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study of ORC with the expansion process twin screw machines

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study of ORC with the expansion process twin screw machines ( study-orc-with-expansion-process-twin-screw-machines )

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Nevertheless, it is still desirable to know the approximate physical sizes of the heat exchangers relative to one another. In order to account for this, the relative full load heat transfer coefficients were estimated. The overall heat transfer coefficient in each case can be calculated assuming counter-flow. Knowing the design value UA and estimating U the off- design condition can be calculated. Overall heat transfer coefficient waste heat source k  0.00067KW / m2K WHS @80C Working fluid k  0.0000705KW / m2K WF @80C p WF ReWHS  1170  0.469 1  31, 213, 310  V L ReWHS WHS WHS p  V L ReWF WF WF WHS ReWHS  9711.3111  3, 592, 946 0.00001758 0.0003543 A (0.074Re 0.8)(1.328Re 0.5) A (0.074Re 0.8)(1.328Re 0.5) WHS WHS WHS WF WF WF A 10,472 WHS A 65,813 WF Pr  4.4288 WF @80C Nu 0.037(Re0.8A/2)Pr0.333 WF NuWF 58103 H  kWF NuWF 4.096KW /m2K 1  2.22KW / m2 K (1/ 4.096)  (0.01/ 0.4)  (1/ 5.5)  2.2196 Nu 0.037(Re0.8A/2)Pr0.333 NuWHS 8216 H  kWHSNuWHS 5.5KW /m2K Pr WHS @80C WHS WHS L WF L pp UOVERALL  1 (1/ HWHS )  (x / kCOPPER )  (1/ HWF ) U OVERALL  Fouling of the heat transfer surfaces can significantly deteriorate the performance of any heat exchanger. Predicting exact fouling parameters require exact reference data from a heat 61

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