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Design and Simulation of Two Stroke Engines

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Chapter 2 - Gas Flow through <strong>Two</strong>-<strong>Stroke</strong> <strong>Engines</strong><br />

reflected pressure, Xr, from a known value <strong>of</strong> the incident pressure, Xj, at the plain open end.<br />

The solution is expressed as a function <strong>of</strong> the unknown quantity, Xr, as follows:<br />

W4 x i + x r - J— x : z~rz f: ^GT<br />

G5 i + G6(Xi + xr - i) v " X i _ 0 (2.8.16)<br />

This is solved by the Newton Raphson method, i.e., by differentiation <strong>of</strong> the above equation<br />

with respect to the unknown quantity, Xr, <strong>and</strong> iterating for the answer in the classic<br />

mathematical manner. Thence the value <strong>of</strong> particle velocity, cr, can be derived "approximately"<br />

from substitution into the equation below once the unknown quantity, Xr, is determined.<br />

cs = ci + cr = G5ao(Xi-Xr) (2.8.17)<br />

This is a far from satisfactory solution to an apparently simple problem. In actual fact, the<br />

inflow process at a plain open-ended pipe is a singular manifestation <strong>of</strong> what is generally<br />

called "cylinder to pipe outflow from an engine." In this case the atmosphere is the very large<br />

"cylinder" flowing gas into a pipe! Thus, as this complex problem is treated in great detail<br />

later in Sec. 2.17, <strong>and</strong> this present boundary condition <strong>of</strong> inflow at a plain-ended pipe can be<br />

calculated by the same theoretical approach as for pipe to cylinder flow, further wasteful<br />

simplistic explanation is curtailed until that point in the text has been reached.<br />

2.9 An introduction to reflection <strong>of</strong> pressure waves at a sudden area change<br />

It is quite common to find a sudden area change within a pipe or duct attached to an<br />

engine. In Fig. 2.6 at position 10 there are sudden enlargements <strong>and</strong> contractions in pipe area.<br />

The basic difference, gas dynamically speaking, between a sudden enlargement <strong>and</strong> contraction<br />

in pipe area, such as at position 10, <strong>and</strong> a plenum or volume, such as at position 2, is that<br />

the flow in the duct is considered to be one-dimensional whereas in the plenum or volume it<br />

is considered to be three-dimensional. A subsidiary definition is one where the particle velocity<br />

in a plenum or volume is so low as to be always considered as zero in any thermodynamic<br />

analysis. This will produce a change in amplitude <strong>of</strong> the transmitted pulse beyond the area<br />

change <strong>and</strong> also cause a wave reflection from it. Such sudden area changes are sketched in<br />

Fig. 2.8, <strong>and</strong> it can be seen that the pipe area can contract or exp<strong>and</strong> at the junction. In each<br />

case, the incident wave at the sudden area change is depicted as propagating rightward, with<br />

the pipe nomenclature as 1 for the wave arrival pipe, with "i" signifying the incident pulse,<br />

"r" the reflected pulse <strong>and</strong> "s" the superposition condition. The X value shown is the conventional<br />

symbolism for pressure amplitude ratio <strong>and</strong> p is that for absolute pressure. For example,<br />

at any instant, the incident pressure pulses at the junction are pji <strong>and</strong> pi2 which, depending<br />

on the areas Ai <strong>and</strong> A2, will give rise to reflected pulses, pri <strong>and</strong> pr2-<br />

In either expansion or contraction <strong>of</strong> the pipe area the particle flow is considered to be<br />

proceeding from the upstream superposition station 1 to the downstream superposition station<br />

2. Therefore the properties <strong>and</strong> composition <strong>of</strong> the gas particles which are considered to<br />

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