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<strong>MAN</strong> B&W 15.05<br />

Calculati<strong>on</strong> of Exhaust Gas Back�Pressure<br />

The exhaust gas back pressure after the turbo�<br />

charger(s) depends <strong>on</strong> the total pressure drop in<br />

the exhaust gas piping system.<br />

The comp<strong>on</strong>ents, exhaust gas boiler, silencer, and<br />

spark arrester, if fitted, usually c<strong>on</strong>tribute with a<br />

major part of the dynamic pressure drop through<br />

the entire exhaust gas piping system.<br />

The comp<strong>on</strong>ents menti<strong>on</strong>ed are to be specified<br />

so that the sum of the dynamic pressure drop<br />

through the different comp<strong>on</strong>ents should, if possible,<br />

approach 200 mm WC at an exhaust gas<br />

flow volume corresp<strong>on</strong>ding to the specified MCR<br />

at tropical ambient c<strong>on</strong>diti<strong>on</strong>s. Then there will be<br />

a pressure drop of 00 mm WC for d<str<strong>on</strong>g>is</str<strong>on</strong>g>tributi<strong>on</strong><br />

am<strong>on</strong>g the remaining piping system.<br />

Fig. 5.05.0 shows some guidelines regarding<br />

res<str<strong>on</strong>g>is</str<strong>on</strong>g>tance coefficients and back�pressure loss<br />

calculati<strong>on</strong>s which can be used, if the maker’s<br />

data for back�pressure <str<strong>on</strong>g>is</str<strong>on</strong>g> not <str<strong>on</strong>g>available</str<strong>on</strong>g> at an early<br />

stage of the project.<br />

The pressure loss calculati<strong>on</strong>s have to be based<br />

<strong>on</strong> the actual exhaust gas amount and temperature<br />

valid for specified MCR. Some general formulas<br />

and definiti<strong>on</strong>s are given in the following.<br />

Exhaust gas data<br />

M: exhaust gas amount at specified MCR in kg/sec.<br />

T: exhaust gas temperature at specified MCR in °C<br />

Please note that the actual exhaust gas temperature<br />

<str<strong>on</strong>g>is</str<strong>on</strong>g> different before and after the boiler. The<br />

exhaust gas data valid after the turbocharger may<br />

be found in Chapter 6.<br />

Mass density of exhaust gas (ρ)<br />

ρ ≅ .293 x 273 ______ x .0 5 in kg/m3<br />

273 + T<br />

The factor .0 5 refers to the average back�pressure<br />

of 50 mm WC (0.0 5 bar) in the exhaust gas<br />

system.<br />

Exhaust gas velocity (v)<br />

Page of 3<br />

In a pipe with diameter D the exhaust gas velocity <str<strong>on</strong>g>is</str<strong>on</strong>g>:<br />

v = M __<br />

ρ<br />

4<br />

x _____<br />

π x D2 in m/s<br />

Pressure losses in pipes (∆p)<br />

For a pipe element, like a bend etc., with the res<str<strong>on</strong>g>is</str<strong>on</strong>g>tance<br />

coefficient ζ, the corresp<strong>on</strong>ding pressure<br />

loss <str<strong>on</strong>g>is</str<strong>on</strong>g>:<br />

∆p = ζ x ½ ρ v 2 x<br />

<strong>MAN</strong> B&W MC/MC�C, ME/ME�C/ME�GI/ME-B engines 198 40 94�9.3<br />

<strong>MAN</strong> <strong>Diesel</strong><br />

___<br />

9.8<br />

in mm WC<br />

where the expressi<strong>on</strong> after ζ <str<strong>on</strong>g>is</str<strong>on</strong>g> the dynamic pressure<br />

of the flow in the pipe.<br />

The fricti<strong>on</strong> losses in the straight pipes may, as a<br />

guidance, be estimated as :<br />

mm WC per diameter length<br />

whereas the positive influence of the up�draught<br />

in the vertical pipe <str<strong>on</strong>g>is</str<strong>on</strong>g> normally negligible.<br />

Pressure losses across comp<strong>on</strong>ents (∆p)<br />

The pressure loss ∆p across silencer, exhaust<br />

gas boiler, spark arrester, rain water trap, etc., to<br />

be measured/ stated as shown in Fig. 5.05.0 (at<br />

specified MCR) <str<strong>on</strong>g>is</str<strong>on</strong>g> normally given by the relevant<br />

manufacturer.<br />

Total back�pressure (∆p M )<br />

The total back�pressure, measured/stated as the static<br />

pressure in the pipe after the turbocharger, <str<strong>on</strong>g>is</str<strong>on</strong>g> then:<br />

∆p M = Σ ∆p<br />

where ∆p incorporates all pipe elements and<br />

comp<strong>on</strong>ents etc. as described:<br />

∆p M has to be lower than 350 mm WC.<br />

(At design stage it <str<strong>on</strong>g>is</str<strong>on</strong>g> recommended to use max.<br />

300 mm WC in order to have some margin for<br />

fouling).

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