1920 Plant Specs
 

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The following figures relate specifically to the period until 1st May 1929 and concentrate particularly on the installation of what at the time was called the High Pressure section. Subsequently this became known as the Medium Pressure section.
     
The Boiler Plant    
     
     
Stirling 5 Drum Boilers 9 & 10 - Installed 1928 - 1929    
Induced Draft Fan 1  
Heating Surface 7,437 square feet
Evaporation Rate (greater than) 40,000 lb per hour
Feed Water Inlet Temperature 100 °F
Steam Pressure 265 lb per square inch
Steam Final Temperature 650 °F
Steam Drum Diameter 42 ins
Steam Drum Length 17' 1 ft ins
Water Drum Diameter 36 ins
Boiler Tubes - Diameter - No 9 Wire Gauge 3¼ ins
Chain Grate Stokers (2 off) - Babcock and Wilcox 16 x 6 ft (l x w)
Economiser Tubes - 160 off Cast Iron 12 ft (l)
Flue Stack Diameter 4' 9 ft ins
Flue Stack Height 60 ft
Coal Bunkers (Split in two for coal and coke) 50 tons
Feed Water Tank - Two Compartments - heated by exhaust steam 15 ft head
Steam Turbine Feed Pumps (2 off) - exhaust to FW tank 120,000 lbs water per hour
Electric Feed Pump - feed either Boiler Group 80,000 lbs water per hour
     
     
Stirling 5 Drum Boilers 5 to 8 - Similar design - Installed 1924 - 1926    
Induced Draft Fan (shared by two boilers) 1 per 2 boilers
Evaporation Rate 25,000 lbs per hour
Feed Water Inlet Temperature 100 °F
Steam Pressure 165 lb per square inch
Final Steam Temperature 540 °F
Flue Stack Diameter (shared by two boilers) 5 ft
Flue Stack Height 90 ft
Feed Water Tank - Two Compartments - heated by exhaust steam 15 ft head
Steam Turbine Feed Pumps (2 off) - exhaust to FW tank 100,000 lbs water per hour
     
     
The Turbine Plant    
     
British Thomson-Houston Turbo-Alternator No 5 Installed 1929 7,500 kilowatt 90% pf
RPM - Curtis Impulse Wheel design 3000 rpm
Phases 3 phase
Periodicity 50 cycles per second
Terminal Voltage 11,000 volts
Steam Inlet Pressure 250 lb per square inch
Steam Inlet Temperature 650 °F
Exhaust Back Pressure (Vacuum) 1.25 ins of mercury
Steam Consumption 90% Power Factor 7500 kw MCR 10.73 lb per KW hr
Steam Consumption 90% Power Factor 6000 kw ECR 10.69 lb per KW hr
Steam Consumption 90% Power Factor 4500 kw 10.97 lb per KW hr
Steam Consumption 90% Power Factor 3000 kw 11.63 lb per KW hr
Turbo-alternator weight (ex condenser) 95 tons
Protective Reactance 15 per cent
Tirril Automantic Voltage Regulator ±1 per cent
     
     
British Thomson-Houston Turbo-Alternators No 3 & 4 Installed 1924 & 1926 3,750 kilowatt
Terminal Voltage 11,000 volts
Steam Inlet Pressure 150 lb per square inch
Steam Inlet Tempersture 540 °F
Exhaust Back Pressure (Vacuum) 1.5 ins of mercury
Steam Consumption 90% Power Factor 3750 kw MCR 12.93 lb per KW hr
Steam Consumption 90% Power Factor 3000 kw ECR 12.89 lb per KW hr
Steam Consumption 90% Power Factor 2250 kw 13.28 lb per KW hr
Steam Consumption 90% Power Factor 1500 kw 14.08 lb per KW hr
Steam Consumption 90% Power Factor  750 kw 16.52 lb per KW hr
     
British Thomson-Houston Turbo-Alternators No 1 & 2 - Ex Torquay 1924 1250 kw
Steam Inlet Pressure 150 lb per square inch
Steam Inlet Temperature (via a de-superheater) 500 °F
RPM 3000 rpm
Phases 1 phase
Terminal Voltage 2000 volts
     
Condensing Plant - Generator 5    
Steam Condensed per hour 64,100 lb per hour
Cooling Surface Area 6,780 square ft
Vacuum at Exhaust Inlet 28¾ ins
Circulating Water 405,000 gals per hour
Circulating Water Inlet Design Temperature 60 °F
Extraction Pump 6.8 BHP
     
Riverside Pumps    
No 1 Pump House - 3 pumps - Turbo-Alternators 1 - 4 inclusive 150,000 gals per hour each
     
No 2 Pump House - 2 pumps - Turbo-Alternator 5 and future extensions 500,000 gals per hour each