PTC 12.1 Calculations Using PEPSE Beta Testing. by Gene Minner Curtiss Wright Jerry Weber Midwest Generation, EME

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PTC 12.1 Calculations Using PEPSE Beta Testing by Gene Minner Curtiss Wright Jerry Weber Midwest Generation, EME

Edison Mission Energy Coal Fired Capacity 6 sites in Illinois Midwest Generation 1 siteinin Pennsylvania 1 site in West Virginia Wind Capacity 812 WTGs and growing Gas Fired 9 sites in California and Washington

PTC 12.1 Feedwater Heater Acceptance Testing Purpose perform acceptance ce testing on new heaters or test existing heaters Conducted within 10% of design feedwater flow Other parameters have corresponding limits Steady state generation (constant load) Test code equations and methodology corrects design performance conditions to actual test conditions for comparison with actual measured values

Feedwater Heater Zones One to three possible zones Desuperheating applicable to fossil unit HP heaters, cools steam to within 5 50 deg of saturation temp Condensing latent heat of condensation Drain Cooling Subcools drains below saturation temperature for ease of transport to lower pressure heater and for efficiency Can exist separately or as part of a two or three zone heater

Heat Transfer Equations Utilized Resistances U = 1/(r shell film + r shell fouling + r t fouling + r metal + r t film ) Overall heat transfer coefficient Utilized to obtain shell side film resistance Supplied by heater manufacturer for each zone r shell fouling + r t fouling are constants R metal = Tube wall conduction = d o /24K (ln (d o /d i )) R t film = Tube side convection =0.0378((u 0378((u 0.4 /(K 0.6 p 0.8 C 0.4 0.8 0.8 p ))(do/di )(1/V ) = 1/ (0.023 (Re 0.8 )(Pr 0.4 ))

Heat Transfer Equations Applied to Each Zone U = 1/(r shell film + r shell fouling + r t fouling + r metal + r t film ) Uses NTUs with the heat transfer resistances to calculate the performance Heat capacity flow rates C shell side = W s actual Q/(W s design (T 1 T 2 ) c fw side = w fw actual Q/(w fw design (t 2 t 1 ) Heat capacity ratio = R = c fw side /C shell side Number of transfer units = NTU = UA/c fw side

Heat Transfer Equations Zone effectiveness = for DS and DC Zones: E = (1 e (NTU * (R 1) )/(1 Re (NTU * (R 1) ) E = 1 e NTU for condensing zone only Feedwater temperature leaving zone = T fw out = E(T shell side in t fw in ) + t fw in Need to perform calculations for each zone in heater beginning with drain cooling zone and ending in desuperheat zone Iteratively converge to solution that satisfies an energy balance Calculate TTD and DCA

Performance Terminal Temperature Difference TTD = T sat T fw outlet Drain Cooler Approach (if applicable) DCA = T drain out T fw inlet

Design data corrections Pressure Drops Pressure Drops adjustments P shell = P design (W s actual /W s design ) 1.8 Performed in each heater zone Assumed negligible in condensing zone p fw = p design (w fw actual /w fw design ) 1.8

Design Data Corrections Heat Transfer Resistances Heat Transfer Resistances Each Zone r shell film, r metal,r t film, r shell fouling, r t fouling r 06 shell film = r shell film design (W s design /W s actual ) 0.6 r metal adjusted for temperature effect on K r fw film = r fw film design (w fw design /w fw actual ) 0.8 r shell hllfouling and r t fouling are constants

PEPSE Calculations Incorporates all the PTC code methodology and calculations User inputs data from manufacturers design spreadsheet plus resistance data that can be easily calculated PEPSE calculates the off design predictions and compares to actual performance

Heater Specification Sheet Data

Resistance data PEPSE Inputs Available from manufacturer or can be calculated R metal = d o /24K (ln (d o /d i )) R Feedwater film = 0.0378((u0378((u 04 0.4 /(K 06 0.6 p 08 0.8 C 04 0.4 08 08 p ))(do/di 0.8 )(1/V 0.8 ) U = 1/(r shell film + r shell fouling + r t fouling + r metal + r t film ) utilized to obtain shell side film resistance

PEPSE inputs for Design Data

PEPSE Inputs for Test Data

PEPSE Outputs

Comparisons to Design Actual to Corrected Design Calculated zone heat transfercoefficients TTD DCA (if applicable) Zone shell pressure drops Feedwater pressure drop

Future Enhancement Ideas From Beta Test on 3 Zone Heater Incorporate resistance calculations Revise the input sheet to designate as optional parameters that can be calculated: Shell side temp leaving condensing zone DS zone pressure drop DC zone pressure drop Condensing zone pressure Note that these are zone dependent and data will be needed for single zone heater

Reference ASME PTC 12.1 1 2000 version