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Title: Use of a fluidized bed heat exchanger to improve the performance of a heat pump. Final report

Technical Report ·
OSTI ID:5529945

The outdoor evaporator heat exchanger of a York 60,000 Btu heat pump in the heating mode was replaced with a fluidized bed heat exchanger. Air temperature control was achieved by recirculating the conditioned air from both the evaporator and condenser heat exchangers through a chambered plenum. Candidate particles and distributor plates for the design of the bed were tested separately. A particle size of 245 microns (glass spheres) at a static bed depth of 1-1/2 in. and a fluidizing air flow of 2.3 fps gave a heat transfer coefficient of 550 W/m/sup 2/-/sup 0/C and the best heat transfer to pressure drop ratio. The overall design heat transfer coefficient was 43 Btu/h-ft/sup 2/-/sup 0/F, which is about 5 times that of the conventional heat pump heat transfer coefficient. The heat exchanger consisted of two 4 ft by 5 ft shallow beds with a static bed 1-1/2 in. high. Particles used were sand, predominantly 300 microns in dia. A distributor plate consisting of a wire mesh screen supported by coarsely perforated plywood was used to support the large bed area (20 ft/sup 2/). Even air flow distribution through the bed was achieved with a stilling chamber beneath the distributor. Design heat duty for the bed was about 33% greater than that of the existing evaporator. Refrigerant was carried by 320 ft of 3/8 in.-dia. copper tubing with 3/4 in. dia copper fins spaced at ten per in. Total heat transfer area was 1/3 that of the existing evaporator. Test results showed: excessive superheat attributed to the high heat transfer efficiency of the fluidized bed; refrigerant entering the compressor at too high a temperature and pressure; and steady state operation of the system was not achieved. Nevertheless, data obtained in slow-transient tests showed a substantial improvement in heat transfer. The modified heat pump, with fluidized bed evaporator, gave an increase of approx. 40% in the COP (exclusive of blower losses). Ice prevention and removal from the tube was accomplished.

Research Organization:
Lehigh Univ., Bethlehem, PA (USA). Inst. of Thermo-Fluid Engineering and Science
DOE Contract Number:
AS02-77ET11297
OSTI ID:
5529945
Report Number(s):
DOE/ET/11297-T1; COO-4490-10; ON: DE82007841
Country of Publication:
United States
Language:
English