HEAT TRANSFER CALCULATION FOR EVAPORATIVE HEATING SURFACE IN SUPERCRITICAL ONCE-THROUGH BOILER SUITABLE FOR PREDICTION OF ENTHALPY VALUE AT INTERMEDIATE POINT
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HEAT TRANSFER CALCULATION FOR EVAPORATIVE HEATING SURFACE IN SUPERCRITICAL ONCE-THROUGH BOILER SUITABLE FOR PREDICTION OF ENTHALPY VALUE AT INTERMEDIATE POINT
Thermal Power GenerationVol. 38, Issue 11, Pages: 47-52(2009)
作者机构:
山东电力研究院
作者简介:
基金信息:
DOI:
CLC:TK229.2
Published:2009
稿件说明:
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LIU Fu-guo, HAN Xiao-gang, HOU Fan-jun, et al. HEAT TRANSFER CALCULATION FOR EVAPORATIVE HEATING SURFACE IN SUPERCRITICAL ONCE-THROUGH BOILER SUITABLE FOR PREDICTION OF ENTHALPY VALUE AT INTERMEDIATE POINT[J]. Thermal power generation, 2009, 38(11): 47-52.
DOI:
LIU Fu-guo, HAN Xiao-gang, HOU Fan-jun, et al. HEAT TRANSFER CALCULATION FOR EVAPORATIVE HEATING SURFACE IN SUPERCRITICAL ONCE-THROUGH BOILER SUITABLE FOR PREDICTION OF ENTHALPY VALUE AT INTERMEDIATE POINT[J]. Thermal power generation, 2009, 38(11): 47-52.DOI:
HEAT TRANSFER CALCULATION FOR EVAPORATIVE HEATING SURFACE IN SUPERCRITICAL ONCE-THROUGH BOILER SUITABLE FOR PREDICTION OF ENTHALPY VALUE AT INTERMEDIATE POINT
The heat transfer modelling method based on actual status of the evaporative heating surface for supercritical once-through boiler has been given.On the basis of operation characters concerning the heating surface
the structure of said heating surface and its parameters under polluted status have been determined
the absorbed heat of said heating surface being predicted by adopting the obtained parameters and the heat transfer calculation model of said evaporative heating surface suitable for prediction of enthalpy value at the intermediate point being further given.This model can clearly describe quantitative relationship between the enthalpy value at intermediate point and every affecting factor.Through test of varying the coal sort
the proportioning ratio of water and coal
the load
and the coefficient of excess air of the once-through boiler for supercritical 600 MW unit
it is shown that the said model can accurately predict the enthalpy value at intermediate point;in the event of variation in operation condition of the boiler
the said model can be used to correct the thermodynamic adjusting parameters