JP2010168537A5 - - Google Patents
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- JP2010168537A5 JP2010168537A5 JP2009201044A JP2009201044A JP2010168537A5 JP 2010168537 A5 JP2010168537 A5 JP 2010168537A5 JP 2009201044 A JP2009201044 A JP 2009201044A JP 2009201044 A JP2009201044 A JP 2009201044A JP 2010168537 A5 JP2010168537 A5 JP 2010168537A5
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- JP
- Japan
- Prior art keywords
- distillation
- less
- composition according
- ratio
- oil fuel
- 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.)
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Description
表7及び表8に示すように、実施例1〜12は、何れも従来のFT軽油である参考例と比較し、体積変化率が増加している。従って、表4〜6とこれらの結果から、炭素数15以下のパラフィン含有量の割合を28容量%以上、且つ、炭素数18以上のノルマルパラフィンの割合を11容量%以下とすることで、実質的にパラフィンのみで構成される軽油燃料組成物であっても、ゴム膨潤性を改良できることが確認できた。なお、実施例2、実施例3及び実施例12のピーク総面積の割合は、参考例よりも低くなっているが、炭素数15以下のパラフィン含有量、炭素数18以上のノルマルパラフィン含有量が本発明の条件を満たすため、体積変化率は比較例或いは参考例よりも増加している。すなわち、体積変化率の増加の観点からイソパラフィンの割合の高いことが好ましい点は上記のとおりであるが、たとえパラフィンのプロトン核磁気共鳴スペクトルにおけるピーク総面積の割合が比較例や参考例よりも低くても、炭素数15以下のパラフィン含有量の割合と炭素数18以上のノルマルパラフィンの割合が本発明の条件を満たしていれば、体積変化率の増加を図ることが確認できた。 As shown in Table 7 and Table 8, in Examples 1 to 12, the volume change rate is increased as compared with the reference example which is a conventional FT light oil. Therefore, from Tables 4 to 6 and these results, the ratio of the paraffin content having 15 or less carbon atoms is 28% by volume or more, and the ratio of the normal paraffin having 18 or more carbon atoms is 11% by volume or less. In particular, it was confirmed that even a light oil fuel composition composed only of paraffin can improve rubber swellability. The ratio of the total peak area of Example 2, Example 3 and Example 12 is lower than the ginseng Reference Example, the number 15 following paraffin content of carbon, normal paraffin content having 18 or more carbon atoms However, since the conditions of the present invention are satisfied, the volume change rate is higher than that of the comparative example or the reference example. That is, from the viewpoint of increasing the volume change rate, it is preferable that the ratio of isoparaffin is high as described above. However, if the ratio of the paraffin content having 15 or less carbon atoms and the ratio of the normal paraffin having 18 or more carbon atoms satisfy the conditions of the present invention, it was confirmed that the volume change rate was increased.
更に、表7及び表8に示すように、蒸留性状およびプロトン核磁気共鳴スペクトルにおけるピーク総面積の割合の関係が、上記式(1)で得られるZ値が−3.5より大きいことを満たすものであれば、従来のFT軽油よりも体積変化率の改善が図られることが確認できた。 Furthermore, as shown in Table 7 and Table 8 , the relationship between the distillation property and the ratio of the total peak area in the proton nuclear magnetic resonance spectrum satisfies that the Z value obtained by the above formula (1) is larger than −3.5. It can be confirmed that the volume change rate can be improved as compared with the conventional FT light oil.
Claims (5)
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009201044A JP2010168537A (en) | 2008-12-26 | 2009-08-31 | Light oil fuel composition |
US13/141,843 US20120138508A1 (en) | 2008-12-26 | 2009-12-24 | Diesel fuel composition |
EP09796013A EP2370550A2 (en) | 2008-12-26 | 2009-12-24 | Diesel fuel composition |
PCT/EP2009/067918 WO2010072839A2 (en) | 2008-12-26 | 2009-12-24 | Diesel fuel composition |
MYPI2011002973A MY180301A (en) | 2008-12-26 | 2009-12-24 | Diesel fuel composition |
CA2747787A CA2747787A1 (en) | 2008-12-26 | 2009-12-24 | Diesel fuel composition |
SG2011044641A SG172241A1 (en) | 2008-12-26 | 2009-12-24 | Diesel fuel composition |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008332634 | 2008-12-26 | ||
JP2009201044A JP2010168537A (en) | 2008-12-26 | 2009-08-31 | Light oil fuel composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2010168537A JP2010168537A (en) | 2010-08-05 |
JP2010168537A5 true JP2010168537A5 (en) | 2012-10-04 |
Family
ID=42167620
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2009201044A Pending JP2010168537A (en) | 2008-12-26 | 2009-08-31 | Light oil fuel composition |
Country Status (7)
Country | Link |
---|---|
US (1) | US20120138508A1 (en) |
EP (1) | EP2370550A2 (en) |
JP (1) | JP2010168537A (en) |
CA (1) | CA2747787A1 (en) |
MY (1) | MY180301A (en) |
SG (1) | SG172241A1 (en) |
WO (1) | WO2010072839A2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2973808B1 (en) * | 2011-04-06 | 2015-01-16 | Total Raffinage Marketing | SPECIAL FLUID COMPOSITION AND USE |
US20160230100A1 (en) * | 2013-09-30 | 2016-08-11 | Shell Oil Company | Fischer-tropsch derived gas oil fraction |
US9863898B2 (en) * | 2013-12-18 | 2018-01-09 | Exxonmobile Research And Engineering Company | High temperature simulated distillation |
RU2631116C2 (en) * | 2015-12-28 | 2017-09-19 | Шарин Евгений Алексеевич | All-season universal diesel fuel |
FR3081879B1 (en) | 2018-05-29 | 2020-11-13 | Total Marketing Services | COMPOSITION OF FUEL AND METHOD OF OPERATION OF AN INTERNAL COMBUSTION ENGINE |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3824489B2 (en) * | 1998-10-05 | 2006-09-20 | セイソル テクノロジー (プロプライエタリー) リミテッド | Biodegradability of middle distillates |
AU765274B2 (en) * | 1998-10-05 | 2003-09-11 | Sasol Technology (Pty) Ltd. | Process for producing middle distillates and middle distillates produced by that process |
DE60239102D1 (en) * | 2001-07-02 | 2011-03-17 | Sasol Tech Pty Ltd | BIODIESEL FISHER TROPHY CARBON MIXTURE |
US6890423B2 (en) * | 2001-10-19 | 2005-05-10 | Chevron U.S.A. Inc. | Distillate fuel blends from Fischer Tropsch products with improved seal swell properties |
US6846402B2 (en) * | 2001-10-19 | 2005-01-25 | Chevron U.S.A. Inc. | Thermally stable jet prepared from highly paraffinic distillate fuel component and conventional distillate fuel component |
US20070187292A1 (en) * | 2001-10-19 | 2007-08-16 | Miller Stephen J | Stable, moderately unsaturated distillate fuel blend stocks prepared by low pressure hydroprocessing of Fischer-Tropsch products |
AU2003270924B2 (en) * | 2002-06-07 | 2008-11-13 | Sasol Technology (Pty) Ltd | Synthetic fuel with reduced particulate matter emissions and a method of operating a compression ignition engine using said fuel in conjunction with oxidation catalysts |
US20040144690A1 (en) * | 2002-12-20 | 2004-07-29 | Lloyd David Hugh | Diesel fuel compositions |
CN1856562B (en) * | 2003-09-03 | 2010-06-23 | 国际壳牌研究有限公司 | Fuel compositions, preparation method and use thereof |
EP1664249B1 (en) * | 2003-09-17 | 2012-11-28 | Shell Internationale Research Maatschappij B.V. | Petroleum- and fischer-tropsch- derived kerosene blend |
JP4615913B2 (en) | 2004-07-02 | 2011-01-19 | 出光興産株式会社 | Fuel oil composition |
JP5121137B2 (en) * | 2005-11-30 | 2013-01-16 | Jx日鉱日石エネルギー株式会社 | Light oil composition |
JP5038647B2 (en) * | 2006-03-31 | 2012-10-03 | Jx日鉱日石エネルギー株式会社 | Light oil composition |
JP4815251B2 (en) * | 2006-03-31 | 2011-11-16 | Jx日鉱日石エネルギー株式会社 | Light oil composition |
CN101790578B (en) * | 2007-05-31 | 2013-05-08 | Sasol技术股份有限公司 | Cold flow response of diesel fuels by fraction replacement |
JP2010150479A (en) * | 2008-12-26 | 2010-07-08 | Showa Shell Sekiyu Kk | Gas oil fuel composition |
-
2009
- 2009-08-31 JP JP2009201044A patent/JP2010168537A/en active Pending
- 2009-12-24 CA CA2747787A patent/CA2747787A1/en not_active Abandoned
- 2009-12-24 MY MYPI2011002973A patent/MY180301A/en unknown
- 2009-12-24 US US13/141,843 patent/US20120138508A1/en not_active Abandoned
- 2009-12-24 WO PCT/EP2009/067918 patent/WO2010072839A2/en active Application Filing
- 2009-12-24 SG SG2011044641A patent/SG172241A1/en unknown
- 2009-12-24 EP EP09796013A patent/EP2370550A2/en not_active Withdrawn
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