意するステップと、
前記精製された脂肪酸とアルコールとのエステル反応を行うステップと、
未反応の反応物質を除去するステップと
を含む,
精製された脂肪酸を利用した合成基油組成物の製造方法。
A step of preparing a fatty acid purified to a content of fatty acids C8 to C12 of 0.3% by weight or less while changing the temperature condition from 150 ° C. to 250 ° C. at 758 mmHG or less .
The step of transesterifying the purified fatty acid with alcohol,
Including steps to remove unreacted reactants,
A method for producing a synthetic base oil composition using purified fatty acids.
前記精製された脂肪酸を用意するステップにて精製された脂肪酸は、C8〜C10の含有量が0重量%である請求項1に記載の精製された脂肪酸を利用した合成基油組成物の製造方法。 The method for producing a synthetic base oil composition using the purified fatty acid according to claim 1, wherein the fatty acid purified in the step of preparing the purified fatty acid has a content of C8 to C10 of 0% by weight. .. 前記アルコールは、トリデシル(tridecyl)アルコール、テトラデシル(tetradecyl)アルコール、ペンタデシル(pentadecyl)アルコール、ヘキサデシルアルコール、1-ヒドロキシトリデシルアルコール、1-ヒドロキシペンタデシルアルコール、イソヘキサデシル(isohexadecyl)アルコール、イソステアリル(isostearyl)アルコール、イソトリデシルアルコール及びネオペンチルグリコールからなる群から選択される請求項1に記載の精製された脂肪酸を利用した合成基油組成物の製造方法。 The alcohols include tridecyl alcohol, tetradecyl alcohol, pentadecyl alcohol, hexadecyl alcohol, 1-hydroxytridecyl alcohol, 1-hydroxypentadecyl alcohol, isohexadecil alcohol, and isostearyl. The method for producing a synthetic base oil composition using the purified fatty acid according to claim 1, which is selected from the group consisting of (isostaryl) alcohol, isotridecyl alcohol and neopentyl glycol. 前記精製された脂肪酸とアルコールとのエステル反応を行うステップでは、
温度を180℃で1時間維持、200℃で1時間維持、及び230℃で1時間維持しながら最終的に250℃まで昇温して行うことである請求項1に記載の精製された脂肪酸を利用した合成基油組成物の製造方法。
In the step of transesterifying the purified fatty acid with an alcohol,
The purified fatty acid according to claim 1, wherein the temperature is maintained at 180 ° C. for 1 hour, 200 ° C. for 1 hour, and 230 ° C. for 1 hour while finally raising the temperature to 250 ° C. A method for producing a synthetic base oil composition used.
前記未反応の反応物質を除去するステップは、
730mmHg以下の圧力で5時間ないし10時間の間に維持するステップと、
20℃ないし50℃に冷却させるステップと
を含む請求項1に記載の精製された脂肪酸を利用した合成基油組成物の製造方法。
The step of removing the unreacted reactant is
A step of maintaining at a pressure of 730 mmHg or less for 5 to 10 hours, and
The method for producing a synthetic base oil composition using a purified fatty acid according to claim 1, which comprises a step of cooling to 20 ° C. to 50 ° C.
前記精製された脂肪酸を用意するステップでは、吸着剤を利用する請求項1に記載の精製された脂肪酸を利用した合成基油組成物の製造方法。 The method for producing a synthetic base oil composition using the purified fatty acid according to claim 1, wherein in the step of preparing the purified fatty acid, an adsorbent is used. 請求項1ないし6のうち、いずれか一項に記載の製造方法によって製造された合成基油組成物。 A synthetic base oil composition produced by the production method according to any one of claims 1 to 6 . 前記合成基油組成物の引火点は、260℃以上である請求項に記載の合成基油組成物。 The synthetic base oil composition according to claim 7 , wherein the flash point of the synthetic base oil composition is 260 ° C. or higher. 前記合成基油組成物の粘度は、40℃で14ないし19cStである請求項に記載の合成基油組成物。 The synthetic base oil composition according to claim 7 , wherein the viscosity of the synthetic base oil composition is 14 to 19 cSt at 40 ° C.
JP2018120514A 2017-09-12 2018-06-26 Manufacturing method of functional synthetic oil using purified aliphatic acid, and functional synthetic oil manufactured thereby Pending JP2019052134A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2017-0116244 2017-09-12
KR1020170116244A KR101853036B1 (en) 2017-09-12 2017-09-12 A method for producing a functional synthetic oil using purified fatty acid and a functional synthetic oil using the same

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JP2017184247A Division JP6434105B1 (en) 2017-09-12 2017-09-26 Method for producing functional synthetic oil using refined fatty acid and functional synthetic oil produced thereby

Publications (2)

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JP2019052134A JP2019052134A (en) 2019-04-04
JP2019052134A5 true JP2019052134A5 (en) 2020-11-12

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JP2017184247A Expired - Fee Related JP6434105B1 (en) 2017-09-12 2017-09-26 Method for producing functional synthetic oil using refined fatty acid and functional synthetic oil produced thereby
JP2018120514A Pending JP2019052134A (en) 2017-09-12 2018-06-26 Manufacturing method of functional synthetic oil using purified aliphatic acid, and functional synthetic oil manufactured thereby

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KR (1) KR101853036B1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110143872A (en) * 2019-06-18 2019-08-20 山东海川化工技术研究院有限公司 The preparation method of neopentyl polyol ester
KR20230028991A (en) 2021-08-23 2023-03-03 박경환 Composition for plasticizer and manufacturing method thereof

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS565436A (en) * 1979-06-28 1981-01-20 Nippon Oil & Fats Co Ltd Preparation of carboxylic acid ester
JPS57125296A (en) * 1981-01-27 1982-08-04 Toei Chemical Kk Viscosity melting point adjustment for mixed fatty acid liquid comprising mainly c16 fatty acids
FR2509322A1 (en) * 1981-07-10 1983-01-14 Cirta Ct Int Rech Tech Appliqu OIL, ITS PREPARATION AND USE
ATE25264T1 (en) * 1981-07-20 1987-02-15 Henkel Kgaa PROCESS FOR THE PRODUCTION OF FATTY ACID ALKYLES WITH IMPROVED PROCESSABILITY.
JPH06721B2 (en) * 1985-12-27 1994-01-05 日本油脂株式会社 Method for producing oleic acid ester
DE4333323A1 (en) * 1993-09-30 1995-04-06 Hoechst Ag Mixtures of isomeric pentanoic acids, esters made from them and their use as lubricants
US6498261B1 (en) * 1995-06-07 2002-12-24 Cognis Corporation Process for improving color and color stability of oleic acid
JP3951832B2 (en) * 2002-06-27 2007-08-01 新日本理化株式会社 Method for producing fatty acid ester
DE602004005010T2 (en) * 2004-03-31 2007-08-09 Cognis Ip Management Gmbh Process for the production of fatty acids with the improved properties odor, color and heat stability
JP5375227B2 (en) * 2009-03-16 2013-12-25 日油株式会社 Method for producing ester lubricating oil for refrigerator
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