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Waste heat recovery Optimizing

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Waste heat recovery Optimizing ( waste-heat-recovery-optimizing )

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Example: Feed preheating in direct fired heater/furnace In this example heat from a process gas stream is recovered and used for preheating the feed gas of a direct fired heater. A shell- and-tube is replaced by a compact heat exchanger, increasing heat recovery and reducing gas consumption. The result is an increase in heat recovery by 1.7 MW (5.814 MMBtu/h). Figure 3.7 Direct process heat integration before and after revamp. Before Feed gas after heater 300°C (572°F) Hot process gas 165°C (329°F) Preheated feed gas 180°C (356°F) After Feed gas after heater 300°C (572°F) Preheated feed gas 225°C (437°F) Hot process gas 250°C (482°F) Hot process gas 130°C (266°F) Direct fired heater/ furnace Hot process gas 250°C (482°F) Direct fired heater/ furnace Cold feed gas 50°C (122°F) Cold feed gas 50°C (122°F) 1.7 MW (5.8 MMBtu/h ) increased heat recovery 36

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