3.2 Combustion
Experiments
82
3.2.1.1
Gas Preparation
Gas conditions in the combustion could be controlled using two methods:
a)
Heating the air up using an inline air process heater and
b)
Pre-combustion in the vessel under lean conditions.
The heater and the gas mixing manifold can be seen in Figure 3.8. The air process
heater enabled reaching temperatures of up to 700 °C at the exit from the heater and
dependent upon set-up inside the combustion vessel and heat losses in the gas injection
lines, temperatures above 250 °C could be achieved within
the chamber for short
periods of time. Vessel was heated up by running heated high pressure air through the
Figure 3.8: Top: Farnam air process heater, Bottom: gas mixing manifold
Gas mixing
manifold
Compressed air
inlet
Fuel inlet
Gas mixing
manifold secondary
exhaust
Pressure
transducer
Farnham
process
heater
Compressed air inlet
Heater control
module
Thermocouple
3.2 Combustion Experiments
83
system until certain wall and air temperatures were achieved.
The low thermal inertia
of the rig meant that up to 3 hours was required to reach 80 °C wall temperature but
also that the temperature could be maintained throughout spray and gasoline vapour
combustion events without experiencing a significant drop. The large volume of the
vessel (22.5l) enabled large number of spray combustions before oxygen levels were
depleted to a critical level, thus speeding up experimental time. This was especially
true for raised initial air pressures.
The pre-combustion method allowed for much increased pressure and
temperature conditions for a short time period. A lean mixture of gaseous fuel was
ignited, giving EGR-like conditions before spray combustion.
This method can
potentially simulate engine conditions better than the heater method but repeat
experiments under same conditions are time consuming. The pre-combustion gaseous
fuel mixture could be prepared based on partial pressures. Dalton’s law of partial
pressures states that the ratio of partial pressures of air and fuel is the same as their
molar ratio [220]. This can be expressed as:
𝑃
𝑓
=
𝑛
𝑓
𝑛
𝑎𝑖𝑟
× 𝑃
𝑎𝑖𝑟
3.2
Generally the pre-combustion method suits better
diesel combustion where
spray variability does not play as much a role as in gasoline combustion where it is
additionally accompanied by spark variability and as a result a larger number of
repeats is required for a statistically relevant average [114].
Additionally to spray combustion, a combination of syringe pump and heater
was used for gasoline vapour combustion. Heated fuel would be pumped at a constant
rate into the pre-heated vessel where it would evaporate and result in a homogeneous
air-fuel mixture. Although typical experimental timescales involved were an order of
magnitude longer per combustion event, the pressure rise from the pre-mixed
gasoline
combustion event was more than 2 magnitudes of order higher. As a result the error
deriving from limitations in pressure transducer sensitivity was reduced.
The air-fuel mixing was aided by a 70 mm brass fan, driven by a 1.3 kW 3,000
rpm electric motor. The fan mount replaced one of the quartz windows to allow for
improved gas mixing while filling the vessel with pre-combustion gases/ gasoline
vapour. The fan location is as shown in Figure 3.9.
3.2 Combustion Experiments
84
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