Page 309 - Failure Analysis Case Studies II
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               7.  CASE  STUDY  2-HOLES   IN  ALUMINIUM  HEAT-EXCHANGER  TUBES
           7.1.  Background
            Figure 11 is a simplified drawing of a heat exchanger from a large gas-fired central heating boiler.
           It consists of  a number  of  externally finned aluminium tubes arranged concentrically around  a
           tubular gas burner. The tubes are enclosed by a perforated sleeve of stainless steel; this is meant to
           spread the hot gases out uniformly as they flow away from the burner.  Figure  12 shows a cross-
           section through one of the heat-exchanger tubes. The ends of the tubes are expanded into headers
           cast from eutectic aluminium-silicon  alloy LM6. The cover plate on the return header is also cast
           in LM6. The cover plate on the inlet/outlet header is cast in grey cast iron, and so too are the pair
           of curved elbows. The boiler contains between two and six of these units depending on the heat
           output required. Technical data for a single heat exchanger are as follows.
            Maximum heat output  = 100 kW.
            Heat flux at bore of tubex230 kW m-*.
            Flow rates2 Imin-'.
            Flow velocity inside tubes0.5m s-',
            Maximum temperature at return elbow = 80 "C.

                                                  Cast-iron
                                    Aluminium    cover plate
                                   , alloy           \        t
                                 / cover plate        \l=zewj














                                         headers
                                                            Return







                                Gas  /
                              distribution
                               screen                     tube
                             Fig. 11.  Simplified drawing of the heat exchanger. Not to scale







                                                  2
                          I_                                        7
                                               400
                     Fig. 12.  Cross-section through the heat-exchanger tube. Dimensions in mrn. Not to scale.
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