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21st Aachen Colloquium Automobile and Engine Technology 2012 11 The system consists of two evaporators in a parallel layout. The system is controlled with a fluid pump, cf. to Fig. 10, which conveys the working fluid via a distributor valve to both evaporators. After the fluid has passed through both evaporators the superheated vapour is released via the turbine. The mechanical energy received from the turbine is dissipated by a turbocharger compressor. The measurement of the resulting power is based on mass flow, pressure and temperature. Downstream the turbine the vapour is re-liquefied in the condenser. At the test bench two electrical hot gas generators replace the exhaust gas tail pipe. One hot gas generator can provide mass flows of up to 900 kg/h at temperatures up to 550 °C. The second gas generator can provide mass flows of up to 1800 kg/h at temperatures up to 400 °C. Thus the flexible emulation of stationary operating points of a commercial vehicle engine is possible. The evaporators are prototypes developed especially for a Rankine process with water as a working fluid. A photo of the test bench is given in Fig. 11. Fig. 11: Photo of the test bench for the turbine Another advantage of this hot gas generator is the adjustability and reproducibility of steam parameters and test conditions. Furthermore the test bench allows low temperatures of the condenser, enabling operation below atmospheric pressure. This allows a high pressure difference with a highly efficient process. 5.5 Experimental Results With the prototype of the turbine, cf. to chapter 5.1, a performance measurement was conducted at the engine operating points B25 to B75, cf. Fig. 12.PDF Image | Waste Heat Recovery for Commercial Vehicles with a Rankine Process
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