CHEN Bo, NI Mingjiang, YING Zhenzhen, et al. Numerical study on heat exchanger of supercritical CO2 Brayton cycle fluidized bed boiler based on solar particle-receiver[J]. Thermal power generation, 2019, 48(7): 70-76.
DOI:
CHEN Bo, NI Mingjiang, YING Zhenzhen, et al. Numerical study on heat exchanger of supercritical CO2 Brayton cycle fluidized bed boiler based on solar particle-receiver[J]. Thermal power generation, 2019, 48(7): 70-76. DOI: 10.19666/j.rlfd.201901002.
Numerical study on heat exchanger of supercritical CO2 Brayton cycle fluidized bed boiler based on solar particle-receiver
the supercritical CO_2 Brayton cycle system based on solar particle-receiver has great development potential. By applying a more accurate particle-side heat transfer model
the supercritical CO_2 fluidized bed heat exchanger model is established. On the basis of the operating parameters of the heat exchanger with 100 kW heat transfer power
the external diameter
tube bundle number
particle size and fluidized gas temperature of the heat transfer pipes are optimized. The results show that
under the condition that the flow pressure loss of CO_2 is 0.01 MPa
the optimized tube bundle parameters of the heat exchanger are as follows: the outer diameter of the tube is 10 mm
the thickness of the tube is 2.9 mm
the number of the tubes is 97. When the small particle size particles are selected
the critical fluidization velocity is low
the flow rate is small
so the heat loss of the gas can be effectively reduced
the heat efficiency of the heat exchanger can be improved
and the energy consumption of the fan can be decreased. With the optimized tube bundle parameters
when the particle size increases from 100 μm to 500 μm
the heat loss increases from 70.32 W to 1 176.00 W
the thermal efficiency declines from 99.93% to 98.84%
the fan power consumption increases from 21.60 W to 405.97 W
the inlet temperature of the fluidized gas rises from 570 ℃to 630 ℃
and the thermal efficiency of the heat exchanger increases from 98.52% to 99.64%.