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15 temperature heat source through a heat transfer ?uid and said second vaporiZer produces heat-depleted heat transfer ?uid alongWithsaidhighpressureWorking?uidvapor. 22. The Waste heat recovery system according to claim 21 Wherein said heat transfer ?uid is selected from the group consistingofexhaustgases,athermaloil,andasyntheticheat transfer?uid. 23. The Waste heat recovery system according to claim 21 5 16 a second condenser receiving said expanded loW pressure Working?uidvaporandproducingsecondcondensate; a second vaporiZer receiving said second condensate and con?gured to receive heat from a loW-temperature heat source, thereby producing said loW pressure Working ?uid vapor; and a generator connected to said high pressure vapor turbine and said loW pressure vapor turbine for producing poWer. 26. The Waste heat recovery system according to claim 25 Wherein said second vaporiZer receives heat from said loW temperature heat source through a ?rst further Working ?uid andsaidsecondvaporiZerproducesheat-depleted?rstfurther Working ?uid along With said loW pressure Working ?uid vapor. 27. The Waste heat recovery system according to claim 26 Wherein said ?rst further Working ?uid is cooling Water. 28. The Waste heat recovery system according to claim 25 Wherein said ?rst vaporiZer receives heat from said high temperatureheatsourcethroughaheattransfer?uidandsaid ?rst vaporizer produces heat-depleted heat transfer ?uid alongWithsaidhighpressureWorking?uidvapor. 29. The Waste heat recovery system according to claim 28 Wherein said heat transfer ?uid is selected from the group consistingofexhaustgases,athermaloil,andasyntheticheat transfer?uid. 30. The Waste heat recovery system according to claim 28 furthercomprisingapreheaterreceivingsaidheatedconden sateandsaidheat-depletedheattransfer?uidandproducing furtherheat-depletedheattransfer?uidandfurtherheated condensate, said further heated condensate supplied to said ?rstvaporizer. 31. The Waste heat recovery system according to claim 25 Wherein said Working ?uid is selected from the group con sistingofWater,alcohol,butane,iso-butane,n-pentane,iso pentane,hexane,iso-hexane,andmixturesthereof. ***** furthercomprisingapreheaterreceivingsaidheatedconden sateandsaidheat-depletedheattransfer?uidandproducing 10 further heat-depleted heat transfer ?uid and further heated condensate, said further heated condensate supplied to said secondvaporiZer. 24. The Waste heat recovery system according to claim 18 Wherein said Working ?uid is selected from the group con sistingofWater,alcohol,butane,iso-butane,n-pentane,iso pentane,hexane,iso-hexane,andmixturesthereof. 25.A WasteheatrecoverysystemutiliZingaWorking?uid comprising: ahighpressurevaporturbinereceivinghighpressure20 Working?uidvaporandproducingpoWerandexpanded highpressureWorking?uidvapor; arecuperatorreceivingsaidexpandedhighpressureWork ing?uidvaporandproducingheat-depletedexpanded highpressureWorking?uidvapor; 25 a ?rst condenser receiving said heat-depleted expanded high pressure Working ?uid vapor and producing ?rst condensate, said ?rst condensate recycled to said recu perator to produce heated condensate and said heat depletedexpandedhighpressureWorking?uidvapor; 30 a ?rst vaporiZer receiving said heated condensate and con ?gured to receive heat from a high-temperature heat source, thereby producing said high pressure Working ?uidvapor; aloWpressurevaporturbinereceivingloWpressureWork 35 ing?uidvaporandproducingpoWerandexpandedloW pressure Working ?uid vapor; US 8,438,849B2PDF Image | MULTI-LEVEL ORGANIC RANKINE CYCLE POWER SYSTEM
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