ThermoGen Power Services Inc. powerful experience Reporte de Determinación de Consumo Específico Artículo 21 de la Resolución Exenta 363 - Prueba CEN Rendimiento de Planta Preparado para: Engie Energía Chile Mejillones CTM1, Rev 00 Santiago, Chile 03, Agosto 2016 This document is proprietary to ThermoGen Power Services Inc. (hereafter known as TGPS) and is furnished in confidence solely for use in considering the merits of this project and for no other direct or indirect use. By accepting this document from TGPS, the recipient agrees to use this document, and the information it contains, exclusively for the above stated purpose and to prohibit use of the information for performance of the proposed work by the recipient or disclosure of the information to, and use by, competitors of TGPS on behalf of the recipient, to avoid publication or other unrestricted disclosure of this document or the information it contains, to make no copies of any part thereof without the prior written permission of TGPS, and to return this document when it is no longer needed for the purpose for which furnished upon request of TGPS.
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ThermoGen Power Services Inc. powerful experience
Reporte de Determinación de Consumo Específico Artículo 21 de la Resolución Exenta 363 - Prueba CEN Rendimiento de Planta Preparado para:
Engie Energía Chile Mejillones CTM1, Rev 00
Santiago, Chile 03, Agosto 2016
This document is proprietary to ThermoGen Power Services Inc. (hereafter known as TGPS) and is furnished in confidence solely for use in considering the merits of this project and for no other direct or indirect use. By accepting this document from TGPS, the recipient agrees to use this document, and the information it contains, exclusively for the above stated purpose and to prohibit use of the information for performance of the proposed work by the recipient or disclosure of the information to, and use by, competitors of TGPS on behalf of the recipient, to avoid publication or other unrestricted disclosure of this document or the information it contains, to make no copies of any part thereof without the prior written permission of TGPS, and to return this document when it is no longer needed for the purpose for which furnished upon request of TGPS.
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Registro de revisiones # Revisión Fecha Revisión Emitido
por Revisado por
00 03-08-2016
Primera Versión C.Simental JP Delia
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Tabla de contenidos Registro de revisiones ii Tabla de contenidos 1
1. Resumen Ejecutivo 2
2. Ejecución de la Prueba 3
2.1. Instrumentación y Datos 3 2.1.1 Mediciones de gases de escape .............................................................. 3
2.2. Ejecución de la Prueba 3 2.2.1 Retrasos y Cambios en el programa de Prueba ........................................ 3
2.3. Calculo de los Resultados 3 2.3.1 Calculo de Potencia Neta Corregida (PN*) ............................................... 3
2.3.3 Datos de análisis química de cenizas y de cal .......................................... 4
4. Resultados y Conclusiones 5
Apéndice A – Detalles de Cálculos 6
Apéndice B – Cálculos de Incertidumbre 7
Apéndice C – Resumen de Datos 8
Apéndice D – Representación Gráfica de los Resultados 9
Apéndice E – Actas de Fin de Pruebas 10
Apéndice F – Reportes de Análisis de Combustible y de Cal 11
Apéndice G – Reportes de Análisis de Residuos 12
Apéndice H – Versión Final del Procedimiento 13
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1. Resumen Ejecutivo El propósito de este documento es reportar los resultados de la prueba de Consumo Específico Neto (CEN) para la unidad 1 de la Central Térmica de Mejillones (CTM1) instalada en la planta de ENGIE ENERGÍA CHILE de Mejillones, Chile. Las pruebas se completaron en los días del 05-07-2016 al 06-07-2016. La metodología utilizada esta descrita en el documento “Procedimiento de Determinación de Consumo Específico según el Artículo 21 de la Resolución Exenta 363, Rev. 00” el cual se localiza en el Apéndice H. El grupo de generación CTM1 consiste de una caldera de carbón pulverizado que alimenta a una turbina de vapor con una capacidad declarada de 166 MW. La planta funciona con combustible carbón. Al quemar carbón la planta utiliza inyección de cal para el control de las emisiones de SO2. Durante las pruebas el grupo probado se operó quemando carbón Cerrejón. El grupo se operó a las cargas pre-determinadas durante el tiempo prescrito para estabilización y recolección de datos. Este reporte ilustra los valores calculados y corregidos de Potencia Eléctrica corregida, de Consumo Específico Neto (CEN) corregido y de flujo de combustible específico corregido usando un valor de Poder Calorífico Superior (PCS) de 6000 kcal/kg. La Tabla 1 ilustra los resultados de la prueba:
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2. Ejecución de la Prueba 2.1. Instrumentación y Datos La instrumentación utilizada durante la prueba fue la misma descrita en el procedimiento. Incluye aquí el número de sección del procedimiento que indica la instrumentación.
2.1.1 Mediciones de gases de escape Para la medición de temperatura de gases y de contenido de oxígeno y de monóxido de carbón se instaló instrumentación temporal. En cada ducto de escape, a la entrada y salida de gases del pre-calentador se colocó una matriz de 4 puntos de mediciones de contenido de O2 y CO y a la salida del pre-calentador una matriz de 10 puntos de mediciones de temperatura. Para obtener una medida final se promediaron los puntos de mediciones de temperatura y de emisiones.
2.2. Ejecución de la Prueba La ejecución de la prueba se realizó tal y como se describe en el procedimiento con las siguientes excepciones:
2.2.1 Retrasos y Cambios en el programa de Prueba El día 04 de julio se inciaron las pruebas a 90 MW sin embargo una falla en el equipo de adquisición de datos Fluxim provocó la pérdida de los datos derivando en la repetición de la prueba el día 06-07-2016. Debido a condiciones puntuales de la unidad observadas durante la prueba, se decide que la carga máxima será de 153 MW. El consumo específico neto para cargas mayores podrá ser obtenido del polinomio CEN a partir de los resultados presentado en el siguiente informe.
2.3. Calculo de los Resultados Los resultados de las pruebas fueron computados del modo descrito en el procedimiento con las siguientes excepciones:
2.3.1 Calculo de Potencia Neta Corregida (PN*) La potencia neta corregida se calculó por la siguiente relación: PN∗ PN ∗ Fc ∆GL ∆TL Donde: PN = Potencia Bruta – Potencia de Servicios Auxiliares TL = Ajusto a la potencia medida para perdidas del transformador principal GL = Ajusto a la potencia medida para perdidas del generador a FP de la
prueba Fc = Corrección por Foco frío
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2.3.3 Datos de análisis química de cenizas y de cal Al extraer las cenizas volantes, se encuentra visiblemente impurezas y posiblemente cal. Aunque la inyección de cal sea después de economizador, se acuerda con el laboratorio de hacer el análisis de carbón y cantidad de hidróxido de calcio (cal pura) sobre las muestras tomadas en los filtros de mangas. Removiendo esa cantidad solo quedaran las cenizas, más las impurezas de la cal (otros minerales que no sean hidróxido de calcio). Para saber la cantidad de impurezas en la muestra se tomará el análisis de pureza realizado a la cal que se inyecto durante la prueba.
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4. Resultados y Conclusiones Se llevó a cabo un programa de prueba CEN completo dentro del alcance especificado en el procedimiento “Procedimiento de Determinación de Consumo Específico según el Artículo 21 de la Resolución Exenta 363, Rev. 00” menos las excepciones descritos en la sección 2 del presente reporte. Un resumen de los datos colectados está incluido en el Apéndice C. Cada punto de medición corresponde a un periodo de 1 hora de medición. Los datos fueron recogidos de diferentes fuentes; electrónicamente del control distribuido (DCS) de la unidad, recolectados manualmente, electrónicamente desde el sistema de adquisición de datos de TGPS y de los contadores de facturación de la central. Los resultados de esta prueba ilustran que se alcanzó el objetivo de prueba: cada punto cumplo los requisitos de estabilidad del código de prueba ASME PTC-4.6. Se incluye un detalle de los cálculos es incluido en el Apéndice A, una comparativa entre la medición de O2 de la instrumentación temporal calibrada y la del DCS en el Apéndice C incluyendo también una comparativa del flujo de agua alimentación del instrumento y la del DCS. Se utilizó los valores de los instrumentos temporales en el cálculo del CEN.
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Apéndice A – Detalles de Cálculos
HeatRate
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Condiciones de PruebaTemperatura Ambiente C 16.16 16.69 18.97230769 18.72538462 22.09230769 20.58461538 15.48076923 14.73230769 16.91538462 16.35384615Presion Ambiente mbara 1012.365224 1012.057558 1018.918513 1017.91347 1014.467609 1013.749721 1012.683145 1012.703656 1009.801339 1009.616739Humedad Relativa % 83.98 76.32 47.09923077 48.84307692 38.20692308 41.73384615 66.49769231 73.22846154 74.84846154 77.98615385Temperatura de Agua de Mar C 15.30196668 15.35411303 15.62817759 15.58141944 16.20071614 16.20248644 16.02855258 16.01651981 16.11790967 16.34696344PF promedio durante la prueba 0.998359823 0.996983552 0.99951313 0.999707823 0.999007305 0.998639699 0.99319875 0.995361278 0.99987133 0.999685644
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HeatRate
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
CorreccionesCorreccion a la Efficiencia de la Caldera % 0.99990823 0.999487281 0.99804494 0.998203959 0.995715228 0.997025354 1.000346294 1.001140357 0.999259732 0.999725825Perdidas del Generador al FP de pruebas kW 2177.907747 2188.482126 2796.546792 2801.875118 3160.71718 3188.85481 3458.409081 3455.172149 3470.515802 3458.403289Perdidas del Generador al FP de referencia kW 2619.03079 2626.824397 3369.310979 3376.592385 3802.661506 3834.372569 4125.697371 4133.814801 4177.254512 4161.759639Correccion para las perdidas del Generador ‐ ΔGL kW ‐441.1230435 ‐438.3422711 ‐572.7641873 ‐574.7172669 ‐641.9443256 ‐645.5177591 ‐667.2882904 ‐678.6426522 ‐706.7387103 ‐703.3563507Perdidas del Transformadores al FP de pruebas kW 159.4590851 160.70263 224.902672 225.7556524 286.7117189 291.8856989 346.9685847 345.8702397 351.051537 348.5703406Perdidas del Transformadores al FP de referencia kW 195.9662728 196.8928304 271.297914 272.3586305 341.4030212 347.0976395 406.7289557 406.6984977 415.2066435 412.2657169Correccion para las perdidas del Transformador Principal ‐ ΔTL kW ‐36.50718769 ‐36.19020046 ‐46.39524205 ‐46.60297802 ‐54.69130232 ‐55.21194068 ‐59.76037099 ‐60.82825798 ‐64.15510655 ‐63.69537624Correccion al HR para la temperatura del Foco Frio ‐ FC1 ‐ 0.994165115 0.994264861 0.99549738 0.995432058 0.996922326 0.996960616 0.997063411 0.997057846 0.997248144 0.997538195
EstabilidadPotencia (+‐1%) % 0.314682966 0.55328916 0.75902611 0.592823045 0.51843631 0.371256578 0.548189652 0.568844666 0.327865244 0.285746133Flujo de Agua de alimentacion (+‐3%) % 0.027244144 0.026281538 0.030896741 0.032011805 0.024236991 0.018701448 0.028186687 0.028834042 0.021370549 0.024194207Flujo de combustible (+‐10%) % 0.037598316 0.044172965 0.035572389 0.043429568 0.032391648 0.029459388 0.036687334 0.032907482 0.358090304 0.085469296Temperatura del vapor principal, max‐min (+‐11C) C ‐1.81427 ‐2.74033 ‐6.7291 ‐8.93994 ‐4.51704 ‐3.57203 ‐7.24824 ‐4.56005 ‐3.1635 ‐5.05627Temperatura del agua de alimentacion (+‐11C) C ‐0.61591 ‐0.7856 ‐1.04338 ‐1.22998 ‐0.78 ‐0.59155 ‐0.78 ‐0.93036 ‐0.64499 ‐0.83999Presion del vapor principal(+‐1%) % 0.044759331 0.049839021 0.064959315 0.055889756 0.030646413 0.02731808 0.048825416 0.041544398 0.310472692 0.303008937Perdidas de agua % 1.445027644 1.162363978 1.92109554 1.329121202 1.781835668 2.254693822 2.519620578 2.257119268 1.609373336 1.827838704
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Air‐Gases
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Determination of Wet Gas from Fuel, MqFgF,kg/kJ,5‐12.1MqFgF= kg/kJ 3.2341E‐05 3.23425E‐05 3.26302E‐05 3.26197E‐05 3.21904E‐05 3.21943E‐05 3.20871E‐05 3.21629E‐05 3.18844E‐05 3.1921E‐05
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Air‐Gases
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Determination of Moisture from H2O in Fuel, MqWF,kg/kJ,5‐12.2MqWF= kg/kJ 3.65174E‐06 3.65174E‐06 3.97858E‐06 3.97858E‐06 3.60725E‐06 3.60725E‐06 3.60246E‐06 3.60246E‐06 3.442E‐06 3.442E‐06
Determination of Moisture from Combustion of H2 in Fuel, MqWH2F,kg/kJ,5‐12.3MqWH2F= kg/kJ 1.42229E‐05 1.42229E‐05 1.38804E‐05 1.38804E‐05 1.37992E‐05 1.37992E‐05 1.41455E‐05 1.41455E‐05 1.40228E‐05 1.40228E‐05
Determination of Gas from Sorbent, MqCO2Sb,kg/kJ, 5‐12.4MqCO2Sb= kg/kJ 0 0 0 0 0 0 0 0 0 0
Determination of Water from Sorbent, MqWSb,kg/kJ, 5‐12.5MqWSb= kg/kJ 0 0 0 0 0 0 0 0 0 0
Determination of Moisture in Air, MqWAz,kg/kJ, 5‐12.6MqWaz= kg/kJ 4.14993E‐06 3.86996E‐06 2.45242E‐06 2.50657E‐06 2.5398E‐06 2.49356E‐06 3.00975E‐06 3.59227E‐06 3.92225E‐06 3.96101E‐06
Determination of Total Moisture in Flue Gas, MqWFgz,kg/kJ, 5‐12.8MqWFgz= kg/kJ 2.20246E‐05 2.17446E‐05 2.03114E‐05 2.03656E‐05 1.99463E‐05 1.99E‐05 2.07578E‐05 2.13403E‐05 2.1387E‐05 2.14258E‐05
Determination of Total Wet Flue Gas Weight (Entering and Leaving Pre‐Heater), MqFgEPH and MqFgLPH,kg/kJ, 5‐12.9MqFgEPH= kg/kJ 0.000398641 0.000396465 0.000384044 0.000383745 0.000388117 0.00041294 0.000428583 0.000404802 0.000376346 0.000377899MqFgLPH= kg/kJ 0.000478316 0.000474541 0.000429066 0.000429012 0.000447654 0.00044161 0.000459334 0.000518054 0.000481416 0.000483419
Determination of Total Dry Flue Gas Weight, MqDFgz,kg/kJ, 5‐12.10MqDFgz= kg/kJ 0.000456291 0.000452796 0.000408754 0.000408646 0.000427708 0.00042171 0.000438577 0.000496713 0.000460029 0.000461993
Determination of Moisture in Flue Gas, MqWFgz,%mass, 5‐12.11MqWFgz= %mass 4.826863399 4.802291587 4.969100509 4.983663997 4.663520126 4.718883564 4.732982748 4.296294515 4.649061384 4.637684339
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Air‐Gases
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Determination of Wet Gas from Fuel, MqFgF,kg/kJ,5‐12.1MqFgF= kg/kJ 3.2341E‐05 3.23425E‐05 3.26302E‐05 3.26197E‐05 3.21904E‐05 3.21943E‐05 3.20871E‐05 3.21629E‐05 3.18844E‐05 3.1921E‐05
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Air‐Gases Corr
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Determination of Moisture from H2O in Fuel, MqWF,kg/kJ,5‐12.2MqWF= kg/kJ 3.65174E‐06 3.65174E‐06 3.97858E‐06 3.97858E‐06 3.60725E‐06 3.60725E‐06 3.60246E‐06 3.60246E‐06 3.442E‐06 3.442E‐06
Determination of Moisture from Combustion of H2 in Fuel, MqWH2F,kg/kJ,5‐12.3MqWH2F= kg/kJ 1.42229E‐05 1.42229E‐05 1.38804E‐05 1.38804E‐05 1.37992E‐05 1.37992E‐05 1.41455E‐05 1.41455E‐05 1.40228E‐05 1.40228E‐05
Determination of Gas from Sorbent, MqCO2Sb,kg/kJ, 5‐12.4MqCO2Sb= kg/kJ 0 0 0 0 0 0 0 0 0 0
Determination of Water from Sorbent, MqWSb,kg/kJ, 5‐12.5MqWSb= kg/kJ 0 0 0 0 0 0 0 0 0 0
Determination of Moisture in Air, MqWAz,kg/kJ, 5‐12.6MqWaz= kg/kJ 3.31514E‐06 3.2889E‐06 2.95617E‐06 2.95544E‐06 3.09829E‐06 3.05326E‐06 3.18318E‐06 3.61882E‐06 3.34354E‐06 3.358E‐06
Determination of Total Moisture in Flue Gas, MqWFgz,kg/kJ, 5‐12.8MqWFgz= kg/kJ 2.11898E‐05 2.11635E‐05 2.08152E‐05 2.08144E‐05 2.05047E‐05 2.04597E‐05 2.09312E‐05 2.13668E‐05 2.08083E‐05 2.08228E‐05
Determination of Total Wet Flue Gas Weight (Entering and Leaving Pre‐Heater), MqFgEPH and MqFgLPH,kg/kJ, 5‐12.9MqFgEPH= kg/kJ 0.000397806 0.000395884 0.000384548 0.000384194 0.000388675 0.000413499 0.000428757 0.000404829 0.000375767 0.000377296MqFgLPH= kg/kJ 0.000477481 0.00047396 0.000429569 0.000429461 0.000448213 0.00044217 0.000459508 0.00051808 0.000480837 0.000482816
Determination of Total Dry Flue Gas Weight, MqDFgz,kg/kJ, 5‐12.10MqDFgz= kg/kJ 0.000456291 0.000452796 0.000408754 0.000408646 0.000427708 0.00042171 0.000438577 0.000496713 0.000460029 0.000461993
Determination of Moisture in Flue Gas, MqWFgz,%mass, 5‐12.11MqWFgz= %mass 4.643912156 4.673965877 5.092339437 5.093505592 4.794096362 4.851603415 4.772524506 4.301641029 4.523262584 4.507161604
Page 9 of 19
Air‐Gases Corr
TP01 TP02 TP03 TP04 TP05 TP06 TP07 TP08 TP09 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Determination of Mass of Residue, MFrRs,kg/kgfuel, 5‐10.1MFrRs= kg/kgfuel 0.091398285 0.091398285 0.095244294 0.095244294 0.074153186 0.074153186 0.085398425 0.085398425 0.074260962 0.074260962
Determination of Mass of Residue at Location Z, MqRsz,kg/kJ, 5‐10.2MqRsBA= kg/kJ 2.99807E‐06 2.99807E‐06 3.15933E‐06 3.15933E‐06 2.36731E‐06 2.36731E‐06 2.76981E‐06 2.76981E‐06 2.36652E‐06 2.36652E‐06
Page 11 of 19
Sorbent‐Residue Corr
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
Determination of Mass of Residue, MFrRs,kg/kgfuel, 5‐10.1MFrRs= kg/kgfuel 0.091398285 0.091398285 0.095244294 0.095244294 0.074153186 0.074153186 0.085398425 0.085398425 0.074260962 0.074260962
Determination of Mass of Residue at Location Z, MqRsz,kg/kJ, 5‐10.2MqRsBA= kg/kJ 2.99807E‐06 2.99807E‐06 3.15933E‐06 3.15933E‐06 2.36731E‐06 2.36731E‐06 2.76981E‐06 2.76981E‐06 2.36652E‐06 2.36652E‐06
Page 12 of 19
Boiler Efficiency
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
QpL1, Losses in Dry GasesQpL2, Losses in Combustion of H2 in FuelQpL3, Losses due to Water in FuelQpL4, Losses due Humidity in the AirQpL5, Losses due Unburnt Carbon
QpL7, Losses due Wet Ash Pit
QpB2, Credit due to Moisture in AirQpB3, Credit due to Sulfation of Sorbent
QpB1, Credit due to Dry Air entering the Boiler
QrL9, Losses due Sensible HeatQrL10, Losses due Air Infiltrations in the Pre‐heaterQrL11, Losses due to Formation of NoxQrL12, Losses due to Pulverizer Rejections
Page 13 of 19
Boiler Efficiency
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
QpL6, Losses due Sensible Heat lost in Residue Corr
QpL1, Losses in Dry Gases CorrQpL2, Losses in Combustion of H2 in FuelQpL3, Losses due to Water in FuelQpL4, Losses due Humidity in the AirQpL5, Losses due Unburnt Carbon
QpB1, Credit due to Dry Air entering the BoilerQpB2, Credit due to Moisture in AirQpB3, Credit due to Sulfation of Sorbent
QpL7, Losses due Wet Ash PitQpL8, Losses due Radiation and ConvectionQrL9, Losses due Sensible HeatQrL10, Losses due Air Infiltrations in the Pre‐heaterQrL11, Losses due to Formation of NoxQrL12, Losses due to Pulverizer Rejections
Page 16 of 18
Boiler Efficiency Corr
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
TP1 TP2 TP3 TP4 TP5 TP6 TP7 TP8 TP9 TP10Fecha 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016 06/07/2016 06/07/2016Hora Inicio 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m. 06:15:00 p. m. 07:15:00 p. m. 03:30:00 p. m. 04:30:00 p. m.Hora Termino 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m. 07:15:00 p. m. 08:15:00 p. m. 04:30:00 p. m. 05:30:00 p. m.
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.193745538 ‐0.164985901 0.017421022 0.001021779O2exit Oxygen Concentration at preheater exit % 0.8 0.358775696 0.751510493 0.361451534 0.07269694NOx Nox Concentration at Boiler Exit % of reading 5 29.90065347 0.00035407 3.13415E‐06 0.000112083
Texitgas Exit Gas Temperature C 1.00028369 15.4478853 ‐3.33067E‐14 1.10997E‐27 2.64729E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 15.4478853 0.067264911 0.004527136 1.07973011
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 1.006499818 0.095230738 0.002267223 0.009187169
MSSP Main Steam Static Pressure % of reading 0.252 0.122195142 ‐0.056559061 0.000203145 4.77653E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 0.851233844 0.073497738 0.001350479 0.003914224
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.154487341 ‐0.007496484 0.001404932 1.34122E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 0.704838722 ‐0.076257945 0.001453819 0.002889014
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.177193478 0.018215451 0.000331991 1.04178E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.313850826 ‐0.15619625 0.006099317 0.002403188
FWSP Feedwater Static Pressure % of reading 0.252 0.176931353 ‐0.001771897 1.99378E‐07 9.82849E‐08CondtankL Condensate Tank Level % of reading 3 10.85697784 ‐3.33067E‐14 9.98402E‐27 1.30762E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.669714457 ‐3.33067E‐14 2.49601E‐27 3.09277E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 4.737532391 ‐2.60265E‐08 6.77381E‐14 1.52033E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0Paux Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 1.982827408
Plant Heat Rate Independent Parameters
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #1 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Calculated
Value
Absolute Systematic Uncertainty, BR
1.661201493 1.082596014
Absolute Random Uncertainty, tSR
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.246757617 ‐0.164985901 0.017421022 0.001657428O2exit Oxygen Concentration at preheater exit % 0.8 0.241615089 0.751510493 0.361451534 0.032969944NOx Nox Concentration at Boiler Exit % of reading 5 16.09272202 0.00035407 3.13415E‐06 3.24667E‐05
Texitgas Exit Gas Temperature C 1.00028369 15.31789086 ‐3.33067E‐14 1.10997E‐27 2.60292E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 15.31789086 0.067264911 0.004527136 1.061634643
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 1.46644892 0.095230738 0.002267223 0.019502405
MSSP Main Steam Static Pressure % of reading 0.252 0.136057604 ‐0.056559061 0.000203145 5.92175E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 1.194160725 0.073497738 0.001350479 0.007703242
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.268200917 ‐0.007496484 0.001404932 4.04237E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 0.855102518 ‐0.076257945 0.001453819 0.00425213
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.275049752 0.018215451 0.000331991 2.51017E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.498184887 ‐0.15619625 0.006099317 0.006055114
FWSP Feedwater Static Pressure % of reading 0.252 0.237542825 ‐0.001771897 1.99378E‐07 1.77158E‐07CondtankL Condensate Tank Level % of reading 3 10.85697784 ‐3.33067E‐14 9.98402E‐27 1.30762E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.090428085 ‐3.33067E‐14 2.49601E‐27 1.31904E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 4.310243718 ‐2.60265E‐08 6.77381E‐14 1.25845E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 1.97319191
Plant Heat Rate Independent Parameters
1.661201493 1.064845487
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #2 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #2 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 1.152884899 0 0 0RH Relative Humidity % 3 7.432892939 0 0 0AP Barometric Pressure % 0.252 7.432892939 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.156173955 ‐0.164985901 0.017421022 0.000663913O2exit Oxygen Concentration at preheater exit % 0.8 0.487415006 0.751510493 0.361451534 0.134173852NOx Nox Concentration at Boiler Exit % of reading 5 58.83330753 0.00035407 3.13415E‐06 0.000433936
Texitgas Exit Gas Temperature C 1.00028369 14.22623252 ‐3.33067E‐14 1.10997E‐27 2.24514E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.22623252 0.067264911 0.004527136 0.915707867
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 3.914981332 0.095230738 0.002267223 0.138999644
MSSP Main Steam Static Pressure % of reading 0.252 0.178787657 ‐0.056559061 0.000203145 0.000102254SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 2.700684975 0.073497738 0.001350479 0.039399962
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.418663031 ‐0.007496484 0.001404932 9.85019E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 4.500898929 ‐0.076257945 0.001453819 0.117806353
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.430466197 0.018215451 0.000331991 6.14834E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.596510566 ‐0.15619625 0.006099317 0.008681155
FWSP Feedwater Static Pressure % of reading 0.252 0.301086914 ‐0.001771897 1.99378E‐07 2.84617E‐07CondtankL Condensate Tank Level % of reading 3 17.15902784 ‐3.33067E‐14 9.98402E‐27 3.26624E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.633754026 ‐3.33067E‐14 2.49601E‐27 2.96099E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 5.014411827 ‐2.60265E‐08 6.77381E‐14 1.70323E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 2.028701791
Plant Heat Rate Independent Parameters
1.661201493 1.164491543
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #3 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #3 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 0.991887607 0 0 0RH Relative Humidity % 3 3.117823863 0 0 0AP Barometric Pressure % 0.252 3.117823863 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.170855228 ‐0.164985901 0.017421022 0.000794603O2exit Oxygen Concentration at preheater exit % 0.8 0.295427878 0.751510493 0.361451534 0.049291615NOx Nox Concentration at Boiler Exit % of reading 5 14.47078593 0.00035407 3.13415E‐06 2.62521E‐05
Texitgas Exit Gas Temperature C 1.00028369 14.56121157 ‐3.33067E‐14 1.10997E‐27 2.35211E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.56121157 0.067264911 0.004527136 0.95933914
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 5.04641294 0.095230738 0.002267223 0.230951011
MSSP Main Steam Static Pressure % of reading 0.252 0.153718331 ‐0.056559061 0.000203145 7.55885E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 2.691106323 0.073497738 0.001350479 0.039120974
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.356570854 ‐0.007496484 0.001404932 7.14508E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 4.338034269 ‐0.076257945 0.001453819 0.109434976
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.369576726 0.018215451 0.000331991 4.53199E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.61256454 ‐0.15619625 0.006099317 0.009154717
FWSP Feedwater Static Pressure % of reading 0.252 0.271757677 ‐0.001771897 1.99378E‐07 2.31868E‐07CondtankL Condensate Tank Level % of reading 3 17.15902784 ‐3.33067E‐14 9.98402E‐27 3.26624E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.393987056 ‐3.33067E‐14 2.49601E‐27 2.15566E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 4.564251243 ‐2.60265E‐08 6.77381E‐14 1.41115E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 2.039076255
Plant Heat Rate Independent Parameters
1.661201493 1.182472653
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #4 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #4 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 0.898745565 0 0 0RH Relative Humidity % 3 1.662315345 0 0 0AP Barometric Pressure % 0.252 1.662315345 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.130127911 ‐0.164985901 0.017421022 0.00046093O2exit Oxygen Concentration at preheater exit % 0.8 1.028213889 0.751510493 0.361451534 0.597086194NOx Nox Concentration at Boiler Exit % of reading 5 21.83460411 0.00035407 3.13415E‐06 5.97682E‐05
Texitgas Exit Gas Temperature C 1.00028369 14.45633968 ‐3.33067E‐14 1.10997E‐27 2.31835E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.45633968 0.067264911 0.004527136 0.945570313
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 2.3617469 0.095230738 0.002267223 0.050584913
MSSP Main Steam Static Pressure % of reading 0.252 0.084923173 ‐0.056559061 0.000203145 2.30705E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 1.853420222 0.073497738 0.001350479 0.018556486
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.342002434 ‐0.007496484 0.001404932 6.57315E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 1.750388207 ‐0.076257945 0.001453819 0.017817179
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.364793099 0.018215451 0.000331991 4.41543E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.472512706 ‐0.15619625 0.006099317 0.005447136
FWSP Feedwater Static Pressure % of reading 0.252 0.232775106 ‐0.001771897 1.99378E‐07 1.70118E‐07CondtankL Condensate Tank Level % of reading 3 20.12256444 ‐3.33067E‐14 9.98402E‐27 4.4919E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.117045988 ‐3.33067E‐14 2.49601E‐27 1.38422E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 4.753906996 ‐2.60265E‐08 6.77381E‐14 1.53086E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 2.096484507
Plant Heat Rate Independent Parameters
1.661201493 1.278928023
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #5 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #5 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 1.453744943 0 0 0RH Relative Humidity % 3 5.895854693 0 0 0AP Barometric Pressure % 0.252 5.895854693 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 2.092149575 ‐0.164985901 0.017421022 0.119145907O2exit Oxygen Concentration at preheater exit % 0.8 0.391886235 0.751510493 0.361451534 0.086734148NOx Nox Concentration at Boiler Exit % of reading 5 27.51587613 0.00035407 3.13415E‐06 9.49175E‐05
Texitgas Exit Gas Temperature C 1.00028369 14.2223354 ‐3.33067E‐14 1.10997E‐27 2.24391E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.2223354 0.067264911 0.004527136 0.91520624
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 2.063896101 0.095230738 0.002267223 0.038630467
MSSP Main Steam Static Pressure % of reading 0.252 0.075736148 ‐0.056559061 0.000203145 1.83489E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 1.125388614 0.073497738 0.001350479 0.006841526
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.221320684 ‐0.007496484 0.001404932 2.7527E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 2.16740594 ‐0.076257945 0.001453819 0.027318114
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.225503201 0.018215451 0.000331991 1.68727E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.342397536 ‐0.15619625 0.006099317 0.00286024
FWSP Feedwater Static Pressure % of reading 0.252 0.133646505 ‐0.001771897 1.99378E‐07 5.6078E‐08CondtankL Condensate Tank Level % of reading 3 20.27268524 ‐3.33067E‐14 9.98402E‐27 4.55917E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 2.648390598 ‐3.33067E‐14 2.49601E‐27 7.78085E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 5.773566207 ‐2.60265E‐08 6.77381E‐14 2.25799E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.40295915 ‐0.164985901 0.017421022 0.004419933O2exit Oxygen Concentration at preheater exit % 0.8 0.769600483 0.751510493 0.361451534 0.334503573NOx Nox Concentration at Boiler Exit % of reading 5 29.4243545 0.00035407 3.13415E‐06 0.000108541
Texitgas Exit Gas Temperature C 1.00028369 14.64586765 ‐3.33067E‐14 1.10997E‐27 2.37954E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.64586765 0.067264911 0.004527136 0.970526393
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 3.172718666 0.095230738 0.002267223 0.091288785
MSSP Main Steam Static Pressure % of reading 0.252 0.136153926 ‐0.056559061 0.000203145 5.93014E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 1.71134638 0.073497738 0.001350479 0.015820631
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.35880981 ‐0.007496484 0.001404932 7.23509E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 1.649555567 ‐0.076257945 0.001453819 0.015823556
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.367909752 0.018215451 0.000331991 4.4912E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.413452444 ‐0.15619625 0.006099317 0.00417054
FWSP Feedwater Static Pressure % of reading 0.252 0.270269465 ‐0.001771897 1.99378E‐07 2.29335E‐07CondtankL Condensate Tank Level % of reading 3 27.38504812 ‐3.33067E‐14 9.98402E‐27 8.31936E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.360134072 ‐3.33067E‐14 2.49601E‐27 2.05223E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 4.46517146 ‐2.60265E‐08 6.77381E‐14 1.35054E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 2.048502875
Plant Heat Rate Independent Parameters
1.661201493 1.198654925
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #7 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #7 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 0.414982236 0 0 0RH Relative Humidity % 3 4.744286712 0 0 0AP Barometric Pressure % 0.252 4.744286712 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.755956 ‐0.164985901 0.017421022 0.015555598O2exit Oxygen Concentration at preheater exit % 0.8 0.285476548 0.751510493 0.361451534 0.04602682NOx Nox Concentration at Boiler Exit % of reading 5 167.5533738 0.00035407 3.13415E‐06 0.003519539
Texitgas Exit Gas Temperature C 1.00028369 14.55572025 ‐3.33067E‐14 1.10997E‐27 2.35034E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.55572025 0.067264911 0.004527136 0.958615706
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 2.112622934 0.095230738 0.002267223 0.040476064
MSSP Main Steam Static Pressure % of reading 0.252 0.115861328 ‐0.056559061 0.000203145 4.29419E‐05SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 1.508369668 0.073497738 0.001350479 0.01229033
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.386515075 ‐0.007496484 0.001404932 8.39553E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 1.219614574 ‐0.076257945 0.001453819 0.008649986
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.400340623 0.018215451 0.000331991 5.31789E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.421434083 ‐0.15619625 0.006099317 0.004333118
FWSP Feedwater Static Pressure % of reading 0.252 0.26615805 ‐0.001771897 1.99378E‐07 2.22411E‐07CondtankL Condensate Tank Level % of reading 3 27.38504812 ‐3.33067E‐14 9.98402E‐27 8.31936E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.532223399 ‐3.33067E‐14 2.49601E‐27 2.6044E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 5.537660674 ‐2.60265E‐08 6.77381E‐14 2.07723E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 1.96192821
Plant Heat Rate Independent Parameters
1.661201493 1.043825608
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #8 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #8 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 0.708219146 0 0 0RH Relative Humidity % 3 2.995238957 0 0 0AP Barometric Pressure % 0.252 2.995238957 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.13952645 ‐0.164985901 0.017421022 0.000529916O2exit Oxygen Concentration at preheater exit % 0.8 0.338589116 0.751510493 0.361451534 0.064746468NOx Nox Concentration at Boiler Exit % of reading 5 38.78336216 0.00035407 3.13415E‐06 0.000188569
Texitgas Exit Gas Temperature C 1.00028369 14.79624873 ‐3.33067E‐14 1.10997E‐27 2.42866E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.79624873 0.067264911 0.004527136 0.990559088
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 1.72356568 0.095230738 0.002267223 0.026940768
MSSP Main Steam Static Pressure % of reading 0.252 0.870791453 ‐0.056559061 0.000203145 0.002425675SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 1.674652918 0.073497738 0.001350479 0.015149474
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.266061218 ‐0.007496484 0.001404932 3.97812E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 1.121888594 ‐0.076257945 0.001453819 0.007319302
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.262230948 0.018215451 0.000331991 2.28164E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.345208852 ‐0.15619625 0.006099317 0.002907402
FWSP Feedwater Static Pressure % of reading 0.252 0.946640191 ‐0.001771897 1.99378E‐07 2.8135E‐06CondtankL Condensate Tank Level % of reading 3 27.38504812 ‐3.33067E‐14 9.98402E‐27 8.31936E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.901761973 ‐3.33067E‐14 2.49601E‐27 4.01213E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 4.231274516 ‐2.60265E‐08 6.77381E‐14 1.21276E‐14Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 1.967329833
Plant Heat Rate Independent Parameters
1.661201493 1.053943201
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #9 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #9 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Symbol Description Units l Value Systematic Random Sensitivity Systematic Random
AT Ambient Temperature C 1 0.454352173 0 0 0RH Relative Humidity % 3 0.685202572 0 0 0AP Barometric Pressure % 0.252 0.685202572 0 0 0FC Fuel Carbon Content % of reading 1 0 0 0FN Fuel Nitrogen Content % of reading 1 0.003669639 1.34663E‐05 0
HHV Fuel Higher Heating Value % of reading 0.00167509 ‐0.154205975 6.67238E‐08 0O2ent Oxygen Concentration at preheater inlet % 0.8 0.206006199 ‐0.164985901 0.017421022 0.001155192O2exit Oxygen Concentration at preheater exit % 0.8 0.316361372 0.751510493 0.361451534 0.056524535NOx Nox Concentration at Boiler Exit % of reading 5 45.01793393 0.00035407 3.13415E‐06 0.000254068
Texitgas Exit Gas Temperature C 1.00028369 14.87643981 ‐3.33067E‐14 1.10997E‐27 2.45505E‐25TexitgasPH Exit Gas Temperature Postheater C 1.00028369 14.87643981 0.067264911 0.004527136 1.00132523
MSF Main Steam Flow 0.996010607MST Main Steam temperature C 0.5 2.853972776 0.095230738 0.002267223 0.073867593
MSSP Main Steam Static Pressure % of reading 0.252 0.85006612 ‐0.056559061 0.000203145 0.002311585SHAF Superheater Attemperator Flow 0.000568411HRHT Hot Reheat Steam Temperature C 0.5 2.004924398 0.073497738 0.001350479 0.021714206
HRHSP Hot Reheat Steam Static Pressure % of reading 5 0.251257338 ‐0.007496484 0.001404932 3.54775E‐06CRHAF Cold Reheat Attemperator Flow ‐0.000223285CRHT Cold Reheat Steam Temperature C 0.5 2.297582985 ‐0.076257945 0.001453819 0.030698178
CRHSP Cold Reheat Steam Static Pressure % of reading 1.00028369 0.252123364 0.018215451 0.000331991 2.10914E‐05FWF Feedwater Flow % of reading ‐0.056559061FWT Feedwater Temperature C 0.5 0.493496795 ‐0.15619625 0.006099317 0.005941689
FWSP Feedwater Static Pressure % of reading 0.252 0.925807572 ‐0.001771897 1.99378E‐07 2.69103E‐06CondtankL Condensate Tank Level % of reading 3 27.38504812 ‐3.33067E‐14 9.98402E‐27 8.31936E‐25
Prim Air Temp Primary Air temperature at boiler inlet C 1.5 1.800398079 ‐3.33067E‐14 2.49601E‐27 3.59584E‐27Prim Air Flow Primary Air Flow at boiler inlet % of reading 10 3.798482939 ‐2.60265E‐08 6.77381E‐14 9.77357E‐15Sec Air Temp Secondary Air temperature at boiler inlet C 1.5 0 ‐3.33067E‐14 2.49601E‐27 0Sec Air Flow Secondary Air Flow at boiler inlet % of reading 10 0 2.58123E‐08 6.66274E‐14 0
PB Unit Electrical Output at Generator Terminals % of reading 0.20985595 0.006511045 1.867E‐06 0PN Unit Electrical Output at Plant Output % of reading 0.20985595 ‐0.995864868 0.043676055 0
Mvar Unit Electrical Reactive Output % of reading 15 ‐0.000133004 3.98029E‐06 0PB12 Unit 12 Gross Output % of reading 0.20985595 0 ‐4.71457E‐05 9.78873E‐11 0
CEN Corrected Plant Heat Rate % 1.988318387
Plant Heat Rate Independent Parameters
1.661201493 1.092620523
Table 2.2 Summary of Results for Plant Heat RateCorrected Plant Heat Rate Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #10 con CARBON
Table 1.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Heat Rate
Symbol Description Units l Value Systematic Random Sensitivity Systematic Uncertainty
PB Unit Electrical Output at Plant Output % of reading 0.209855951 0.006511 1.867E‐06 0PN* Unit Gross Electrical Output % of reading 0.209855951 ‐0.9958649 0.043676055 0mvar Plant and Generator MVAR reading % of reading 0.209855951 ‐0.000133 7.79067E‐10 0PB12 Unit 12 Gross Output % of reading 0.209855951 ‐4.715E‐05 9.78873E‐11 0
PN* Corrected Plant Power Output % 0.208992637
Plant Output Independent Parameters
0.208992637 0
Table 2.2 Summary of Results for Plant Output
Plant Performance Test Post-test Uncertainty AnalysisCTM1 PUNTO #10 con CARBON
Table 2.1 Absolute Contribution of Systematic and Random Uncertainty of Independent Parameters on the Plant Output
Corrected Plant Output Calculated Result
Symbol Description Units
Calculated
Value
Absolute Systematic Uncertainty, BR
Absolute Random Uncertainty, tSR
Total Absolute Uncertainty, UR
EC-L – Mejillones CTM U1 Reporte de Determinacion de Consumo Neto Especifico Rev 00
Artículo 21 de la Resolución Exenta 363 - Prueba CEN Rendimiento de Planta
Apéndice C – Resumen de Datos
Data Summary
TP1 TP2 TP3 TP4 TP5 TP6Date 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016Start time 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m.End time 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m.
TP1 TP2 TP3 TP4 TP5 TP6Date 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016Start time 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m.End time 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m.
Output Generator Active Power kW 91,046.80 91,298.40 115,638.47 115,946.46 134,684.01 136,139.87Re‐active Power kVar 5221.073127 7107.393008 3609.793788 2803.437492 6005.684648 7108.22643
Net Power (exported to grid)Active Power Exported to Grid PN kW 81,678.34 81,970.33 105,124.64 105,460.05 123,845.63 125,282.08Re‐active Power Exported to Grid kVAR 4865.2 6757.0 3342.0 2530.9 5807.6 9269.2Power Factor PF 0.998230698 0.996619712 0.999495053 0.999712154 0.998902295 0.997274191Auxiliares de la Unidad Paux kW 9,554.56 9,521.04 10,743.91 10,742.61 11,126.21 11,189.79Auxiliares de la Unidad kVAR 7,561.07 7,554.74 7,991.43 8,000.15 8,161.83 8,182.38
Page 2 of 10
Data Summary
TP1 TP2 TP3 TP4 TP5 TP6Date 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016Start time 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m.End time 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m.
DCSST Gross Active Power TYE001MVC||XQ01 MW 91.04680267 91.2983967 115.6384696 115.9464631 134.6840105 136.1398657ST Gross Reactive Power TTMA||XQ01 Mvar 5.221073127 7.107393008 3.609793788 2.803437492 6.005684648 7.10822643Combustion air Temperature 1 TE‐BD45A||XQ01 C 312.3136465 313.2356403 322.9334813 324.5931617 336.3766522 337.8542632Combustion air Temperature 2 TE‐BD45B||XQ01 C 331.6067198 332.1420397 348.2610608 348.776033 360.6672845 361.0926705FW Flow (Fluxim ‐ Instrumento Temporal) kg/s 85.56042438 85.21703601 105.5015005 105.7906817 121.8177285 122.9438135
Temperature FW at Boiler Inlet (after APH 3) TE‐AH88||XQ01 C 212.0662175 212.1525677 223.860231 223.755244 231.9280047 232.4368727
Pressure FW at Boiler Inlet (inlet economizer) PT‐AH88||XQ01 barg 141.8188975 141.7263462 144.7629365 144.8187865 147.5468098 147.7935258Main Steam Temperature at Boiler Outlet 1 TE‐AA04||XQ01 C 520.3124042 520.1176087 519.2719488 520.3100245 518.9208042 519.3721513Main Steam Pressure at Boiler Outlet 1 PT‐AA04||XQ01 barg 136.5024215 136.4970668 137.6151043 137.519236 138.553202 138.61909Superheater Attemperator 1 Flow FT‐AH79||XQ01 kg/s 6.005963116 6.127155792 10.57367565 10.17073249 13.38480634 13.44210183Cold Reheat Temperature at Boiler Inlet 1 TE‐AC20||XQ01 C 335.3967965 335.2002845 328.5650528 328.3663312 319.9220905 318.143709Cold Reheat Pressure at Boiler Inlet 1 PT‐AC20||XQ01 barg 23.49600462 23.55396153 29.58624717 29.62771932 34.41463458 34.78969855Hot Reheat Temperature at Boiler Outlet 1 TE‐AB12||XQ01 C 521.155355 521.8031858 529.7912087 529.8775838 530.9143178 530.8538275Hot Reheat Pressure at Boiler Outlet 1 PT‐AB12||XQ01 barg 22.19365732 22.22177972 28.02566295 28.08124627 32.7158452 33.07159458Reheater Attemperator Flow FT‐AH80||XQ01 kg/s 0.019134341 0.019113142 0.938254962 1.007386285 1.936539528 2.128887771Superheater Attemperator pressure PT‐AH48||XQ01 barg 218.9462343 217.9396495 214.6560232 215.6686225 207.9097865 206.7491308Superheater Attemperator temperature TE‐AH78||XQ01 C 146.1147133 146.3012112 152.945249 153.4083073 159.3877227 159.9071228Aux Flow Steam pressure upstream of steam
valve PT‐AC32||XQ01 barg 14.02727236 14.01551733 14.00166426 14.01542447 13.99394813 14.00153443Aux Flow Temperature upstream of the aux valve C 198.3814216 198.3442915 198.3005053 198.3439981 198.2761028 198.3000948Aux Flow Steam Pressure in header barg 2.337878726 2.335919554 2.33361071 2.335904078 2.332324689 2.333589071Aux Flow Steam Temperature in header C 137.2023596 344.5956153 344.5956153 344.5956153 344.5956153 344.5956153Cooling Water Temperature‐1 TE‐DA11||XQ01 C 14.89176732 14.93495954 15.2214791 15.16310878 15.75304558 15.77035398Cooling Water Temperature‐2 TE‐DA12||XQ01 C 15.71216603 15.77326653 16.03487608 15.9997301 16.6483867 16.6346189Condensate Tank Level ‐ Final LT‐AF08||XQ01 mm 411.80148 408.97876 422.74377 413.46756 420.38947 427.6964Condensate Tank Level ‐ initial LT‐AF08||XQ01 mm 388.35132 390.23178 385.86914 387.80576 381.63193 378.21442Condenser Pressure‐1 PT‐AD70|256655|OUT bara ‐0.958572164 ‐0.958384938 ‐0.955687803 ‐0.955669394 ‐0.950750661 ‐0.950475647Heater # 2 Inlet Water Temperature TE‐AH85||XQ01 C 173.388111 173.5172535 182.2339707 182.3913868 188.858891 189.4371948Heater # 2 Outlet Water Temperature TE‐AH86||XQ01 C 210.4979633 210.601759 222.0948182 222.229276 230.9124257 231.6901003Heater # 2 Temperature (Steam) TE‐AC20||XQ01 C 335.3967965 335.2002845 328.5650528 328.3663312 319.9220905 318.143709Heater # 2 Pressure (Steam) PT‐AC20||XQ01 barg 23.49600462 23.55396153 29.58624717 29.62771932 34.41463458 34.78969855Heater # 2 Water Pressure PT‐AD40||XQ01 barg 23.14631258 23.20457368 29.17073283 29.20790762 33.93771783 34.31082147Heater # 2 Drain Water Temperature TE‐AD52||XQ01 C 40.04184337 40.00071792 42.324589 42.40852985 44.68367803 44.88703855
Page 3 of 10
Data Summary
TP1 TP2 TP3 TP4 TP5 TP6Date 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016Start time 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m.End time 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m.
Air Temperatures at Boiler boundaryTemperature Primary Air Inlet TE‐BP12||XQ01 C 136.2928618 136.843174 167.0566205 167.0091187 177.9952777 172.1414597Primary air flow‐total T/h 30.35475466 30.33592551 31.59993474 31.57878138 32.1863502 32.1863502Primary air flow‐A FT‐BP12||XQ01 T/h 11.42289153 11.38050517 10.4835582 10.49192225 10.09946971 10.09946971Primary air flow‐B FT‐BP22||XQ01 T/h 9.695641765 9.724775809 10.77071872 10.75183393 11.23563367 11.23563367Primary air flow‐C FT‐BP32||XQ01 T/h ‐0.212729063 ‐0.213609309 ‐0.212803471 ‐0.211885338 ‐0.210982506 ‐0.210982506Primary air flow‐D FT‐BP42||XQ01 T/h 9.448950432 9.444253833 10.5584613 10.54691053 11.06222932 11.06222932Temperature Secondary Air Inlet TE‐BD30||XQ01 C 279.8967883 280.641887 285.1099028 286.2671525 290.4783372 290.4783372Secondary airflow total FT‐BD30||XQ01 T/h 328.1553047 329.7196532 432.3403518 433.463157 512.7826123 522.7915863Boiler O2 Levels AIT‐BD52||XQ01 % 3.953943785 4.005576882 4.161499377 4.221612618 4.184611625 4.174405917Boiler O2 Levels 2 AIT‐BD72||XQ01 % 3.304387827 3.262635367 2.705696265 2.877181078 2.593635402 2.593635402Gases Leaving the boiler 1 TE‐BD45A||XQ01 C 312.3136465 313.2356403 322.9334813 324.5931617 336.3766522 336.3766522Gases Leaving the boiler 2 TE‐BD45B||XQ01 C 331.6067198 332.1420397 348.2610608 348.776033 360.6672845 360.6672845Gases Entering preheaters 1 TE‐BD04||XQ01 C 20.07326345 20.69267093 21.29723442 22.50623192 25.52520838 24.74904755Gases Entering preheaters 2 TE‐BD16||XQ01 C 19.35194122 20.355396 207.0331886 216.8429797 239.9129852 236.3095917
CEMS ValuesSOx Levels SO2_C(mg‐m3N): CEM CT ppm 127.7127049 130.8076066 137.0020656 127.587 135.0216311 137.0218525Nox Levels NOX_C(mg‐m3N): CEM C ppm 175.3756689 173.853177 167.3016033 177.8246131 179.7439246 183.3476951
TP1 TP2 TP3 TP4 TP5 TP6Date 06/07/2016 06/07/2016 05/07/2016 05/07/2016 05/07/2016 05/07/2016Start time 09:45:00 a. m. 10:45:00 a. m. 10:30:00 a. m. 11:30:00 a. m. 02:30:00 p. m. 03:30:00 p. m.End time 10:45:00 a. m. 11:45:00 a. m. 11:30:00 a. m. 12:30:00 p. m. 03:30:00 p. m. 04:30:00 p. m.
StabilityGenerator Power TYE001MVC||XQ01 % 0.314682966 0.55328916 0.75902611 0.592823045 0.51843631 0.371256578Flujo de Agua de alimentacion 1 % 0.027244144 0.026281538 0.030896741 0.032011805 0.024236991 0.018701448Flujo de combustible 1 FT‐BP26A||XQ01 % 0.037598316 0.044172965 0.035572389 0.034158009 0.030993009 0.028478811Flujo de combustible 2 FT‐BP26B||XQ01 % 0.006165679 0.006479967 0.009318931 0.008870955 0.010663812 0.008313997Flujo de combustible 3 FT‐BP26C||XQ01 % ‐40.95218752 ‐48.06338125 ‐32.16434883 ‐48.41102958 ‐48.22290891 ‐31.99396173Flujo de combustible 4 FT‐BP26D||XQ01 % 0.037479797 0.034277342 0.033235105 0.043429568 0.032391648 0.029459388
Temperatura del vapor principal 1 (max‐min) TE‐AA04||XQ01 C ‐1.81427 ‐2.74033 ‐6.7291 ‐8.93994 ‐4.51704 ‐3.57203Temperatura del agua de alimentacion TE‐AH88||XQ01 C ‐0.61591 ‐0.7856 ‐1.04338 ‐1.22998 ‐0.78 ‐0.59155Presion del vapor principal 1 PT‐AA04||XQ01 % 0.044759331 0.049839021 0.064959315 0.055889756 0.030646413 0.02731808
Production of Total CaSO3MW of S g/mol 32.065 32.065 32.065 32.065 32.065 32.065MW of SO2 g/mol 64.066 64.066 64.066 64.066 64.066 64.066MW CaSO3 g/mol 120.17 120.17 120.17 120.17 120.17 120.17Fuel Sulfur content mol/kgfuel 1.63247E‐05 1.63247E‐05 1.59331E‐05 1.59331E‐05 1.57735E‐05 1.57735E‐05Total SO2 produced mol/kgfuel 1.63247E‐05 1.63247E‐05 1.59331E‐05 1.59331E‐05 1.57735E‐05 1.57735E‐05Total SO2 produced kg/kgfuel 1.045856721 1.045856721 1.020772279 1.020772279 1.010545995 1.010545995Captured SO2 kg/kgfuel 0.891205096 0.88879879 0.875462107 0.885462904 0.854663029 0.854656654Captured SO2 mol/kgfuel 1.39107E‐05 1.38732E‐05 1.3665E‐05 1.38211E‐05 1.33404E‐05 1.33403E‐05Total CasO3 produced in residue mol/kgfuel 1.39107E‐05 1.38732E‐05 1.3665E‐05 1.38211E‐05 1.33404E‐05 1.33403E‐05Total CasO3 produced in residue kg/kgfuel 1.671652926 1.667139366 1.642123458 1.660882171 1.60311017 1.603098212
Output Generator Active Power kWRe‐active Power kVar
Net Power (exported to grid)Active Power Exported to Grid PN kWRe‐active Power Exported to Grid kVARPower Factor PFAuxiliares de la Unidad Paux kWAuxiliares de la Unidad kVAR
DCSST Gross Active Power TYE001MVC||XQ01 MWST Gross Reactive Power TTMA||XQ01 MvarCombustion air Temperature 1 TE‐BD45A||XQ01 CCombustion air Temperature 2 TE‐BD45B||XQ01 CFW Flow (Fluxim ‐ Instrumento Temporal) kg/s
Temperature FW at Boiler Inlet (after APH 3) TE‐AH88||XQ01 C
Pressure FW at Boiler Inlet (inlet economizer) PT‐AH88||XQ01 bargMain Steam Temperature at Boiler Outlet 1 TE‐AA04||XQ01 CMain Steam Pressure at Boiler Outlet 1 PT‐AA04||XQ01 bargSuperheater Attemperator 1 Flow FT‐AH79||XQ01 kg/sCold Reheat Temperature at Boiler Inlet 1 TE‐AC20||XQ01 CCold Reheat Pressure at Boiler Inlet 1 PT‐AC20||XQ01 bargHot Reheat Temperature at Boiler Outlet 1 TE‐AB12||XQ01 CHot Reheat Pressure at Boiler Outlet 1 PT‐AB12||XQ01 bargReheater Attemperator Flow FT‐AH80||XQ01 kg/sSuperheater Attemperator pressure PT‐AH48||XQ01 bargSuperheater Attemperator temperature TE‐AH78||XQ01 CAux Flow Steam pressure upstream of steam
valve PT‐AC32||XQ01 bargAux Flow Temperature upstream of the aux valve CAux Flow Steam Pressure in header bargAux Flow Steam Temperature in header CCooling Water Temperature‐1 TE‐DA11||XQ01 CCooling Water Temperature‐2 TE‐DA12||XQ01 CCondensate Tank Level ‐ Final LT‐AF08||XQ01 mmCondensate Tank Level ‐ initial LT‐AF08||XQ01 mmCondenser Pressure‐1 PT‐AD70|256655|OUT baraHeater # 2 Inlet Water Temperature TE‐AH85||XQ01 CHeater # 2 Outlet Water Temperature TE‐AH86||XQ01 CHeater # 2 Temperature (Steam) TE‐AC20||XQ01 CHeater # 2 Pressure (Steam) PT‐AC20||XQ01 bargHeater # 2 Water Pressure PT‐AD40||XQ01 bargHeater # 2 Drain Water Temperature TE‐AD52||XQ01 C
StabilityGenerator Power TYE001MVC||XQ01 %Flujo de Agua de alimentacion 1 %Flujo de combustible 1 FT‐BP26A||XQ01 %Flujo de combustible 2 FT‐BP26B||XQ01 %Flujo de combustible 3 FT‐BP26C||XQ01 %Flujo de combustible 4 FT‐BP26D||XQ01 %
Temperatura del vapor principal 1 (max‐min) TE‐AA04||XQ01 CTemperatura del agua de alimentacion TE‐AH88||XQ01 CPresion del vapor principal 1 PT‐AA04||XQ01 %
Production of Total CaSO3MW of S g/molMW of SO2 g/molMW CaSO3 g/molFuel Sulfur content mol/kgfuelTotal SO2 produced mol/kgfuelTotal SO2 produced kg/kgfuelCaptured SO2 kg/kgfuelCaptured SO2 mol/kgfuelTotal CasO3 produced in residue mol/kgfuelTotal CasO3 produced in residue kg/kgfuel