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Fuels and their combustion
605
whole charge in the cylinder tends to fire simultaneously, causing violent
combustion. With a short delay, ignition is initiated at several points, and the
flame subsequently spreads progressively throughout the charge. On the
other hand, the injection must be timed appropriately relative to the cetane
number of the fuel that will be used: a higher cetane number than that for
which the timing was set can lead to ignition before adequate mixing has
occurred and thus increase emissions.
Cetane number is defined precisely as the percentage of n-cetane + 0.15
times the percentage of heptamethylnonane contents of the blend of reference
fuel having the same ignition quality as the fuel under test. Ignition quality
is determined by varying the compression ratio to give the same ignition
delay period for the test fuel and two blends of reference fuels. One blend
has to be of better and the other of poorer ignition quality than the test fuel,
but the difference between the two has to be no more than five cetane numbers.
The cetane number is obtained by interpolation between the results obtained
at the highest and lowest compression ratios.
Carrying out these laboratory engine tests, however, is not at all convenient,
so two other criteria are widely used. One is the diesel index and the other
the cetane index. The diesel index, which is obtained mathematically, is
computed by multiplying the aniline point of the fuel by its API gravity/100.
The aniline point is the lowest temperature in degrees fahrenheit at which the
fuel is completely miscible with an equal volume of freshly distilled aniline,
which is phenylamine aminobenzene. API, measured with a hydrometer,
stands for American Petroleum Institution, and degrees API = (141.5/Specific
gravity at 60°F) – 131.5 It is a measure of density for liquids lighter than
water.
The cetane index is calculated from API gravity and volatility, the latter
originally taken as represented by its mid-volatility, or mid-boiling point
(50% recovery temperature, T50). Since its introduction, the formula has
been modified from time to time, to keep up with advancing fuel technology,
and is now based on an extremely complex formula embracing the density
and volatility of three fractions of the fuel (those at the 10, 50 and 90%
distillation temperatures T10, T50 and T90, respectively). This formula can be
found in Automotive Fuels and Fuel Systems, Vol. 2, T.K. Garrett, Wiley.
The cetane index is, in general, better than the diesel index as an indication
of what the cetane number of a fuel would be if tested in a CFR engine in a
laboratory, and it is much less costly and time-consuming to obtain. In general,
alkanes have high, aromatics low, and naphthenes intermediate, cetane and
diesel indices.
Values of 50 or above for either the diesel or cetane index indicate good
combustion and ignition characteristics, below 40 are totally unacceptable
and even below 45 undesirable. Low values mean difficult cold starting the
generation of white smoke, and the engine will be noisy.
BS 2869: Part 1: 1988 prescribes minimum limits of 48 for the cetane
number and 46 for the cetane index. In Europe and Japan the minimum
cetane number requirement is 45, and in the USA it is 40, the latter possibly
being because a high proportion of their crude oil comes from Mexico and
Venezuela. A reduction in cetane number from 50 to 40 leads to an increase
in the ignition delay period of about 2° crankshaft angle in a direct and about
half that angle in an indirect injection engine.
606
17.17
The Motor Vehicle
Tendency to deposit wax
In cold weather, a surprisingly small wax content, even as little as 2%, can
crystallise out and partially gel a fuel. These crystals can block the fuel
filters interposed between the tank and injection equipment of the engine,
and ultimately cause the engine to stall. In very severe conditions, the pipelines
can become blocked and a thick layer of wax may sink to the bottom of the
fuel tank. Paraffins are the most likely constituents to deposit wax which,
because they have high cetane numbers, is unfortunate.
The various measures of the tendency of a fuel to precipitate wax include
cloud point, which is the temperature at which the wax, coming out of
solution, first becomes visible as the fuel is cooled (ASTM test D 2500).
Another test (ASTM 3117) is for the wax appearance point, which is that at
which the wax crystals become visible in a swirling sample of fuel.
Then there is the pour point, which is the temperature at which the quantity
of wax in the fuel is such as to cause it to begin to gel (ASTM D97). To
establish the pour point, checks on the condition of the fuel are made a 3°C
intervals by removing the test vessel from the cooling bath and tilting it to
see if the fuel flows. Another criterion, the gel point, is that at which the fuel
will not flow out when the vessel is held horizontal. In practical terms, this
translates roughly into a temperature 3° above that at which it becomes no
longer possible to pour the fuel out of a test tube.
Another way of estimating operational performance of a fuel is to combine
the cloud point, CP, and the difference between it and the pour point, PP, to
obtain a wax precipitation index, WPI. The formula for doing this is as
follows—
1
WPI = CP – 1.3(CP – PP – 1.1) 2
Other tests include the cold filter plugging point (CFPP) of distillate fuels,
IP 309/80 and the CEN European Standard EN116: 1981. This the lowest
temperature at which 20 ml of the fuel will pass through a 45 µm fine wiremesh screen in less than 60 s. However, since paper element filters are now
widely used, the relevance of wire-mesh filters is open to question so, at the
time of writing, the CEN is debating the desirability of introducing a test
called the simulated filter plugging point. In the USA, the low temperature
fuel test (LTFT) is preferred to the CEPP test. The LTFT is the temperature
at which 180 ml of fuel passes through a 17 µm screen in less than 60 s. All
these and other tests are described in detail in Automotive Fuels and Fuel
Systems, Vol. 2, T.K. Garrett, Wiley.
17.18
Density
Because injection equipment meters the fuel on a volume basis, any variations
in density, because it is related to energy content, will affect the power
output. The greater the density of the fuel the higher will be both the power
and smoke. Fortunately, however, hydrocarbon fuels differ relatively little as
regards their densities.
Density is measured by the use of a hydrometer with scales indicating
specific gravity or g/m3. The sample should be tested at 15°C or the appropriate
correction applied. Figures for density differ from those for API gravity, or
deg API, in that the higher the number in deg API gravity, the lighter is the
fuel.
Fuels and their combustion
17.19
607
Volatility
The volatility of the fuel influences many other properties, including density,
auto-ignition temperature, flashpoint, viscosity and cetane number. Obviously,
the higher the volatility the more easily does the fuel vaporise in the combustion
chamber. Low-volatility components may not burn completely and therefore
could leave deposits and increase smoke. Within the range 350 to 400°C,
however, the effects of low volatility on exhaust emissions are relatively
small. The mix of volatilities is important: high-volatility components at the
lower end of the curve in Fig. 17.8 improve cold starting and warm-up while,
at the upper end components having volatilities that are too low increase
deposits, smoke and wear.
17.20
Viscosity
The unit of kinematic viscosity is the stoke, which is the time taken for a
certain volume of fuel at a prescribed temperature and a constant head to
flow under the influence of gravity through a capillary tube of a prescribed
diameter. That of absolute velocity is the poise, which is the force required
to move an area of 1 cm2 at a speed of 1 cm/s past two parallel surfaces that
are separated by the fluid. For convenience, the figures are usually expressed
in centipoises and centistokes (cP and cSt). The two are related in that cP =
cSt × Density of the fluid. The SI units are m2/s, and the CGS or stoke’s units
are cm2/s (see also Section 18.4).
Increasing viscosity reduces the cone angle of the injected spray and the
distribution and penetration of the fuel, while increasing the size of the
droplets. It will therefore affect optimum injection timing. An upper limit for
viscosity has to be specified to ensure adequate fuel flow for cold starting.
Lucas Diesel Systems quote a figure of 48 cSt at –20°C as the upper and, to
guard against loss of power at high temperatures, 1.6 cSt at 70°C as the
lower limit. BS 2869 calls for a maximum value of 5 cSt and a minimum of
2.5 cSt at 40°C. In Fig. 17.9, all these points are plotted and a viscosity
tolerance band established. The viscosity of the average fuel lies approximately
mid-way between the upper and lower limits.
Too high a viscosity can cause excessive heat generation in the injection
equipment, owing to viscous shear in the clearances between the pump plungers
and their bores. On the other hand, if it is too low, the leakage through those
clearances, especially at low speeds, can be so high that restarting a hot
engine can become impossible. This, however, is because the increase in
temperature of the fuel locally due to conduction of heat to the injection
system during a short shut-down period further reduces the viscosity of the
fuel in the pump prior to starting.
17.21
Smoke
When the engine is started from cold, white smoke comprising tiny droplets
of liquid, mainly fuel and water, increases as cetane number and volatility of
the fuel are reduced. It persists until the temperature has risen to the point at
which the droplets are vaporised in the engine and remain so until well after
they have issued from the exhaust tail pipe. The reason why the fuel droplets,
although surrounded in the combustion chamber by excess oxygen, remain
608
The Motor Vehicle
48.0
40
Kinematic viscosity of fuel, cSt
20
10
5.0
4
2.5
2
1.6
–20 –10
0
10
20
30
40
50
Temperature of fuel, °C
60
70
Fig. 17.9 A typical tolerance band for fuel viscosity is illustrated here. At 40°C, the
limits are from 2.5 to 5.0 cSt
unburnt is that, in the cold environment, not only do they not evaporate but
also their temperature never rises to that of auto-ignition.
Cetane number increases with the density and volatility, and varies with
composition of the fuel. Fuels having high cetane numbers are principally
the paraffinic straight-run distillates. However, because these have both high
cloud points and low volatility, a compromise has to be struck between good
ignition quality and suitability for cold weather operation.
Another product of combustion can be black smoke. This is formed because
the hydrogen molecules are oxidised preferentially so, if there is insufficient
oxygen in their vicinity, it is the carbon atoms that remain unburnt. High aromatic
content, viscosity and density and low volatility all increase the tendency to
produce black smoke.
Although aromatics tend to produce smoke, they also make a major
contribution to the lubricity of the fuel. Consequently, their removal can give
rise to abnormally high rates of wear of injection pumps, especially in
distributor-type pumps in which all the work is done by only one or two
plungers and, perhaps, a single delivery passage might be subject to severe
erosion.
As previously explained, the volatility factor is misleading. Because the
more volatile fuels have high API gravities (indicating low specific gravities),
and their low viscosities allow more to escape back past the injection pumping
elements, the weight delivered to the cylinder per injection is smaller. For
any given power, a certain weight of fuel must be injected, so a greater
volume of the more volatile fuel and a longer injection period are therefore
Fuels and their combustion
609
required, and this might affect droplet size. Depending on the air movement
and other conditions in the combustion chamber, such changes could have
either a beneficial or adverse effect on combustion and therefore smoke
generation.
17.22
Particulates
Even though more than 90% of the total mass of particulates in the exhaust,
Fig. 17.10, is carbon, sulphur compounds are a problem too. Moreover, as
advances in engine and injection equipment design lead to reduced carbon
particulates from both the fuel and lubricating oil, sulphur could become a
significantly higher proportion of the total. Removal of sulphur from the fuel
is a costly, though necessary, process.
17.23
Additives
Until the mid-nineteen-seventies, the diesel fuel generally available in the
UK and Europe was of a very high quality. Subsequently, on account of a
shortage of appropriate crude oils, the quality world-wide showed a tendency
to fall, though not as rapidly as had been expected. Since fuel reserves are
being consumed at an increasing rate, the trend inevitably will remain
downwards unless some economical way of synthesising high quality diesel
fuel in the enormous quantities required can be developed. The trend has
already led to the introduction of additives many of which hitherto had been
entirely unnecessary and therefore not even under serious consideration.
Even so, there is no incentive for the oil companies to use additives unless
they are cost-effective. Some are sold in the after-market but, unless the
purchaser knows in detail the content of his fuel, he could be either paying
for products that do not suit it or simply adding to what is already present at
saturation level, in which event the extra will make little or no difference. A
possible exception is where a commercial vehicle operator has a large residual
stock of fuel bought in bulk during the summer, which he needs to convert
by adding anti-wax additives for winter use.
Residue
Sulphur
dependent
NOx
HC
HC
Soot
Soot
CO
Pollutants
Particulates
Fig. 17.10 Typical analysis of the pollutants in the exhaust from a diesel engine
610
The Motor Vehicle
17.24 The effects of additives on combustion and
performance
Type of operation
One of the early entrants, in 1988, into the multi-additive diesel fuels market
was Shell’s Advanced Diesel. This contains several additives, one of which
has raised its cetane number from the 48 required by British Standards, and
the minimum of 50 for Shell’s base fuel, to typically between 54 and 56.
Among the others are a corrosion inhibitor, anti-foam, cold flow and reodorant additives. The benefits claimed include lower noise, 3% better fuel
economy, Fig. 17.11, 8.4% less black and white smoke Fig. 17.12, a general
improvement in overall engine performance and durability, and a reduction
in vehicle downtime.
Of all the additives available, the most obviously important to the operator
are the cetane improvers and those that help to overcome the tendency to
wax precipitation in winter. Others used include anti-oxidants, combustion
Road tankers
City delivery
Long haul
Long haul
City delivery
Short haul
Road tankers
Bus fleet
Bus fleet
Bus fleet
Commercial delivery
Road tankers
Average saving
5.39%
0.27%
2.2%
0
1
2
3
4
5
Fuel saved, %
6
Fig. 17.11 Considerable scatter of results were apparent in fuel consumption trials
instituted by Shell on several different fleets and types of operation. Among the
variables of course are driver habits
White
smoke
Black
smoke
8.4%
10
% 20
25%
30
Fig. 17.12 Results of tests carried out by Shell to show that their Advanced Diesel
fuel offered a reduction of 25% in white and 8.4% in black smoke as compared with
another commercially available fuel
Fuels and their combustion
611
improvers, cold flow improvers, corrosion inhibitors, detergents, re-odorants,
anti-foamants and, less commonly, stabilisers, dehazers, metal deactivators,
biocides, anti-icers, and demulsifiers. Anti-static additives are used too, but
mainly to benefit the blenders by facilitating storage, handling and distribution.
17.25
Cetane number and cetane improvers
Because cetane number is a measure of the ignitability of the fuel, Fig.17.13,
a low value may render starting in cold weather difficult and increase the
tendency towards the generation of white smoke, Fig. 17.14. It also increases
the ignition delay (interval between injection and ignition). As a result, fuel
must be injected into the combustion chamber earlier. Consequently, more
fuel is injected before ignition occurs, so the ultimate rate of pressure rise is
more rapid, and the engine therefore noisy. Also, because the fuel has less
time to burn before the exhaust valve opens, the hydrocarbon emissions are
increased.
On the other hand, if the cetane number is higher than that for which the
injection system is timed, power will be lost because a high proportion of the
pressure rise will occur when the piston is at or near TDC. Furthermore, the
Fig. 17.13 Combustion sequences photographed through a quartz window in the
piston crown of an engine running on (top) a commercially available alternative fuel
and (bottom) Shell Advanced Diesel. The two part circles are the inlet and exhaust
valve heads and the bright spot to the left of the cylinder is an illuminated pointer over
degree markings on the flywheel, which are too small to be visually identifiable here
Fig. 17.14 Two photographs showing white smoke in the exhaust gases of an engine
running on (left) a commercially available fuel and (right) Shell Advanced Diesel
612
The Motor Vehicle
fuel might ignite before it has mixed adequately with the air, so smoke and
hydrocarbon emissions may be experienced. Consequently, fuels having high
cetane numbers perform best when the injection is retarded. Conversely,
with too much retard, there will not be enough time for complete combustion,
so smoke and hydrocarbon emissions will again be the outcome. Since high
cetane numbers are difficult to achieve, the regulations in most countries
specify only the lowest limit that is acceptable.
Cetane improvers, mainly alkyl nitrates, are substances that decompose
easily and form free radicals at the high temperatures in combustion chambers.
Unfortunately, however, it is the fuels that have the lowest cetane numbers
that tend to respond least to cetane improvers.
Combustion improvers differ from cetane improvers in that they are mainly
organic compounds of metals such as barium, calcium, manganese or iron
and are catalytic in action. Barium compounds could be toxic, so interest
now centres mainly on the others. Although these compounds produce metalbased particulates, they also lower the auto-ignition temperature of the carbonbased deposits in both the cylinders and particle traps, causing them to be
more easily ignited.
17.26
Cold weather problems
A surprisingly small wax content can partially gel a fuel. Different countries
specify cold filter plugging points ranging from about –5°C in the Mediterranean region to –32°C in the far north. In practical terms, the basic consideration
is that the engine shall start at the lowest over-night soaking temperature
likely to be experienced in service. Once it has started, if the filter becomes
partially blocked, the rate of flow could be such that the return flow of warm
fuel to the tank is reduced, and therefore also the rate at which the temperature
of the fuel in the tank is raised.
17.27
Cold weather additives
All additives for cold weather operation modify the shapes of the wax crystals,
which otherwise tend to adhere to each other. They therefore come under the
general heading of wax crystal modifiers (WCMs). From Stoke’s law we
deduce that the rate of settling of crystals is directly proportional to the
square of their diameter times the difference between their density and that
of the fluid, and is inversely proportional to the viscosity of the fluid.
Consequently, small crystal size is the overriding need.
There are three types of modifier: pour-point depressants flow improvers
and cloud-point depressants. Which of these is used depends basically on
local requirements and the type of wax to be treated. The last mentioned is
mainly a function of the boiling range of the distillates and the country of
origin of crude oil. In general, cracked products contain high proportions of
aromatics, which have low cetane numbers, but they also contain less wax
and, moreover, dissolve what wax there is more readily than do straightdistilled fuels. Fuels having narrow boiling ranges form large wax crystals
that are less susceptible to treatment by additives than the smaller and more
regular-shaped crystals formed in fuels having wider boiling ranges.
The earliest WCM additives were the pour-point depressants (PPDs)
introduced in the 1950s. These modify the shape and reduce the size of the
Fuels and their combustion
613
wax crystals. The flat plates of naturally formed wax crystals tend to overlap
and interlock, and thus to gel the fuel. Those formed in the presence of a
PPD, however, are thicker and smaller, and some multi-axial needle crystals
are introduced between the platelets, all of which makes it more difficult for
them to interlock.
More effective are the flow improvers. These cause small multi-axial
needle crystals to form, instead of larger platelets. Moreover, by virtue of the
presence of some additive molecules between the crystals, they tend not to
adhere to each other. Although these crystals will pass through wire-gauze
strainers, they are stopped by the finer filters used to protect the injection
pumps and injectors. Even so, by virtue of their small size and the multiaxial arrangement of the needles, the unaffected liquid fuel still tends to pass
between them.
The small compact wax crystals tend to settle in the bottoms of tanks.
This is more of a problem in storage than vehicles, but wax anti-settling
additives (WASAs) can nevertheless play a useful part in the avoidance of
wax enrichment as vehicle fuel tanks become empty, especially in very cold
climates. These, too, modify the crystal formation, by both forming nuclei
and arresting growth. As the temperature of the fuel falls through the cloud
point, their nuclei form centres on which small wax crystals grow and
subsequently, other additive molecules attach to their surfaces and block
further growth. Primarily, these additives improve cold filterability, but they
also lower the pour point.
Although a cloud-point depressant by itself lowers the cold filter-plugging
point of a base fuel, the opposite effect may be obtained by using it in a fuel
containing also a flow improver. The improvement obtainable by cloudpoint depressants is generally only small, of the order of 3°C, and they are
costly. Therefore they are unattractive, except where the cloud point is included
as part of a diesel-fuel specification and the blender therefore wishes to
lower it.
17.28
Dispersants and corrosion inhibitors
The primary function of dispersant additives is to restrict the size of the
particles formed within the fuel at the high temperatures in the engine and,
additionally, to remove them from the metal surfaces. However, they must be
used continuously, otherwise gum deposits that form when they are not
present are dislodged when they are, and tend to block filters.
There are also dispersant modifiers, or detergents, which keep the surfaces
of the combustion chambers and injection nozzles clean. However, if used to
excess, some can actually cause gums to form.
Finally, there are corrosion inhibitors for protecting fuel-system components
and also bulk storage tanks and barrels.
Fuel surfaces can be oxidised in contact with air, causing the formation of
gums, sludges and sediments. Surface-active additives can help to prevent this,
but must be added immediately after refining the fuel and while it is still warm.
17.29
Detergents and anti-corrosion additives
Detergents are used mainly to remove carbonaceous and gummy deposits
from the fuel-injection system. Gum can cause sticking of injector needles,
614
The Motor Vehicle
while lacquer and carbon deposited on the needles can restrict the flow of
fuel, distort the spray and even totally block one or more of the holes in a
multi-hole injector, Fig. 17.15. The outcome can be misfiring, loss of power,
increased noise, fuel consumption, and hydrocarbon, CO, smoke and particulate
emissions in general, Fig. 17.16. Furthermore, starting may become difficult,
because the fuel droplets have become too large owing to the reduction in
flow rate.
Detergent molecules are characterised by, at one end, a head comprising
a polar group and, at the other, an oleofilic tail. The arms of the polar group
latch on to the metal and particulate molecules, Fig. 17.17. Those attached to
the metal form barrier films inhibiting deposition and, incidentally, offering
a degree of protection against corrosion, while those latched on to the
particulates are swept away with the fuel because their oleofilic tails carry
them into solution in it.
Fig. 17.15 Effects of carbon deposits on diesel injector sprays: (left) a new and (right)
a sooty injector
%
–25
–20
–15
–10
–5
0
CO
HC
(HC + NOx)Particles
Fig. 17.16 The left- and right-hand columns represent respectively the percentage
exhaust clean-up and actual output levels measured after 4000 and 15 000 miles
respectively during road tests with Shell Advanced Diesel fuel. The exhaust emissions
measurements were taken while running with the vehicle on a chassis dynamometer
immediately after it had completed its road mileage
Fuels and their combustion
Detergent
molecule
latched on
to carbon
particle
615
Carbon
particle
Free detergent
molecule
Detergent latched on to
metal molecules
Wall of manifold
Fig. 17.17 Molecules of detergent additives in fuels are held in solution by their tails,
while their polar heads latch on to the molecules of the contaminant. In application to
lubricants, some additives have molecules that also latch on to those of the metal
surfaces, leaving the tails to protect the latter from corrosion. Alternatively, different
additives, functioning in a similar manner but latching only on to the metal, may be
used for protecting it against corrosion
Anti-corrosion additives (perhaps about 5 ppm) are mainly used to protect
pipelines in which diesel fuel is transported, but no more than trace proportions
are likely to remain by the time it reaches the vehicle. Therefore, if vehicle
fuel-system protection is required too, the treatment must be heavier. As in
the case of the detergents, the polar heads attach themselves to the metal, but
the water repellent tails form an oily coating over the surface to protect it
against corrosive attack. In Fig. 17.18, test samples that have been left over
a long period in the base fuel are compared with those left in Shell Advanced
Diesel.
17.30
Anti-foamants and re-odorants
To allow the fuel tank to be completely filled more rapidly, and to avoid
splashing, surfactant anti-foamant additives are used. The inclusion of re-
Fig. 17.18 Specimens subjected to the ASTM D.665A corrosion test: (top) with Shell
Advanced Diesel and (below) in a commercially available alternative fuel