DETERMINATION OF SURFACE ASH AND INTERNAL PIPE DEPOSIT HEAT-TRANSFER RESISTANCE IN STEAM GENERATOR HEAT TRANSFER CALCULATION

1978 ◽  
Author(s):  
V.V. Meetor ◽  
R.E. Krzyzhanovski ◽  
I.I. Tchoodnovskaya ◽  
I.S. Pavlof ◽  
I.N. Konopelko ◽  
...  
Keyword(s):  
Heat Transfer ◽  
Steam Generator ◽  
Transfer Resistance ◽  
Heat Transfer Calculation

INFLUENCE OF HEAT TREATMENT OF MOUNTAIN MASSIVE ON TEMPERATURE MODE OF GEOTHERMAL CIRCULATION SYSTEM

2018 ◽  
pp. 44-50
Author(s):  
Yu. P. Morozov
Keyword(s):  
Heat Transfer ◽  
Operating Time ◽  
Fluid Motion ◽  
Coolant Temperature ◽  
Circulation System ◽  
Thermal Processes ◽  
Temperature Mode ◽  
Heat Influx ◽  
Stationary Heat Transfer

Based on the solution of the problem of non-stationary heat transfer during fluid motion in underground permeable layers, dependence was obtained to determine the operating time of the geothermal circulation system in the regime of constant and falling temperatures. It has been established that for a thickness of the layer H <4 m, the influence of heat influxes at = 0.99 and = 0.5 is practically the same, but for a thickness of the layer H> 5 m, the influence of heat inflows depends significantly on temperature. At a thickness of the permeable formation H> 20 m, the heat transfer at = 0.99 has virtually no effect on the thermal processes in the permeable formation, but at = 0.5 the heat influx, depending on the speed of movement, can be from 50 to 90%. Only at H> 50 m, the effect of heat influx significantly decreases and amounts, depending on the filtration rate, from 50 to 10%. The thermal effect of the rock mass with its thickness of more than 10 m, the distance between the discharge circuit and operation, as well as the speed of the coolant have almost no effect on the determination of the operating time of the GCS in constant temperature mode. During operation of the GCS at a dimensionless coolant temperature = 0.5, the velocity of the coolant is significant. With an increase in the speed of the coolant in two times, the error changes by 1.5 times.

APPLICATION OF ADSORPTION METHOD FOR DETERMINATION OF LOCAL CONVECTIVE HEAT TRANSFER RATES

1974 ◽  
Author(s):  
S. Koncar-Djurdjevic ◽  
M. Mitrovic ◽  
S. Cvijovic ◽  
G. Popovic ◽  
Dimitrije Voronjec
Keyword(s):  
Heat Transfer ◽  
Convective Heat Transfer ◽  
Convective Heat ◽  
Adsorption Method ◽  
Transfer Rates

Heat transfer calculation of blunt bodies in nonequilibrium air flow

1997 ◽  
Author(s):  
N. Hamamoto ◽  
M. Lee ◽  
Y. Nakamura ◽  
I. Menshov ◽  
N. Hamamoto ◽  
...  
Keyword(s):  
Heat Transfer ◽  
Air Flow ◽  
Blunt Bodies ◽  
Heat Transfer Calculation
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