JPWO2008123246A1 - 潤滑油基油及びその製造方法並びに潤滑油組成物 - Google Patents
潤滑油基油及びその製造方法並びに潤滑油組成物 Download PDFInfo
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Abstract
Description
ノルマルパラフィンを含有する原料油について、水素化処理触媒を用いて水素化処理する第1工程と、
第1工程により得られる被処理物について、水素化脱ロウ触媒を用いて水素化脱ロウする第2工程と、
第2工程により得られる被処理物について、水素化精製触媒を用いて水素化精製する第3工程と
を備える。
(ガスクロマトグラフィー条件)
カラム:液相無極性カラム(長さ25mm、内径0.3mmφ、液相膜厚さ0.1μm)昇温条件:50℃〜400℃(昇温速度:10℃/min)
キャリアガス:ヘリウム(線速度:40cm/min)
スプリット比:90/1
試料注入量:0.5μL(二硫化炭素で20倍に希釈した試料の注入量)
(I)100℃における動粘度が1.5mm2/s以上3.5mm2/s未満、より好ましくは2.0〜3.0mm2/sの潤滑油基油
(II)100℃における動粘度が3.0mm2/s以上4.5mm2/s未満、より好ましくは3.5〜4.1mm2/sの潤滑油基油
(III)100℃における動粘度が4.5〜20mm2/s、より好ましくは4.8〜11mm2/s、特に好ましくは5.5〜8.0mm2/sの潤滑油基油。
(IV)40℃における動粘度が6.0mm2/s以上12mm2/s未満、より好ましくは8.0〜12mm2/sの潤滑油基油
(V)40℃における動粘度が12mm2/s以上28mm2/s未満、より好ましくは13〜19mm2/sの潤滑油基油
(VI)40℃における動粘度が28〜50mm2/s、より好ましくは29〜45mm2/s、特に好ましくは30〜40mm2/sの潤滑油基油。
ρ=0.0025×kv100+0.816 (1)
[式中、kv100は潤滑油基油の100℃における動粘度(mm2/s)を示す。]
A=4.3×kv100+100 (2)
[式中、kv100は潤滑油基油の100℃における動粘度(mm2/s)を示す。]
実施例1−1〜1−3においては、まず、溶剤精製基油を精製する工程において減圧蒸留で分離した留分を、フルフラールで溶剤抽出した後で水素化処理し、次いで、メチルエチルケトン−トルエン混合溶剤で溶剤脱ろうした。溶剤脱ろうの際に除去され、スラックワックスとして得られたワックス分(以下、「WAX1」という。)を、潤滑油基油の原料油として用いた。WAX1の性状を表1に示す。
実施例2−1〜2−3においては、WAX1をさらに脱油して得られたワックス分(以下、「WAX2」という。)を、潤滑油基油の原料として用いた。WAX2の性状を表5に示す。
実施例3−1〜3−3においては、パラフィン含量が95質量%であり、20から80までの炭素数分布を有するFTワックス(以下、「WAX3」という。)を用いた。WAX3の性状を表9に示す。
実施例4−1〜4−3においては、水素圧の高い燃料油水素化分解装置を使用し、燃料油水素化分解装置から得られるボトム留分を用いた。
Claims (3)
- 尿素アダクト値が4質量%以下であり且つ粘度指数が100以上であることを特徴とする潤滑油基油。
- ノルマルパラフィンを含有する原料油について、得られる被処理物の尿素アダクト値が4質量%以下であり且つ粘度指数が100以上となるように、水素化分解/水素化異性化を行う工程を備えることを特徴とする潤滑油基油の製造方法。
- 請求項1に記載の潤滑油基油を含有することを特徴とする潤滑油組成物。
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JP2007092592 | 2007-03-30 | ||
JP2007092592 | 2007-03-30 | ||
PCT/JP2008/055574 WO2008123246A1 (ja) | 2007-03-30 | 2008-03-25 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
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JP2009509113A Active JP6190091B2 (ja) | 2007-03-30 | 2008-03-25 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
JP2015077499A Active JP6190412B2 (ja) | 2007-03-30 | 2015-04-06 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
JP2017077774A Active JP6262901B2 (ja) | 2007-03-30 | 2017-04-10 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
JP2017239859A Active JP6513780B2 (ja) | 2007-03-30 | 2017-12-14 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
JP2019075020A Pending JP2019108561A (ja) | 2007-03-30 | 2019-04-10 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
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JP2017077774A Active JP6262901B2 (ja) | 2007-03-30 | 2017-04-10 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
JP2017239859A Active JP6513780B2 (ja) | 2007-03-30 | 2017-12-14 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
JP2019075020A Pending JP2019108561A (ja) | 2007-03-30 | 2019-04-10 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
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US (1) | US8754016B2 (ja) |
EP (1) | EP2135928B1 (ja) |
JP (5) | JP6190091B2 (ja) |
KR (1) | KR101396804B1 (ja) |
CN (2) | CN101652460A (ja) |
CA (1) | CA2682660C (ja) |
SG (1) | SG179416A1 (ja) |
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WO2008123249A1 (ja) * | 2007-03-30 | 2008-10-16 | Nippon Oil Corporation | 緩衝器用作動油 |
CN101652460A (zh) | 2007-03-30 | 2010-02-17 | 新日本石油株式会社 | 润滑油基油及其制造方法以及润滑油组合物 |
US20080269091A1 (en) * | 2007-04-30 | 2008-10-30 | Devlin Mark T | Lubricating composition |
CN103923726A (zh) * | 2007-12-05 | 2014-07-16 | 吉坤日矿日石能源株式会社 | 润滑油组合物 |
JP5483662B2 (ja) | 2008-01-15 | 2014-05-07 | Jx日鉱日石エネルギー株式会社 | 潤滑油組成物 |
JP5800448B2 (ja) * | 2008-03-25 | 2015-10-28 | Jx日鉱日石エネルギー株式会社 | 潤滑油基油及びその製造方法並びに潤滑油組成物 |
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CN102239241B (zh) | 2008-10-07 | 2013-09-18 | 吉坤日矿日石能源株式会社 | 润滑油基油及其制造方法以及润滑油组合物 |
JP2010090251A (ja) * | 2008-10-07 | 2010-04-22 | Nippon Oil Corp | 潤滑油基油及びその製造方法、潤滑油組成物 |
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CN105296119A (zh) | 2016-02-03 |
US20100130395A1 (en) | 2010-05-27 |
EP2135928A1 (en) | 2009-12-23 |
US8754016B2 (en) | 2014-06-17 |
JP6190412B2 (ja) | 2017-08-30 |
CA2682660C (en) | 2015-06-02 |
JP6262901B2 (ja) | 2018-01-17 |
CA2682660A1 (en) | 2008-10-16 |
JP2015127426A (ja) | 2015-07-09 |
KR20090129502A (ko) | 2009-12-16 |
JP2018040016A (ja) | 2018-03-15 |
CN105296119B (zh) | 2019-03-12 |
KR101396804B1 (ko) | 2014-05-20 |
EP2135928A4 (en) | 2011-06-29 |
JP6190091B2 (ja) | 2017-08-30 |
JP6513780B2 (ja) | 2019-05-15 |
JP2019108561A (ja) | 2019-07-04 |
EP2135928B1 (en) | 2013-08-21 |
SG179416A1 (en) | 2012-04-27 |
JP2017137503A (ja) | 2017-08-10 |
CN101652460A (zh) | 2010-02-17 |
WO2008123246A1 (ja) | 2008-10-16 |
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