[0001] This invention relates to unleaded gasolines for use in direct injection gasoline
engines and more particularly to such a gasoline which is capable of reducing the
amount of environmental pollutants emission and further excellent in durability of
the engine in which the gasoline is employed.
[0002] From the viewpoint of resource-savings and suppression of global warming, it has
been a world-wide demand that the usage of fossil fuel should be decreased and in
connection with this an improvement in fuel consumption becomes the most important
issue for gasoline-engine automobiles. On the other hand, there are some urban areas
which fail to achieve the environmental standards in terms of the amount of pollutants
such as NOx (nitrogen oxide), and gasoline-engine automobiles are thus required to
be less in the amount of such pollutants emission. A direct injection gasoline engine
is considered to be the most effective means for meeting or satisfying such a demand
or standard.
[0003] A conventional engine forms a homogeneous pre-mixture of gasoline and air by injecting
gasoline into the intake port, while a direct injection gasoline engine injects gasoline
directly into the combustion chamber like a diesel engine so that it becomes possible
to form a stratified fuel mixture which is rich in the neighborhood of the spark plug
but ultra highly lean in the entire combustion chamber. Due to the formation of such
a stratified fuel mixture, combustion with the highly lean mixture can be achieved,
leading to an improvement in fuel consumption equivalent to that of a diesel engine.
Moreover, the direct injection of gasoline into the combustion chamber is contributive
to the freedom of delay in gasoline vaporization as seen in the conventional engine
and enables further enhanced accuracy in control of fuel injection rate.
[0004] However, the direct injection gasoline engine would be encountered with some unexpected
problems which are different from those of the conventional engines due to the direct
injection of gasoline into the combustion chamber. One of such problems is related
to the smoke exhausted mainly from the part of the mixture in which the gasoline is
excessively rich, upon the stratified combustion. This smoke contained in exhaust
gases not only adversely affects the environment but also causes smoldering of the
spark plug, leading to deterioration of durability of the engine.
[0005] In view of the foregoing problems, the present invention is intended to provide an
unleaded gasoline suitable for a direct injection gasoline engine which gasoline is
capable of reducing the amount of environmental pollutants emission and further improving
durability of the engine.
[0006] It has now been found after extensive research that the amount of exhaust smoke can
be reduced by use of an unleaded gasoline containing an oxygen-containing compound
in a predetermined amount for a direct injection gasoline engine, resulting in suppression
of smoldering of the spark plug and the formation of deposits in the combustion chamber
thereby improving durability of the engine.
[0007] According to the present invention, there is provided an unleaded gasoline for a
direct injection gasoline engine which contains an oxygen-containing compound having
2-15 carbon atoms in an amount in terms of oxygen atom of 0.1-15 mass % based on the
total gasoline.
[0008] The unleaded gasoline for a direct injection gasoline engine according to the invention
contains an oxygen-containing compound having 2-15, preferably 2-12, more preferably
2-10 carbon atoms.
[0009] There is no particular limitation imposed on the structure of the oxygen-containing
compound as long as it has 2-15 carbon atoms in the molecule. Generally, such an oxygen-containing
compound has in its molecule at least one oxygen-containing group selected from the
group consisting of a hydroxyl group, an ether bond and a carbonyl group.
[0010] An oxygen-containing compound eligible for the present invention is represented by
the formula

wherein R
1 and R
3 each are hydrogen or a C
1 - C
15 hydrocarbon group, R
2 is a C
2 - C
4 alkylene group and n is an integer of 0 - 7, provided that the total carbon number
in the molecule is from 2 to 15 and if n is 0, it is excluded that both R
1 and R
3 are hydrogen at the same time.
[0011] Each of R
1 and R
3, independently the other, is hydrogen or a C
1 - C
15 hydrocarbon but is preferably hydrogen or a C
1 - C
13 straight or branched alkyl group, a C
2 - C
13 straight or branched alkenyl group, a C
5 - C
13 cycloalkyl or alkylcycloalkyl group, a C
6 - C
13 aryl or alkylaryl group or a C
7 - C
13 arylalkyl group. Preferred alkyl groups for R
1 and R
3 include methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl,
straight or branched pentyl, straight or branched hexyl, straight or branched heptyl,
straight or branched octyl, straight or branched nonyl, straight or branched decyl,
straight or branched undecyl, straight or branched dodecyl and straight or branched
tridecyl.
[0012] Preferred examples of an alkenyl group for R
1 and R
3 include vinyl, propenyl, isopropenyl, straight or branched butenyl, butadienyl, straight
or branched pentenyl, straight or branched hexenyl, straight or branched heptenyl,
straight or branced octenyl, straight or branced nonenyl, straight or branched decenyl,
straight or branched undecenyl, straight or branched dodecenyl and straight or branched
tridecenyl groups.
[0013] Preferred examples of a cycloalkyl group for R
1 and R
3 include cyclopentyl, cyclohexyl and cycloheptyl groups while preferred examples of
an alkylcycloalkyl groups include methylcyclopentyl, dimethylcyclopentyl (inclusive
of all positional isomers), ethylcyclopentyl (inclusive of all positional isomers),
straight or branched propylcyclopentyl (inclusive of all positional isomers), ethylmethylcyclopentyl
(inclusive of all positional isomers), trimethylcyclopentyl(indusive of all positional
isomers), diethylcyclopentyl (inclusive of all positional isomers), ethyldimethylcydopentyl
(inclusive of all positional isomers), straight or branched propylmethylcyclopentyl
(inclusive of positional isomers), straight or branched propylethylcyclopentyl (inclusive
of all positional isomers), di(straight or branched) propylcyclopentyl (inclusive
of all positional isomers), straight or branched propylethylmethylcyclopentyl (inclusive
of all positional isomers), methylcyclohexyl (inclusive of all positional isomers),
dimethylcyclohexyl (inclusive of all positional isomers), ehtylcyclohexyl (inclusive
of all positional isomers), straight or branched propylcyclohexyl (inclusive of all
positional isomers), ethylmethylcyclohexyl (inclusive of all positional isomers),
trimethylcyclohexyl (inclusive of all positional isomers), diethylcyclohexyl (inclusive
of all positional isomers), ethyldimethylcyclohexyl (inclusive of all positional isomers),
straight or branched propylmethylcyclohexyl (inclusive of all positional isomers),
straight or branched propyl ethyl cyclohexyl (inclusive of all positional isomers),
di-straight or branched propylcyclohexyl (inclusive of all positional isomers), straight
or branched propylethylmethylcyclohexyl (inclusive of all positional isomers), methylcycloheptyl
(inclusive of all positional isomers), dimethylcycloheptyl (inclusive of all positional
isomers), ethylcycloheptyl (inclusive of all positional isomers), straight or branched
propylcycloheptyl (inclusive of all positional isomers), ethylmethylcycloheptyl (inclusive
of all positional isomers), trimethylcycloheptyl (inclusive of all positional isomers),
diethylcycloheptyl (inclusive of all positional isomers), ethyldimethylcycloheptyl
(inclusive of all positional isomers), straight or branched propylmethylcycloheptyl
(inclusive of all positional isomers), straight or branched propylethylcycloheptyl
(inclusive of all positional isomers), di-straight or branched proypylcycloheptyl
(inclusive of all positional isomers) and straight or branched propylethylmethylcycloheptyl
groups (inclusive of all positional isomers).
[0014] Preferred examples of an aryl group for R
1 and R
3 include phenyl and naphtyl groups, while preferred examples of an alkylaryl group
include tolyl (inclusive of all positional isomers), xylyl (inclusive of all positional
isomers), ethylphenyl (inclusive of all positional isomers), straight or branched
propylphenyl (inclusive of all positional isomers), ethyl methyl phenyl (inclusive
of all positional isomers), trimethylphenyl (inclusive of all positional isomers),
straight or branched butylphenyl (inclusive of all positional isomers), straight or
branched propyl methyl phenyl (inclusive of all positional isomers), diethylphenyl
(inclusive of all positional isomers), ethyldimethylphenyl (inclusive of all positional
isomers), tetramethylphenyl (inclusive of all positional isomers), straihgt or branched
pentylphenyl (inclusive of all positional isomers), straight or branched hexylphenyl
(inclusive of all positional isomers) and straight or branched heptylphenyl (inclusive
of all positional isomers).
[0015] Among of these, R
1 and R
3 each independently are preferably hydrogen or a C
1 - C
12 straight or branched alkyl group, more preferably hydrogen or a C
1 - C
6 straight or branched alkyl group and most preferably hydrogen or C
1 - C
4 straight or branched alkyl group.
[0016] R
2 in formula (I) is a C
2 - C
4 alkylen group such as ethylene, propylene (1-methylethylene, 2-methylethylene), trimethylene,
butylene(1-ethylethylene, 2-ethylethylene), 1,2-dimethylethylene, 2,2-dimethylethylene,
1-methyltrimethylene, 2-methyltrimethylene, 3-methylthrimethylene and tetramethylene
among which ethylene, propylene and butylene are preferred.
Formula (I) wherein either R
1 or R
2 is hydrogen, the other is a hydrocarbon and n is 0 represents a monohydric alcohol.
Such an alcohol is exemplified by a monohydric aliphatic alcohol which may be straight
or branched. Specific examples of the monohydric aliphatic alcohol include ethanol,
straight or branched propanol, straight or branched butanol, straight or branched
pentanol, straight or branched hexanol, straight or branched heptanol, straight or
branched octanol, straight or branched nonanol, straight or branched decanol, straight
or branched undecanol, straight or branched dodecanol, straight or branched tridecanol,
straight or branched tetradecanol, straight or branched pentadecanol and mixtures
thereof. Preferred among the above monohydric aliphatic alcohol are those having 2
- 12 carbon atoms, more preferred are those having 2 - 10 carbon atoms and most preferred
are those having 2 - 6 carbon atoms because they are particularly excellent in an
reduction in exhausted smoke. Methanol is not preferred because it would increase
aldehyde concentration in the exhaust gas and is corrosive.
Formula (I) wherein R
1 and R
2 each are a hydrocarbon group and n is 0 represents an ether. Such an ether compound
exemplarily includes dimethylether, methyl ethyl ether, diethylether, methyl propylether
(inclusive of all isomers of propyl group), ethyl n-propylether (inclusive of all
isomers of propyl group), dipropylether, methylbutylether (inclusive of all isomers
of butyl group), ethylbutylether (inclusive of all isomers of propyl group), propylbutylether
(inclusive of all isomers of propyl group and butyl group), dibutylether (inclusive
of all isomers of butyl group), methylpentylether (inclusive of all isomers of pentyl
group), ethylpentylether (inclusive of all isomers of pentyl group), propylpentylether
(inclusive of all isomers of propyl group and pentyl group), butylpentylether (inclusive
of all isomers butyl group and pentyl group) and dipentylether (inclusive of all isomers
of pentyl group). Preferred among the above ethereal compounds are those having 2
-12 carbon atoms, more preferred are those having 3 - 10 carbon atoms and most preferred
are those having 4 - 8 carbon atoms because of an excellent effect in a reduction
of exhaust smoke.
[0017] Represented by formula (I) wherein R
1 and R
3 each are hydrogen and n is an integer of more than 1 is a dihydric alcohol. Specific
examples of such a dihydric alcohol include ethylene glycol, propylene glycol, 1,3-propane
diol, 1,2-butane diol (butylene glycol), 1,3-butane diol, 1,4-butane diol, 2-methyl-1,2-propane
diol, 2-methyl-1,3-propane diol, 1,2-pentane diol, 1,3-pentane diol, 1,4-pentane diol,
1,5-pentane diol, neopentyl glycol and polymers thereof.
[0018] Represented by formula (I) wherein at least one of R
1 and R
3 is a hydrocarbon group and n is an integer of more than 1 is a compound obtained
by etherifying at least one of the two terminal hydroxyl groups of the above-mentioned
dihydric alcohol. Such a terminal-etherified compound exemplarily include ethylene
glycol monoalkylether, ethylene glycol dialkylether, propylene glycol monoalkylether,
propylene glycol dialkylether, butylene glycol monoalkylether, butylene glycol dialkylether,
diethylene glycol monoalkylether, diethylene glycol dialkylether, dipropylene glycol
monoalkylether, dipropylene glycol dialkylether, dibutylene glycol monoalkylether
and dibutylene glycol dialkylether.
[0019] Although not encompassed by compounds represented by formula (I), polyhydric alcohols
having three or more hydroxyl groups can be used as the oxygen-containing compound
defined by the present invention. Such alcohols are those having 3 - 10, preferably
3 - 6 hydroxyl groups. Specific examples of the alcohol having 3 - 10 hydroxyl groups
are polyhydric alcohols such as glycerol, polyglycerol (dimers through pentamers of
glycerol such as diglycerol, triglycerol and tetraglycerol), trimethylolalkane (trimethylolethane,
trimethylolpropane and trimethylolbutane) and the dimers and trimers thereof, pentaerythrirol
and the dimers and trimers thereof, 1,2,4-butanetriol, 1,3,5-pentanetriol, 1,2,6-hexanetriol,
1,2,3,4-butanetetrol, sorbitol, sorbitan, sorbitol glycerin condensation products,
adonitol, arabitol, xylitol and mannitol; and saccharides such as xylose, arabinose,
ribose, rhamnose, glucose, fructose, galactose, mannose, sorbose, cellobiose, maltose,
isomaltose, trehalose and sucrose; and mixtures thereof.
[0020] The oxygen-containing compound having in its molecule a carbonyl group may be exemplified
by ketones and esters. Such ketones can be represented by the formula

wherein R
4 and R
5 are each independently a C
1 - C
13 hydrocarbon group, provided that the total carbon number of R
4 and R
5 is from 2 to 14.
[0021] Preferred hydrocarbon groups for each R
4 and R
5 are a C
1 - C
13 straight or branched alkyl group, a C
2 - C
13 straight or branched alkenyl group, a C
5 - C
13 cycloalkyl or alkylcycloalkyl group, a C
6 - C
13 aryl or alkylaryl group or a C
7 - C
13 arylalkyl group all of which have been exemplified with respect to R
1 and R
3, R
4 and R
5 each are more preferably a C
1 - C
12 straight or branched alkyl group. Further more preferably, R
4 and R
5 each are a C
1 - C
6 straight or branched alkyl group and most preferably are a C
1 - C
4 alkyl group.
[0022] Specific examples of the ketones represented by formula (II) include dimethylketone
(acetone), methylethylketone, diethyl ketone, methyl propyl ketone (inclusive of all
isomers of propyl group), ethylpropylketone (inclusive of all isomers of propyl group),
dipropyl ketone (inclusive of all isomers of propyl group), methylbutylketone (inclusive
of all isomers of butyl group), ethylbutylketone (inclusive of all isomers of butyl
group), propylbutylketone (inclusive of all isomers of propyl and butyl groups), dibutylketone
(inclusive of all isomers of butyl group), methylpentylketone (inclusive of all isomers
of pentyl group), ethylpentylketone (inclusive of all isomers of pentyl group), propylpentylketone
(inclusive of all isomers of propyl and pentyl groups), butylpentylketone (inclusive
of all isomers of butyl and pentyl groups) and dipentylketone (inclusive of all isomers
of pentyl group).
[0023] Although not encompassed by formula (II), a cyclic ketone such as cyclohexane and
the like is also eligible for the inventive oxygen-containing compound.
[0024] There may be used an alcohol which may be monohydric or polyhydric and an acid which
may be monobasic or polybasic for the ester used as the oxygen-containing compound.
[0025] Preferred monohydric alcohols may be those having 1 -10 carbon atoms, more preferred
are those having 1 - 6 carbon atoms and most preferred are those having 1 - 4 carbon
atoms. Specific examples of the monohydric alcohol having 1 -10 carbon atoms are methanol,
ethanol, straight or branched propanol, straight or branched butanol, straight or
branched pentanol, straight or branched hexanol, straight or branched heptanol, straight
or branched octanol, straight or branched nonanol, straight or branched decanol, straight
or branched undecanol, straight or branched undecanol, straight or branched dodecanol,
straight or branched tridecanol, straight or branched tetradecanol, straight or branched
pentadecanol and mixtures thereof.
[0026] Alternatively, an alokoxyalcohol having 2 - 14, preferably 2 - 10, more preferably
2 - 6 carbon atoms is also eligible. Specific examples of such an alkoxy alcohol are
methoxymethyl alcohol, methoxyethyl alcohol, ethoxyethyl alcohol, methoxypropyl alcohol
(inclusive of all isomers of propyl group), ethoxypropyl alcohol (inclusive of all
isomers of propyl group), propoxypropyl alcohol (inclusive of all isomers of propyl
group), methoxybutyl alcohol (inclusive of all isomers of butyl group), ethoxybutyl
alcohol (inclusive of all isomers of butyl group) and methoxypentyl alcohol (inclusive
of all isomers of pentyl group).
[0027] Eligible polyhydric alcohols are the dihydric alcohols and polyhydric alcohols having
3 or more hydroxyl groups which are exemplified as being preferred for the compound
represented by formula (I).
[0028] Eligible monobasic acids are fatty acids having 2 -14 carbon atoms. Such fatty acids
may be straight or branched and saturated or unsaturated. Specific examples of the
fatty acids are saturated fatty acids such as ethanoic acid (acetic acid), straight
or branched propanoic acid, straight or branched butanoic acid, straight or branched
heptanoic acid, straight or branched hexanoic acid, straight or branched heptanoic
acid, straight or branched octanoic acid, straight or branched nonanoic acid, straight
or branched decanoic acid, straight or branched undecanoic acid, straight or branched
dodecanoic acid, straight or branched tridecanoic acid, straight or branched tetradecanoic
acid; and unsaturated aliphatic acids such as straight or branched propenoic acid
(acryic acid), straight or branched butenoic acid (inclusive of methacrylic acid),
straight or branched heptenoic acid, straight or branched hexenoic acid, straight
or branched heptenoic acid, straight or branched octenoic acid, straight or branched
nonenoic acid, straight or branched decenoic acid, straight or branched undecenoic
acid, straight or branced dodecenoic acid, straight or branched tridecenoic acid and
straight or branched tetradecenoic acid; and mixtures thereof. Among these fatty acids,
preferred are saturated fatty acids having 2 - 10 carbon atoms, more preferred are
saturated fatty acids having 2 - 6 carbon atoms and most preferred are saturated aliphatic
acids having 2 - 4 carbone atoms.
[0029] Eligible polybasic acids are dibasic acids having 2 -13 carbon atoms and trimellitic
acid. These dibasic acids having 2 -13 carbon atoms may be straight or branched and
saturated or unsaturated. Specific examples of such dibasic acids are saturated dibasic
acids such as ethanedioic acid (oxalic acid), propanedioic acid (oxalic acid), straight
or branched butanedioic acid (inclusive of succinic acid), straight or branched pentanedioic
acid, straight or branched hexanedioic acid, straight or branched heptanedioic acid,
straight or branched octanedioic acid, straight or branched nonanedioic acid, straight
or branched decanedioic acid, straight or branched undecanedioic acid, straight or
branched dodecandioic acid and straight or branched tridecanedioic acid; and unsaturated
dibasic acid such as straight or branched butenedioic acid (inclusive of maleic acid
and fumaric acid), straight or branched pentendioic acid, straight or branched hexenedioic
acid, straight or branched heptenedioic acid, straight or branched octenedioic acid,
straight or branched nonendioic acid, straight or branched decenedioic acid, straight
or branched undecenedioic acid, straight or branched dodecenedioic acid and straight
or branched tridecendioic acid; and mixtures thereof. Preferred among these polybasic
acids are dibasic acids having 2 - 10 carbon atoms. More preferred are dibasic acids
having 2 - 6 carbon atoms and most preferred are dibasic acids having 2 - 4 carbon
atoms.
[0030] The esters used as the inventive oxygen-containing compound may constituted by any
combinations of an alcohol and an acid. Such combinations are exemplified as follows:
(1) an ester of a monohydric alcohol and a monobasic acid,
(2) an ester of a polyhydric alcohol and a monobasic acid,
(3) an ester of a monohydric alcohol and a polybasic acid,
(4) an ester of a polyhydric alcohol and a polybasic acid,
(5) a mixed ester of a mixture of a monohydric alcohol and a polyhydric alcohol and
a polybasic acid,
(6) a mixed ester of a polyhydric alcohol and a mixture of a monobasic acid and a
polybasic acid, and
(7) a mixed ester of a mixture of a monohydric alcohol and a polyhydric alcohol and
a mixture of a monobasic acid and polybasic acid.
[0031] If a polyhydric alcohol is used as an alcohol component, the ester obtained may be
a full ester derived from the complete esterification of all of the hydroxyl groups
contained in the polyhydric alcohol or a partial ester having one or more of hydroxyl
groups remaining unesterified. If a polybasic acid is used as an acid component, the
ester may be a full ester derived from the complete esterification of all of the carboxyl
groups in the polybasic acid or a partial ester having one or more of carboxyl groups
remaining unesterified.
[0032] An alcohol and an acid forming the ester used as the inventive oxygen-containing
compound has individually been described. Preferred esters are methyl acetate, ethyl
acetate, propyl acetate (inclusive of all isomers of propyl group), butyl acetate
(inclusive of all isomers of butyl group), methoxypropyl acetate (inclusive of all
isomers of propyl group), dimethyl succinate, diethyl succinate, dimethyl maleate
and diethyl maleate.
[0033] Besides the above-described ester, there may be used a carbonic ester represented
by the formula

wherein R
6 and R
7 are each independently a C
1 - C
13 hydrocarbon group provided that the total carbon number of R
6 and R
7 is from 2 to 14.
[0034] Preferred hydrocarbon groups for each R
6 and R
7 are a C
1 - C
13 straight or branched alkyl group, a C
2 - C
13 straight or branched alkenyl group, a C
5 - C
13 cycloalkyl or alkylcycloalkyl group, a C
6 - C
13 aryl or alkylaryl group or a C
7 - C
13 arylalkyl group all of which has been exemplified with respect to R
1 and R
3, R
6 and R
7 each are preferably a straight or branched C
1 - C
12 alkyl group, more preferably a straight or branched C
1 - C
6 alkyl group and most preferably a straight or branched C
1 - C
4 alkyl group.
[0035] Specific examples of the carbonic ester represented by formula (III) are dimethyl
carbonate, methylethyl carbonate, diethyl carbonate, methylpropyl carbonate (inclusive
of all isomers of propyl group), ethylpropyl carbonate (inclusive of all isomers of
propyl group), dipropyl carbonate (inclusive of all isomers of propyl group), methylbutyl
carbonate (inclusive of all isomers of butyl group), ethylbutyl carbonate (inclusive
of all isomers of butyl group), propylbutyl carbonate (inclusive of all isomers of
propyl and butyl groups), dibutyl carbonate (inclusive of all isomers of butyl group),
methylpentyl carbonate (inclusive of all isomers of pentyl group), ethylpentyl carbonate
(inclusive of all isomers of pentyl group), propylpentyl carbonate (inclusive of all
isomers of propyl and pentyl groups), butylpentyl carbonate (inclusive of all isomers
of butyl and pentyl groups) and dipentyl carbonate (inclusive of all isomers of pentyl
group).
[0036] Furthermore, besides the above-exemplified esters, a cyclic ester such as γ-butyllactone
is also eligible for the oxygen-containing compound according to the invention.
[0037] In the present invention, the oxygen-containing compound may be used singular or
in combination.
[0038] The unleaded gasoline according to the invention contains, based on the total weight
thereof, the above-described oxygen-containing compound in an amount in terms of oxygen
atom of more than 0.1 mass %, preferably more than 0.7 mass %, more preferably more
than 1.5 mass % and most preferably more than 2 mass % and less than 15 mass %, preferably
less than 10 mass %, more preferably less than 8 mass %. The content of the oxygen-containing
compound if less than the lower limit of 0.1 mass % would not be sufficient in an
reduction of the amount of the exhaust smoke, while the content in excess of the upper
limit of 15 mass % would not be expected in further enhancement and would lead to
the possibility of an increase in fuel consumption and an increase in NOx emission.
[0039] The content of the oxygen-containing compound itself is not particularly restricted
as long as the content thereof by oxygen atomic conversion falls within the range
of 0.1 -15 mass %. However, the oxygen-containing compound content should be greater
than 0.3 mass %, preferably greater than 1 mass %, based on the total mass of the
gasoline because a further reduction in the amount of the exhaust smoke can be expected.
[0040] The inventive gasoline is substantially free of alkyl lead compounds such as tetraethyl
lead, but should such compounds be present, the amount thereof should be held below
the lower threshold specified by JIS K2255 related to the test method for lead in
gasolines.
[0041] Although the inventive gasoline is not restricted to octane number, it should have
an octane number of greater than 89, preferably greater than 90, more preferably greater
than 90.5 and most preferably greater than 91 by the research octane number (RON),
and an octane number of greater than 80, preferably greater than 80.5 and most preferably
greater than 81 by the motor octane number (MON) so as to maintain good anti-knock
performance.
[0042] Both RON and MON octane numbers are values measured by the test procedure of JIS
K 2280 "Testing Method for Octane Number and Cetane Number".
[0043] The distillation properties of the inventive gasoline pursuant to the test method
of JIS K 2254 "Testing Method for Distillation of Petroleum Products" should be as
follows:
Running point at 10 vol. % (T
10)... 35 - 55°C
Running point at 30 vol. % (T
30) ... 55 - 75°C
Running point at 50 vol. % (T
50) ... 75 - 100°C
Running point at 70 vol. % (T
70) ... 100 - 130°C
Running point at 90 vol. % (T
30) ... 120 -160°C
End point ... 130 - 210°C
[0044] Lower limit temperature (T
10) is 35°C, preferably 40°C. Below 35°C would cause gasoline coking in an injector.
Upper limit temperature (T
10) is 55°C, preferably 50°C, more preferably 48°C. Above 55°C would lead to aggravated
low temperature engine startability.
[0045] Lower limit temperature (T
30) is 55°C, preferably 60°C. Below 55°C would invite objectionable high temperature
engine performance and cause gasoline coking in an injector. Upper limit temperature
(T
30) is 75°C, preferably 70°C, more preferably 68°C. Above 75°C would lead to aggravated
low temperature engine performance.
[0046] Lower limit temperature (T
50) is 75°C, preferably 80°C. Below 75°C would adversely affect engine performance at
low and normal temperatures. Upper limit temperature (T
50) is 100°C, preferably 95°C, more preferably 93°C. Above 100°C would lead to aggravated
high temperature engine performance.
[0047] Lower limit temperature (T
70) is preferably 100°C. Upper limit temperature (T
70) is 130°C, preferably 125°C, more preferably 123°C, most preferably 120°C. Above
130°C would lead to aggravated normal temperature engine performance.
[0048] Upper limit temperature (T
90) is 160°C, preferably 150°C, more preferably 140°C. The upper limit of less than
160°C leads to a reduction in engine oil dilution and prevents an increase in exhaust
smoke, deterioration in the engine oil and the formation of sludges. Lower limit temperature
(T
90) is preferably greater than 120°C.
[0049] Lower limit end point is preferably 130°C, while upper limit is 210°C, preferably
200°C, more preferably 195°C and most preferably 190°C. End point in excess of 210°C
would lead to aggravated normal temperature engine performance.
[0050] Though not restricted, the Reid vapor pressure (RVP) of the inventive gasoline as
defined by JIS K 2258 "Testing Method for Vapor Pressure of Petroleum Products (Reid
Method)" should be less than 70 kPa, preferably less than 65 kPa, more preferably
less than 60 kPa and most preferably less than 55 kPa to preclude the possibility
of gasoline coking in the injector and suppress the amount of evaporative emission.
[0051] Though not restricted, the density at 15°C of the inventive gasoline should preferably
be in the range of 0.73 to 0.77 g/cm
3. The lower limit of densities is 0.73 g/cm
3, preferably 0.735 g/cm
3. Densities below 0.73 g/cm
3 would result in increased fuel consumption. The upper limit of density is 0.77 g/cm
3, preferably 0.76 g/cm
3. Densities above 0.77 g/cm
3 would lead to the possibility of insufficient acceleration and spark plug smoldering.
[0052] The term "density" used herein designate a density determined by JIS K 2541 resting
Method for Densities of Crude Oil and Petroleum Products and Density-Mass-Volume Conversion
Table".
[0053] Although the inventive gasoline is not restricted in terms of the contents of paraffins,
olefins and aromatics, such contents should preferably be in the following range:
| Paraffins (V(P)) |
50 - 100 % by volume |
| Olefins (V(O)) |
0 -15 % by volume |
| Aromatics (V(Ar)) |
0 - 35 % by volume |
[0054] The content of V(P) in the inventive gasoline should be in the range of 50 - 100
% by volume, preferably 60 - 100 % by volume, more preferably 70 - 100 % by volume
with a view to precluding gasoline coking in the injector, reducing spark plug smoldering
and ozone-formability of the exhaust gas as well as the benzene concentration thereof,
with a freedom from soot.
[0055] The content of V(O) in the inventive gasoline should be in the range of 0 -15 % by
volume, preferably 0 - 10 % by volume, more preferably 0 - 7 % by volume, most preferably
0 - 5 % by volume with a view to preventing gasoline coking in the injector.
[0056] The content of V(Ar) in the inventive gasoline should be in the range of 0 - 35 %
by volume, preferably 0 - 30 % by volume, more preferably 0 - 100 % by volume, most
preferably 0 - 20 % by volume with a view to precluding gasoline coking in the injector,
reducing spark plug smoldering and ozone-formability of the exhaust gas as well as
the concentrates of benzene thereof, with a freedom from soot.
[0057] The contents of the above paraffins, olefins and aromatics are measured by the procedure
of JIS K 2536 resting Method for Hydrocarbon Types in Petroleum Products by Fluorescent
Indicator Adsorption".
[0058] The inventive gasoline is not restricted in terms of the content of each component
other than the oxygen-containing compound which however should be in the following
range.
(1)V(Bz) : 0 - 1 % by volume
(2) V(Tol) : 0 - 30 % by volume
(3) V(C8A) : 0 - 20 % by volume
(4) V(C9A) : 0 - 5 % by volume
(5) V(C10+A) : 0 - 3 % by volume
(6) V(PA) = 0 or
when V(PA) ≠ 0, V(MA)/V(PA) : more than 1
(7) V(C4) : 0 - 10 % by volume
(8) V(C5) : 10 - 35 % by volume
(9) V(C6) : 10 - 30 % by volume
(10) V(C7+p) : 10 - 50 % by volume
(11) V(C7+) : 10 - 50 % by volume
[0059] V(Bz) is the amount of benzene, based on the total gasoline. The amount of the benzene
should be in the range of 0 - 1 % by volume, preferably 0 - 0.5 % by volume. The benzene
in an amount of 0 - 1 % by volume results in the reduced concentrate of benzene in
the exhaust gas.
[0060] V(Tol) and V(G
8A) are the amount of toluene and the amount of a C
8 aromatic hydrocarbon, based on the total gasoline, respectively. V(Tol) should be
in the range of 0 - 30 % by volume, preferably 0 - 20 % by volume, while V(C
8A) should be in the range of 0 - 20 % by volume, preferably 0 -15 % by volume. The
C
8 aromatic hydrocarbon includes ethylbenzene and xylene (inclusive of all positional
isomers).
[0061] V(C
9A) is the amount of a C
9 aromatic hydrocarbon, based on the total gasoline. V(C
9A) should be in the range of 0 - 5 % by volume, preferably 0 - 3 % by volume with
a view to reducing the formability of ozone in the exhaust gas. The C
9 aromatic hydrocarbon exemplarily include n-propylbenzene, isopropylbenzene (cumene),
ethylmethylbenzene (inclusive of all positional isomers) and trimethylbenzene (inclusive
of all positional isomers).
[0062] V(C
10+A) is the amount of the aromatic hydrocarbon having more than 10 carbon atoms, based
on the total gasoline. V(C
10+A) should be in the range of 0 - 3 % by volume, preferably 0 - 1 % by volume but more
preferably be hold to 0 % by volume. The aromatic hydrocarbon having more than 10
carbon atoms exemplarily includes diethylbenzene (inclusive of all positional isomers),
dimethylethylbenzene (inclusive of all positional isomers), tetramethylbenzene (inclusive
of all positional isomers) and n-butylmethylbenzene (inclusive of all positional isomers).
[0063] V(MA) and V(PA) are the amount of the aromatic hydrocarbon having one alkyl substituent
(% by volume) and the amount of the aromatic hydrocarbon having more than 2 alkyl
substituents (% by volume), based on the total gasoline. In the present invention,
if V(PA) is 0 or V(MA) is not 0, the ratio of V(PA) to V(MA) should be held more than
1, preferably 1.5, more preferably more than 2.
[0064] The above V(Bz), V(Tol), V(C
8A), V(C
9A), V(C
10+A), V(C
9+), V(MA) and V(PA) are determined by the procedure of JIS K 2536 "Testing Method for
Hydrocarbon Types in Petroleum Products by Gas Chromatography".
[0065] V(C
4) is the amount of a C
4 hydrocarbon, based on the total gasoline. V(C
4) should be in the range of 0 - 10 % by volume, preferably 0 - 5 % by volume, more
preferably 0 - 3 % by volume with a view to further reducing the amount of evaporative
emission. The C
4 hydrocarbon exemplarily includes n-butane, 2-methylbutane (isobutane), 1-butene,
2-butene and 2-mehtylpropene.
[0066] V(C
5) is the amount of a C
5 aliphatic hydrocarbon, based on the total gasoline. The lower limit of V(C
5) should be 10 % by volume, preferably 15 % by volume, while the upper limit should
be 35 % by volume, preferably 30 % by volume. The C
5 aliphatic hydrocarbon content more than 10 % by volume is contributive to the production
of an unleaded gasoline excelled in engine performance at normal temperatures. The
C
5 aliphatic hydrocarbon content less than 35 % by volume leads to an unleaded gasoline
improved in high temperature engine performance. When a consideration given to the
preclusion of gasoline coking in the injector, it is desired that the unsaturated
hydrocarbon content (V(C
5o)) (volume %) in the C
5 aliphatic hydrocarbon is 0, or the ratio of the saturated hydrocarbon content (V(C
5p)) (volume %) in the C
5 aliphatic hydrocarbon to (V(C
5o)), that is, (V(C
5p))/(V(C
5o)), is more than 1, preferably more than 1.5, more preferably more than 2, most preferably
3. The C
5 unsaturated aliphatic hydrocarbon exemplarily includes n-pentane, 2-methylbutane
(isopentane), and 2,2-dimethylpropane (neopentane), while the C
5 saturated aliphatic hydrocarbon exemplarily includes 1-pentene, 2-pentene, 2-methyl-1-butene,
2-methyl-2-butene and 3-methyl-1-butene.
[0067] V(C
6) is the amount of a C
6 aliphatic hydrocarbon, based on the total gasoline. The lower limit of the C
6 aliphatic hydrocarbon content is 10 % by volume, preferably 15 % by volume, while
the upper limit is 30 % by volume, preferably 25 % by volume. The C
6 aliphatic hydrocarbon content greater than 10 % by volume results in the production
of an unleaded gasoline excelled in normal temperature engine performance, while the
same less than 30 % by volume leads to the production of an leaded gasoline further
improved in high temperature engine performance. In view of prevention in gasoline
coking in the injector, it is desired that the unsaturated hydrocarbon content (V(C
6o)) (volume %) in the C
6 aliphatic hydrocarbon is 0, or the ratio of the saturated hydrocarbon content (V(C
6p)) (volume %) in the C
6 aliphatic hydrocarbon to (V(C
6o)), that is, (V(C
6p))/(V(C
6o)), is more than 2, preferably more than 3, more preferably more than 5, most preferably
10. The C
6 saturated aliphatic hydrocarbon exemplarily includes n-hexane, 2-methylpentane, 3-methylpentane,
2,2-dimethylbutane and 2,3-dimethylbutane, while the C
6 unsaturated aliphatic hydrocarbon exemplarily includes 1-hexene, 2-hexene, 3-hexene,
2-methyl-1-pentne, 3-methyl-1-pentene, 4-methyl-1-pentene, 2-mehtyl-2-pentene, 3-methyl-2-pentne,
4-methyl-2-pentene, 2,3-dimethyl-1-butene, 3,3-dimethyl-1-butene and 2,3-dimethyl-2-butene.
[0068] V(C
7+p) is the amount of a saturated aliphatic hydrocarbon having more than 7 carbon atoms,
based on the total gasoline. The lower limit of V(C
7+p) is 10 % by volume, preferably 20 % by volume, while the upper limit of the same
is 50 % by volume, preferably 45 % by volume. V(C
7+p) greater than 10 % by volume leads to an unleaded gasoline excelled in normal temperature
engine performance, while V(C
7+p) less than 50 % by volume leads to an unleaded gasoline excelled in high temperature
engine performance. The saturated aliphatic hydrocarbon of more than 7 carbon atoms
exemplarily includes n-heptane, 2-methylhexane, 3-methylhexane, 2,2-dimethyl pentane,
2,3-dimethylpentane, 2,4-dimethylpentane, 3,3-dimethylpentane, 3-ethylpentane and
2,2,3-trimethylbutane.
[0069] (C
9+) is the amount of a hydrocarbon having more than 9 carbon atoms, based on the total
gasoline. (C
9+) is in the range of 0 - 10 % by volume, preferably 0 - 5 % by volume. By reducing
the amount of the aliphatic compound having more than 9 carbon atoms, it makes it
possible to reduce the amount of gasoline which dilutes the engine oil thereby reducing
the amount of the exhaust hydrocarbon, preventing the engine oil from deterioration
and precluding sludge formation.
[0070] The above V(C
4), V(C
5), V(C
5p), V(C
5o), V(C
6), V(C
6p), V(C
6o), V(C
7+p) and V(C
9+) are as determined by gas chromatography. Analysis is made with the use of a methyl
silicone-made capillary column, a helium or nitrogen carrier gas and an FID detector
under a set of condition of 25 to 50 mm in length, 0.5 to 1.5 ml/min in gas flow rate,
1:50 to 1:250 in partition ratio, 150 to 250°C in inlet temperature, -10 to 10°C in
initial column temperature, 200 to 250°C in end column temperature and 150 to 250°C
in detector temperature.
[0071] No particular limitation is imposed upon the sulfur content of the inventive gasoline,
which however is less than 50 ppm, preferably less than 30 ppm, more preferably 20
ppm, most preferably less than 10 ppm, based on the total gasoline. This content if
larger than 50 ppm would be responsible for poisoning an after treatment catalyst,
increases of the concentrations of NOx, Co and Hc and a sharp rise in benzene emission.
[0072] The term "sulfur content" used herein refers to a sulfur content measured by the
method of JIS K 2541 "Testing Method for Sulfur in Crude Oil and Petroleum Products".
[0073] The unwashed existing gum and washed gum of the inventive gasoline should be in an
amount of less than 20 mg/100 ml and an amount of less than 3 mg/100 ml, preferably
less than 1 mg/100 ml, respectively as measured by the method of JIS K.2261 "Testing
Method for Existing Gum of Petroleum Products, Motor Gasolines and Aviation Fuels
by Spray Evaporation". Deviations from these amounts would lead to the formation of
deposits in the fuel-induction system and the occurrence of agglutination in the intake
valve.
[0074] The gross calorific value of the inventive gasoline should be more than 35,000 J/g,
preferably 40,000 J/g, more preferably 45,000 J/g as measure by JIS K 2279 "Testing
and Calculation Methods for Gross Calorific Value of Crude Oil and Petroleum Products".
[0075] The oxidation stability of the inventive gasoline should be over 480 minutes, preferably
over 1,440 minutes as measured by the method of JIS K 2287 "Testing Method for Gasoline
Oxidation Stability (Induction Period Method)". Oxidation stability less than 480
minutes would lead to the formation of gum during storage.
[0076] The inventive gasoline should exhibit 1 or lain the value of the copper corrosion
test conducted in accordance with the procedure of JIS K 2513 "Copper Corrosion Test
of Petroleum Products (at a temperature of 50°C for 3 hours)". Copper corrosion exceeding
1 would cause corrosion of the pipe of the fuel system.
[0077] The kerosene content of the inventive gasoline should be in the range of 0 - 4 %
by volume, based on the total gasoline. The kerosene content referred herein means
the content of a C
13 - C
14 hydrocarbon (% by volume) as quantitatively determined by the gas chromatographic
process in which a methyl-silicone caterpillar column having a column length of 25
- 50 m is fed with a helium or nitrogen gas at a flow rate of 0.5 - 1.5 ml/min and
a divisional ratio of 1:50 - 1:250 and operated at an inlet temperature of 150 - 250°C
and at initial column temperature of -10 -10°C and final column temperature of 150
- 250°C, and a hydrogen ion detector is operated at 150 - 250°C.
[0078] No particular restriction is imposed upon the production method for the unleaded
gasoline of the invention. There may be used any suitable known base gasolines such
as light naphtha derivable by atmospheric distillation of crude oil, cracked gasoline
derivable by catalytic cracking or hydrocracking, reformed gasoline obtainable by
catalytic reforming, polymerized gasoline available by olefin polymerization, alkylates
derivable addition reaction or alkylation of a hydrocarbon such as isobutane with
a lower olefin, isomerized gasoline derivable by converting light naphtha into isoparaffin
using an isomerization device, de-n-paraffinized oil, butane, aromatic hydrocarbons
and paraffinic fractions derivable by hydrocracking dimerized propylene.
[0079] A typical blend formulation of the inventive unleaded gasoline is shown below.
(1) reformed gasoline : 0 - 70 vol. %
(2) light fractions of reformed gasoline
(boiling at 25 - 120°C) : 0 - 35 vol. %
(3) heavy fractions of reformed gasoline
(boiling at 110 - 200°C) : 0 - 45 vol. %
(4) cracked gasoline : 0 - 50 vol. %
(5) light fractions of cracked gasoline
(boiling at 25 - 90°C) : 0 - 45 vol. %
(6) alkylate : 0 - 40 vol. %
(7) paraffin fraction derived from dimerizing and subsequently hydrogenating propylene
: 0 - 30 vol. %
(8) isomerized gasoline : 0 - 30 vol. %
(9) light naphtha : 0 - 10 vol. %
(10) butane : 0 - 10 vol. %
(11) oxygen-containing compound : 0.3 - 30 vol. %
[0080] Upon production of the inventive unleaded gasoline, any suitable methods can be employed
to reduce the benzene content in the inventive gasoline, one example of such methods
being to add smaller amount of reformed gasoline containing a large amount of benzene.
Alternatively, the benzene-content reduction can be achieved by using reformed gasoline
having been subjected to treatments for reducing the benzene content. Such treatments
are as follows :
(1) removing benzene fraction by distilling reformed gasoline,
(2) extracting benzene from reformed gasoline with sulforan or like solvents,
(3) converting benzene into other compounds by a method such as
(A) conversion into cyclohexane, methylcyclopentane and the like via hydrogenation
of benzene,
(B) conversion into toluene, xylene, ethylbenzene and the like via reaction of benzene
with C9 or greater aromatic hydrocarbon, or
(C) alkylation of benzene with lower olefins such as ethylene and propylene or with
lower alcohols such as methanol and ethanol
. (4) using as a reformer feed of desulfurized heavy naphtha derived by removing C6 hydrocarbons by distillation, and
(5) controlling the operation conditions of a catalytic reforming apparatus.
[0081] In a direct injection gasoline engines, there is a risk that due to the injector
being subjected to increased temperatures, the gasoline therein is coked by its denaturation,
leading to an increase in combustion chamber deposition (CCD). Therefore, the inventive
unleaded gasoline should be added with detergent additives such as succinic acid imide,
polyalkyl amine and polyetheramine so as to prevent injector coking and reduce CCD.
Preferred for such detergent additives are those which are free of residues after
being subject to thermal decomposition at 300°C in the air. The amount of the above
additives is less than 1 % by volume, preferably less 0.1 % by volume, based on the
total gasoline.
[0082] There may be used some conventional fuel additives exemplarily including antioxidants
such as phenol- or amine- ones, metallic inactivating agents such as Shiff-type compounds
or thioamide-type compounds, surface ignition preventers such as organophosphorus-derived
compounds, combustion adjuvants such as alkali metal or alkaline earth metal salts
of organic acids and sulfuric esters of higher alcohols, antistatic agents such as
anionic surfactants, cationic surfactants and amphoteric surfactants, colorants such
as azo dyes, rust preventives such as alkenyl succinate, identify agents such as quinizarin
and coumarin and malodorants such as natural essential-based aromatics. These may
be used in combination but preferably in an amount of less than 0.1 % by mass, based
on the total gasoline.
[0083] The invention will be further described by way of the following examples which however
should not be construed in a limiting sense.
[0084] There was prepared a variety of base gasolines each having the composition and properties
as indicated in Table 1.
Inventive Examples 1 - 6 and Comparative Examples 1 and 2
[0085] Sample gasolines for Inventive and Comparative Examples were prepared by blending
the base gasolines in accordance with the blending ratio indicated in Table 2. The
composition and properties of each sample gasoline are shown in Table 2.
[0086] Each of the sample gasolines thus obtained was evaluated in performance by the following
automotive tests.
Automotive Test 1
[0087] Using a diesel smoke meter, smoke exhaustion was measured on an automobile installed
with a 1.8-liter displacement, direct injection gasoline engines. During the test,
the automobile was kept to run at a constant speed of 40 km/h.
Automotive Test 2
[0088] A 2.0-liter displacement, direct injection gasoline engine was operated at a oil-water
temperature of 60 °C under the condition equivalent to the constant running at a speed
of 40 km/h for 150 hours and thereafeter the dilution of the engine oil by the gasoline
was measured.
[0089] As described above, the inventive unleaded gasoline contains a specified oxygen-containing
compound in a definite amount thereby redudng the amount of exhaust smoke and suppressing
smoldering of the spark plug and the formation of deposit in the combustion chamber,
leading to improved engine durability.
Table 1
| |
(A) base gasoline |
(B) base gasoline |
(C) MTBE |
(D) TAEE |
(E) MPA |
| RON |
100.2 |
102.9 |
118 |
111 |
53 |
| MON |
88.7 |
89.9 |
101 |
95 |
40 |
| Distillation properties (°C) |
Initial Boiling Point |
30.0 |
30.5 |
|
|
|
| T10 |
48.5 |
51.5 |
|
|
|
| T30 |
69.5 |
78.5 |
|
|
|
| T50 |
98.0 |
111.5 |
|
|
|
| T70 |
118.0 |
134.0 |
|
|
|
| T90 |
140.0 |
162.5 |
|
|
|
| End Point |
174.5 |
176.0 |
|
|
|
| RVP (kPa) |
75.0 |
70.0 |
53.3 |
12.5 |
2.0 |
| density (g/cm3) |
0.757 |
0.775 |
0.747 |
0.770 |
0.970 |
| Composition (vol. %) |
aromatics |
33 |
43 |
0 |
0 |
0 |
| olefins |
9 |
9 |
0 |
0 |
0 |
| paraffins |
58 |
49 |
0 |
0 |
0 |
| Bz |
0.7 |
0.5 |
0 |
0 |
0 |
| Kerosene content |
0 |
0 |
0 |
0 |
0 |
| oxygen content (mass %) |
0 |
0 |
18.2 |
13.8 |
36.4 |
| sulfur content (mass ppm) |
8 |
9 |
0 |
0 |
0 |
| MTBE : methyl-t-butyl-ether |
| TAEE : t-amylethyl-ether |
| MPA : methoxypropyl acetate |
Table 2
| |
Inventive Examples |
Comparative Examples |
| |
1 |
2 |
3 |
4 |
5 |
6 |
1 |
2 |
| Base gasoline Volume % |
(A) |
95 |
90 |
85 |
85 |
85 |
|
100 |
|
| (B) |
|
|
|
|
|
85 |
|
100 |
| (C) |
5 |
10 |
15 |
|
|
15 |
|
|
| (D) |
|
|
|
15 |
|
|
|
|
| (E) |
|
|
|
|
15 |
|
|
|
| oxygen content mass % |
0.9 |
1.8 |
2.7 |
2.9 |
6.7 |
1.8 |
0.0 |
0.0 |
| Distillation Properties to °C |
T10 |
48.5 |
49.0 |
50.5 |
54.5 |
52.5 |
52.0 |
48.5 |
51.5 |
| T30 |
66.5 |
66.0 |
65.0 |
78.5 |
80.0 |
74.0 |
69.5 |
78.5 |
| T50 |
94.5 |
88.0 |
84.5 |
101.0 |
112.0 |
108.5 |
98.0 |
111.5 |
| T70 |
116.0 |
115.0 |
113.0 |
114.0 |
127.5 |
127.0 |
118.0 |
134.0 |
| T80 |
140.5 |
140.0 |
138.0 |
136.5 |
141.0 |
158.5 |
140.0 |
162.5 |
| End Point |
175.0 |
176.0 |
175.5 |
176.0 |
164.0 |
173.0 |
174.5 |
176.0 |
| Aromatics |
31.5 |
29.9 |
28.2 |
28.2 |
28.2 |
37.3 |
33.2 |
43.1 |
| Paraffins |
54.7 |
51.8 |
49.0 |
49.0 |
49.0 |
41.0 |
57.6 |
49.1 |
| Olefins |
8.7 |
8.3 |
7.8 |
7.8 |
7.8 |
6.7 |
9.2 |
7.8 |
| Composition Vol. % |
V(Bz) |
0.7 |
0.6 |
0.6 |
0.6 |
0.6 |
0.5 |
0.7 |
0.5 |
| V(Tol) |
12.6 |
12.0 |
11.3 |
11.3 |
11.3 |
9.4 |
13.3 |
11.2 |
| V(C8A) |
9.1 |
8.6 |
8.2 |
8.2 |
8.2 |
7.2 |
9.6 |
8.6 |
| V(C9A) |
8.6 |
8.1 |
7.7 |
7.7 |
7.7 |
19.5 |
9.0 |
21.9 |
| V(C10+A) |
0.6 |
0.5 |
0.5 |
0.5 |
0.5 |
0.8 |
0.6 |
0.9 |
| V(MA)/V(PA) |
1.9 |
1.9 |
1.9 |
1.9 |
1.9 |
1.7 |
1.9 |
1.6 |
| V(C4) |
8.4 |
7.9 |
7.5 |
7.5 |
7.5 |
6.3 |
8.8 |
7.5 |
| V(C5p) |
9.1 |
8.6 |
8.2 |
8.2 |
8.2 |
6.8 |
9.6 |
8.2 |
| V(C5o) |
5.2 |
5.0 |
4.7 |
4.7 |
4.7 |
3.9 |
5.5 |
4.7 |
| V(C6p) |
6.0 |
5.7 |
5.4 |
5.4 |
5.4 |
4.5 |
6.3 |
5.4 |
| V(C6o) |
3.5 |
3.3 |
3.1 |
3.1 |
3.1 |
2.6 |
3.7 |
3.1 |
| V(C7+p) |
31.3 |
29.6 |
28.0 |
28.0 |
28.0 |
23.4 |
32.9 |
28.0 |
| V(C9+) |
9.1 |
8.6 |
8.2 |
8.2 |
8.2 |
20.2 |
9.6 |
22.8 |
| kerosene content |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
| RON |
101.3 |
102.5 |
102.9 |
102.0 |
90.5 |
104.5 |
100.2 |
102.9 |
| MON |
89.0 |
90.0 |
90.1 |
89.9 |
80.6 |
92.3 |
88.7 |
89.9 |
| RVP kPa |
76.0 |
77.5 |
77.5 |
74.5 |
72.0 |
72.0 |
75.0 |
70.0 |
| density g/cm3 |
0.756 |
0.755 |
0.755 |
0.769 |
0.792 |
0.776 |
0.757 |
0.775 |
| sulfur content mass ppm |
7 |
8 |
8 |
7 |
8 |
7 |
8 |
9 |
| Unwashed existent gum mg/100mL |
1 |
1 |
1 |
1 |
1 |
1 |
1 |
1 |
| washed existent gum mg/100mL |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| oxidation stability |
>1440 |
>1440 |
>1440 |
>1440 |
1440> |
>1440 |
>1440 |
>1440 |
| copper corrosion |
1A |
1A |
1A |
1A |
1A |
1A |
1A |
1A |
| Automobile Test 1 smoke % |
4.7 |
2.9 |
1.8 |
3.3 |
2.8 |
4.8 |
6.5 |
9.3 |
Automobile Test 2
dilution by gasoline vol. % |
5.7 |
6.2 |
5.5 |
6.3 |
6.4 |
7.4 |
6.3 |
8.5 |