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Operation and Analysis of a Supercritical CO2 Brayton Cycle

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Operation and Analysis of a Supercritical CO2 Brayton Cycle ( operation-and-analysis-supercritical-co2-brayton-cycle )

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T100 P100 = 0 % Turbiine Ball Bearing Coriolis Flow Meter = 95 % Motor Alternator = 66 % Compressor 50.2 kW T301 P301 Waste Heat Gas Chiller 50.2 kW Laby Seal T400 P400 1 T = 305 K P = 7690 kPa THtrShell-1 THtrCore-2 0 kW THtrCore-1 THtrShell-1 Rotor Cavity T = 322.8 K P = 13842 kPa 2 CO2 3.51 kg/s T300 P300 2m Manual Valve T500 P500 T300 P300 P401 T = 305.7 K P = 7705 kPa PDrain 52.8 kW TDrain1 TDrain2 Recirc Valve Haskel Gas Booster Leakage Flow (~0.15 kg/s) Coriolis Flow Meter Figure 2-6: Simple diagram of the heated un-recuperated supercritical CO2 Brayton loop. Im I mm C d dT me CO Li F l Fi 2 2x O2 i i l ll V r V er x 1 a a rs 13 2L T lP 3 Pu l lv 0 0 k i ve k q q um e( W W( u u mp p H r rI (N (W i Wa a Is No t so ot tl lo t S o o w w ) l l ) a at Sh ti ho r io s s o ow n n F w n n ) ) Figure 2-7: Engineering drawing of the heated but un-recuperated Brayton loop. C s sT C Fl o o lo r r ow i io o wM l li i T Me e 19 t te e r u ur r b bo u u He 5 r 50 o b - - A be ea 0k a kW W ( Al e& t t E l t t & S E (n no e e x x om r rn na Sh c ch mi at he ha in n to el an a a l l ) ) o ll n r r g ge - - C Co er om mp pr re es (N s No s so o o el t tS l r H r H e ea a t t e e R R P y Pu ( s (H o o ur H t to or rg a as ge s rC e P k ke Ca P a v u vi um it ty mp ps si io on n H He e a at te er L Le F s Fl ea o l o ak r r ow k i io w M a a o l g g li i M e Sh e C e C o s e ho o t t e e w r ( r wn n)

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