Using the figures from Example 3.12.5, if the boiler had been operating at 10 bar g, steaming at 5 000 kg/h and had a feedwater temperature of 80°C (hf = 335 kJ/kg), the change in energy requirement could be calculated as follows: Condition 1, manual TDS control: Blowdown rate = 11.1%. Example 3.12.7. Condition 2, automatic TDS control :

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Using the figures from Example 3.12.5, if the boiler had been operating at 10 bar g, steaming at 5 000 kg/h and had a feedwater temperature of 80°C (hf = 335 kJ/kg), the change in energy requirement could be calculated as follows: Condition 1, manual TDS control: Blowdown rate = 11.1%. Example 3.12.7. Condition 2, automatic TDS control :