Consumo de Combustible

A continuación, se muestran los requisitos estimados de suministro de combustible a plena y media carga de gas natural y vapor de LP.

Gas Natural

Vapor de PL

 

 

 

 

1/2 Carga

Carga completa

1/2 Carga

Carga completa

 

 

 

 

84 C

162 C

35 C

65 C

 

 

 

 

84,000 B

162,000 B

86,375 B

163,625 B

 

 

 

 

C = en pies cúbicos por hora

B = BTU por hora

Dimensiones de la Cañería de Combustible

Las tablas siguientes indican la capacidad máxima del tubo en pies cúbicos de gas por hora para presiones de gas de 0,5 psi o inferiores y una caída de presión de 0,3 pulgadas en la columna de agua. Se indica la densidad específica del gas.

En los valores indicados se ha tenido en cuenta una cantidad normal de restricciones debidas a curvas, accesorios, etc. Si se utiliza un número inusual de accesorios, curvas u otras restricciones, consulte los reglamentos nacionales y locales.

Propiedades físicas

Vapor de

Gas

 

PL

Natural

Estado normal a presión

Gas

Gas

atmosférica

 

 

Punto de ebullición (en °F):

 

 

Inicia

-44

-259

Fina

-44

-259

Poder calorífico:

 

 

BTU por galón (LHV Neto*)

83,340

63,310

BTU por galón (bruto**)

91,547

 

Pies cúbicos (gas)

2,500

1,000

Densidad***

36.39

57.75

Peso†

4.24

2.65

Número de octanos:

 

 

De investigación

110+

110+

Motor

97

 

* LHV (poder calorífico inferior) es el valor nominal más realista. ** El poder calorífico bruto no considera la pérdida de calor en forma

de agua durante la combustión.

*** La densidad se expresa en “Pies Cúbicos de Gas por Galón de Líquido”.

† El peso se indica en “Libras por Galón de Líquido”.

NPT

10ft

15ft

20ft

30ft

40ft

50ft

60ft

70ft

80ft

90ft

100ft

 

 

 

 

 

 

 

 

 

 

 

 

3/4”

346

293

240

192

163

145

132

120

113

106

99

 

 

 

 

 

 

 

 

 

 

 

 

1”

653

549

446

360

307

274

250

230

211

197

187

 

 

 

 

 

 

 

 

 

 

 

 

Tamaño del tubo de gas natural - Diagrama de flujo de gas, en pies cúbicos por hora, densidad específica=0,65

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

NPT

10ft

15ft

20ft

30ft

40ft

50ft

60ft

70ft

80ft

90ft

100ft

 

 

 

 

 

 

 

 

 

 

 

 

3/4”

277

192

158

126

107

95

87

79

74

69

65

 

 

 

 

 

 

 

 

 

 

 

 

1”

428

360

293

236

202

180

164

151

139

129

123

 

 

 

 

 

 

 

 

 

 

 

 

Tamaño del tubo de propano líquido (LP) - Diagrama de flujo de gas, en pies cúbicos por hora, densidad específica=1,50

Tamaño del Tanque de Propano Requerido

Considerando la tasa de consumo de gas y la temperatura mínima promedio durante el invierno, un instalador puede especificar el tamaño necesario del tanque de almacenamiento de PL:

Tasa de consumo

32° F

20° F

10° F

0° F

-10° F

-30° F

-40° F

 

 

 

 

 

 

 

 

50 pies cúbicos/h

115

115

115

250

250

400

600

 

 

 

 

 

 

 

 

100 pies cúbicos/h

250

250

250

400

500

1000

1500

 

 

 

 

 

 

 

 

150 pies cúbicos/h

300

400

500

500

1000

1500

2500

 

 

 

 

 

 

 

 

200 pies cúbicos/h

400

500

750

1000

1200

2000

2500

 

 

 

 

 

 

 

 

300 pies cúbicos/h

750

1000

1500

2000

2500

4000

5000

 

 

 

 

 

 

 

 

12

BRIGGSandSTRATTON.COM

Page 28
Image 28
Briggs & Stratton 10000 Watt Consumo de Combustible, Gas Natural Vapor de PL, Dimensiones de la Cañería de Combustible

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