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US 2012/0186219A1 Jul.26,2012 pressureportionWithinthesupercriticalcarbondioxidether modynamic poWer generating cycle, and Wherein the ?rst carbon dioxide source is operable to decouple the high-side pressureportionfromtheloW-sidepressureportion. 8. The energy production system according to claim 7 Whereinthehigh-sidepressureportionisfurthercomprisedof a high pressure storage tank, and the loW-side pressure por tion is further comprised of a loW pressure storage tank. 9. The energy production system according to claim 8 further comprised of at least one carbon dioxide Venting to at least one of the loW pressure storage tank and ambient envi ronment. 10. The energy production system according to claim 8 Wherein the high pressure storage tank and the loW pressure storagetankdecouplethehigh-sidepressureportionfromthe loW-side pressure portion Whereby transients on either the high-side pressure portion or the loW-side pressure portion areasynchronous. 11. The energy production system according to claim 10 Wherein the transients are asynchronous by at least 0.1 sec onds. 12. The energy production system according to claim 10 Wherein the transients are asynchronous by at least 0.5 sec onds. 13. The energy production system according to claim 10 Whereinthetransientsareasynchronousbyatleast5seconds. 14. The energy production system according to claim 10 Wherein the transients are asynchronous by at least 20 sec onds. 15. The energy production system according to claim 1 is further comprised of a top cycle poWer generating Brayton cycle having a combustor that concurrently produces Waste heatandcombustionexhaust,andWhereinaslipstreamfrom the combustion exhaust is the ?rst carbon dioxide source to the supercritical carbon dioxide thermodynamic poWer gen eratingcycle. 16. The energy production system according to claim 1 Wherein the supercritical carbon dioxide thermodynamic poWergeneratingcyclehasahigh-sidepressureandloW-side pressureportionWithinthesupercriticalcarbondioxidether modynamic poWer generating cycle, and Wherein the ?rst carbondioxidesourceisoperabletodecouplethemass ?oW rateofthehigh-sidepressureportionfromthemass ?oW rate oftheloW-sidepressureportion. 17. The energy production system according to claim 16 Whereinthemass ?oW rateofthehigh-sidepressureportion has a Variance from the mass ?oW rate ofthe loW-side pres sure portion by at least 0.5 percent. 18. The energy production system according to claim 16 Whereinthemass ?oW rateofthehigh-sidepressureportion has a Variance from the mass ?oW rate ofthe loW-side pres sure portion by at least 1.0 percent. 19. The energy production system according to claim 16 Whereinthemass ?oW rateofthehigh-sidepressureportion has a Variance from the mass ?oW rate ofthe loW-side pres sure portion by at least 0.2 percent. 20. The energy production system according to claim 15 Wherein the supercritical carbon dioxide thermodynamic poWergeneratingcyclehasahigh-sidepressureandloW-side pressureportionWithinthesupercriticalcarbondioxidether modynamic poWer generating cycle, Wherein the supercriti calcarbondioxidethermodynamicpoWergeneratingcycleis further comprised of a Venting Valve from at least one of the high-sidepressureandloW-sidepressureportion,Whereinthe top cycle poWer generating Brayton cycle has combustion exhaust containing carbon dioxide and a carbon dioxide sequestrationsystemoperabletocaptureatleast1.0percent ofthetopcyclepoWergeneratingBraytoncyclecombustion exhaustWherebythecarbondioxideVentedfromtheVenting Valve of the supercritical carbon dioxide thermodynamic poWer generating cycle is upstream of the carbon dioxide sequestrationsystem. 21.A methodforoperatinganenergyproductionsystem according to claim 16 having a control system operable to regulatethemass ?oW rateoftheloW-sidepressureportion independentlyofthemass ?oW rateofthehigh-sidepressure portion.PDF Image | HYBRID SUPERCRITICAL POWER CYCLE
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