Boundary vapor contentsin an annular channel
Description
The work is aimed at the experimental investigation of the worsening of the heat transfer in an annular channel. The experiments have been carried out on the annular channel 32x28x3000 mm with the even distribution of the heat flux along the length at pressures of 6.9-19.6 MPa, flow rate of 350-1000 kg/m2s, and specific heat fluxes from 0.18 up to 0.6 MW/m2. Heating is external, oneside. Water monodistillate of the following composition has been used as a coolant: pH 9; dry residue - 0.8-1.2 mg/kg, oxygen -10-15 mg/kg. It is found out that the change character of the temperature field of the heating surface of the annular channel at the regime with the worsen of heat emission depends on the ratio of regime parameters. At pressures of 6.9-13.7 MPa and flow rate of 350-500 kg/m2s the channel wall temperature rises monotoneously, never reaching its maximum. With pressure rise > 13.7 MPa and mass velocity > 500 kg/m2s the temperature of the heat emitting surface reaches its maximum, and then slowly falls. At pressures of 6.9-11.8 MPa the boundary vapor content value within the whole range of mass velocities does not depend on the specific heat flux q. At pressures higher than 13.7 MPa and mass velocities of 350-1000 kg/m2s the boundary vapor content depends on q. The heating of the external or internal surface of the annular channel affects the value of the boundary vapor content within the whole range of regime parameters' change under investigation
Availability note (English)
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Additional details
Additional titles
- Original title (Russian)
- Граничные паросодержания в кольцевом канале
Publishing Information
- Imprint Pagination
- 15 p.
- Report number
- FEI--878
INIS
- Country of Publication
- USSR
- Country of Input or Organization
- USSR
- INIS RN
- 10494692
- Subject category
- S42: ENGINEERING;
- Descriptors DEI
- ANNULAR SPACE; BURNOUT; FLOW RATE; HEAT FLUX; HIGH TEMPERATURE; MEDIUM PRESSURE; TWO-PHASE FLOW; VOID FRACTION
- Descriptors DEC
- CONFIGURATION; FLUID FLOW
Optional Information
- Notes
- 6 refs.; 4 figs.; 1 table.