Versatile pinch point avoidance recuperator for supercritical carbon dioxide power generation systems
View Patent ↗A supercritical carbon dioxide power generation Brayton cycle system and method that employs an alternate heat recuperation method and apparatus that utilizes switched banks of bead filled tanks to accumulate and recover the thermal energy of the two streams of working fluid in such a way that the variable thermal properties of the supercritical carbon dioxide can be accommodated without significant loss of thermal efficiency.
1. A supercritical carbon dioxide power generation Brayton cycle system comprising:
a heat source for heating a working fluid;
a turbine in fluid communication with the working fluid exiting the heat source and having an inlet for the working fluid exiting the heat source and an outlet for the working fluid exiting the turbine;
a compressor in fluid communication with the outlet of the turbine having an inlet for the working fluid exiting the turbine and an outlet in fluid communication with the heat source for communicating the working fluid back to the heat source;
a versatile pinch point avoidance recuperator comprising a plurality of tanks each housing beads constructed of a solid filler material that absorbs, retains and transmits heat, with the plurality of tanks connected in parallel between the compressor and the turbine with a valving arrangement that connects an inlet of a first group of tanks, the first group of tanks comprising at least one tank of the plurality of tanks, to the outlet of the turbine and an outlet of the first group of tanks to the inlet of the compressor and connects an outlet of a second group of tanks, the second group of tanks comprising at least one other tank of the plurality of tanks, to an inlet of the heat source and an inlet of the second group of tanks to the outlet of the compressor so that a first flow through the first group of tanks is in counter-flow relationship with a second flow through the second group of tanks with the valving arrangement operable to alternately reverse the first flow and the second flow while maintaining the counter-flow relationship between the first group of tanks and the second group of tanks; and
a heat sink in fluid communication with the first group of tanks or the second group of tanks such that the working fluid passes through the heat sink before entering the compressor.
2. The supercritical carbon dioxide power generation Brayton cycle system of claim 1 wherein the solid filler material comprises sand.
3. The supercritical carbon dioxide power generation Brayton cycle system of claim 1 wherein the solid filler material comprises a ceramic.
4. The supercritical carbon dioxide power generation Brayton cycle system of claim 1 wherein the compressor compresses the working fluid to a pressure equal to or greater than 72.9 atm or 7.39 MPa.
5. The supercritical carbon dioxide power generation Brayton cycle system of claim 1 wherein the heat source heats the working fluid to a temperature equal to or greater than 304.25 K.
6. The supercritical carbon dioxide power generation Brayton cycle system of claim 1 wherein the heat sink reduces the temperature of the working fluid entering the compressor.
7. A method of employing supercritical carbon dioxide as a working fluid in a power generation Brayton cycle system comprising: a heat source for heating a working fluid; a turbine in fluid communication with the working fluid exiting the heat source and having an inlet for the working fluid exiting the heat source and an outlet for the working fluid exiting the turbine; a compressor in fluid communication with the outlet of the turbine having an inlet for the working fluid exiting the turbine and an outlet in fluid communication with the heat source for communicating the working fluid back to the heat source; a versatile pinch point avoidance recuperator comprising a plurality of tanks each housing beads constructed of a solid filler material that absorbs, retains and transmits heat, with the plurality of tanks connected in parallel between the compressor and the turbine with a valving arrangement that connects an inlet of a first group of tanks, the first group of tanks comprising at least one tank of the plurality of tanks, to the outlet of the turbine and an outlet of the first group of tanks to the inlet of the compressor and connects an outlet of a second group of tanks, the second group of tanks comprising at least one other tank of the plurality of tanks, to an inlet of the heat source and an inlet of the second group of tanks to the outlet of the compressor so that a first flow through the first group of tanks is in counter-flow relationship with a second flow through the second group of tanks with the valving arrangement operable to alternately reverse the first flow and the second flow while maintaining the counter-flow relationship between the first group of tanks and the second group of tanks; and a heat sink in fluid communication with the first group of tanks or the second group of tanks such that the working fluid is cooled in the heat sink before the working fluid enters the inlet of the compressor;
the method comprising:
heating the working fluid with the heat source;
passing the working fluid through the inlet of the turbine;
expanding the working fluid through the turbine;
conveying the working fluid exiting the outlet of the turbine to the inlet of the first group of tanks of the versatile pinch point avoidance recuperator;
routing the working fluid exiting the outlet of the first group of tanks of the versatile pinch point avoidance recuperator through the heat sink to the inlet of the compressor;
compressing the working fluid in the compressor;
directing the working fluid exiting the outlet of the compressor to the inlet of the second group of tanks of the versatile pinch point avoidance recuperator; and
returning the working fluid exiting the outlet of the second group of tanks of the versatile pinch point avoidance recuperator to the heat source.
8. The method of claim 7 including the step of reconfiguring the valving arrangement after a preselected period of time, wherein the counter-flow relationship of the first flow through the first group of tanks and the second flow through the second group of tanks is reversed after the preselected period of time.
9. The method of claim 8 wherein the preselected period of time is before the solid filler material of the plurality of tanks reaches thermal equilibrium with the working fluid passing through the plurality of tanks.